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Authority agrees
S.P:
STUDY
ENERGY EFFICIENCY ADN
BIOMASS POTENTIAL ANALYSIS
PURCHASER: UNDP - SERBIA
OBJECT: PUBLIC BUILDINGS
INVESTOR:
LOCATION: Municipality: Kuĉevo
DOCUMENT: STUDY
RECORD NO.: SI - 06 / 2012
DATE: 15.11.2012.
PLACE: NOVI SAD
PERPETRATOR:
RESPONSIBLE DESIGNER:
Bratislav Milenković B. Sc. Mech. Eng.
PROJECT MANAGER:
Ph. D. Todor Janić
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Kaće Dejanović 52
21000 Novi Sad
Serbia
Mob: +381-64-160-99-96
Phone: +381-21-496-320
Fax: +381-21-496-320
E-mail: [email protected]
The contracting authority of study:
UNDP – Srbija, Internacionalnih Brigada 69, Beograd
Title of the study:
ENERGY EFFICIENCY AND BIOMASS POTENTIAL ANALYSIS
Authors of the study:
Prof. dr Todor Janić, Ph.D.
Bratislav Milenković, B. Sc. Mech. Eng.
Prof. dr Miladin Brkić, Ph.D.
Zoran Janjatović, B. Sc. Agro Ecc.
Msc. Darijan Pavlović, M. Sc. Agro Ecc.
Jelena Vurdelja, B. Sc. Agro Ecc.
Ivan Tot, dipl. ing, B. Sc. Agro Ecc.
1
CONTENT
REWIEW OF TABLE 3
REVIEWOF FIGURES 5
TASK 1 – Analysis of the available biomass energy resources in Munucipality of Kuĉevo 7
1.1. Analysis of available biomass resources in the municipality of Kuĉevo and quantitative
aspects of thermal energy that can be used for energy purposes 7
1.2 Type, form and price of available biomass as an energy source 13
TASK 2 – Analysis of thermal energy required in selected facilities for public use 24
2.1. The choice of public facilities in Kuĉevo location that will be heated by biomass 24
2.2 Technical features of the heating system with heat loss analysis overview for selected
public facilities in Kuĉevo municipality 27
2.2.1. Primary School „Veljko Dugoševiće“ u Turiji 27
2.3.Analysis of the measures for the increase of energy efficiency in buildings for public
use 33
2.3.1 Power consumption in coplex ES„Veljko Dugošević“ in Turiji andsuggestions of
practical measures for increasing the energy efficiency of facility 34
TASK 3 – Techno-economic analysisfor thermal facility which uses biomass as a fuel, for
heating chosen buildings 42
3.1.Technologyof available biomass form combustion 42
3.2. Selection of combustion technologies and technical solutions for the thermal power
plants and defining the maximum boiler plant thermal power for continuous heating of
public buildings 42
3.3. Definingthe optimalplacefor the construction ofthermal powerplants(with
thetechnical,economic and environmentalaspects) 43
3.4. Technical description of the biomass boiler facility (thermo-technical equipment, boiler
room, hot water piping) with the extended bill of quantities for the Kuĉevo municipality,
along with the expected energy and ecology efficiency 44
3.4.1. Expected energy efficiency and ecological efficiency for biomass combustion in
boiler facilities 47
3.4.2. Marginal values of gas emission for specific types of furnaces 49
3.5. Necessary amount of biomass for hourly and seasonal work of the boiler facility 51
3.5.1. Hourly consumption of biomass 51
2
3.5.2. Seasonal consumption of biomass 51
3.6. Economic analyses of construction the heating facility 53
3.6.1. Current price of the heating energhy from the used components 53
3.6.2. Financial effectiveness with the profitability analyses 54
3.6.3. Economic evaluation of the project 66
3.6.4. Summarized economic feasibility investment evaluation 67
3.7. Conclusions 68
3.8. Literature 72
4. APPENDIX 76
3
REWIEW OF TABLE
Table 1. Overview of biomass obtained from cereal and industrial crop production in Kuĉevo
municipality (Municipalities and regions of the Republic of Serbia (2011))
Table 2. Overview of biomass obtained from orchards and vineyards in Kuĉevo municipality
Table 3. Energy potential from manure in Kuĉevo municipality
Table 4. Biomass productionin forestryandwood industry (m3)
Table 5. Communal waste availability in Kuĉevo municipality
Table 6. Biomass type, amounts available, usage percent, equivalent amounts of liquid fuel
and savings amount.
Table 7. Prices of different forms of biomass bales
Table 8. Price of briquettes from agricultural biomass 400 gr/com.
Table 9. The price of pellets from agricultural biomass 20 gr/com.
Table 10. Chips from waste woodfrom the forest and cut fire wood second class
Table 11. The pelletsfrom wastewoodfrom theforest andcutfire woodsecond class - 20 gr/com.
Table 12. List of companies engaged in the production and distribution of pellets
Table 13. Transport costs of pellets from producer to municipalities Kuĉevo (Turija)
Table 14. View of room heat lossof the school building
Table 15. Display summaries of the complex ES "Veljko Dugošević" in Turija
Table 16. Display power consumption based on kWh
Table 17. Display seasonal fuel consumption of the existing boiler and the savings that can be
achieved by applying technical - organizational measures to increase efficiency
Table 18. Possible harmful effects of certain elements and corrective technologicalmeasures
Table 19. Maximum allowed levels (MAL) of smoke gases in air for work and life
environment (SRPS Z.BO 001)
Table 20. Borderline emission values (BEV) for small solid fuel combustion facilites
(Regulation, Official Gazette of the Republic of Serbia, No. 71/2010)
Table 21. Marginal values of emissions(MVE) for small facilities for the combustion of gas
fuel (Regulation, “Official Gazette of the Republic of Serbia”, no 71/2010)
4
Table 22. Marginal values of emissions (MVI) of gases, soot, suspended particles and
heavy metals, sediment andaerosediment content, (Rulebook, “Official Gazette of the
Republic of Serbia”, no 54/92, 30/99 and 19/2006)
Table 23. Analyses of the quantity and prices of heating energy for the period 2011/2012
Table 24. Structure of the total investment
Table 25. Cost projection of 1kWh of required energy
Table 26. Income statement - current operations
Table 27. Projected income statement - first year of operations
Table 28. Depreciation calculation
Table 29. Financial cash-flow
Table 30. Loan repayment plan
Table 31. Economic flow of the project
Table 32. Time of return of investments
Table 33. Internal rate of return calculation
Table 34. Relative net present value calculation
Table 35. Profitability break even point
Table 36. Dynamic sensitivity analyses
Table 37. Potential risk analyses
Table 38. Anylizes of the cost savings vs. new investments
5
REVIEWOF FIGURES
Figure 1. The position of the municipality Kuĉevo compared with other municipalities of
Braniĉevo district
Figure 2. Structure of the savings that can be achieved in the municipality Kuĉevo using
biomass
Figure 3. Direcorate of Public communal enterprise Kuĉevo building
Figure 4. House of Culture“Veljko Dugošević” in Kuĉevo
Figure 5. Elementary school “Veljko Dugošević” in Turija
Figure 6. Exterior school wall, 45 cm thick
Figure 7. Exterior school wall, 30 cm thick
Figure 8. Exterior wall of the upgrade
Figure 9. Interior bearing wall
Figure 10. Interior dividing wall, 15 cm thick
Figure 11. Interior wall, 30 cm thick
Figure 12. Floor in the classrooms in the ground floor
Figure 13. Floor in the corridors in the ground floor
Figure 14. Floor in the upgraded part of the school, in the ground floor
Figure 15. Floor above the open area of the school
Figure 16. Floor on the story
Figure 17. Floor in the upgraded part on the story
Figure 18. Ceiling on the story
Figure 19. Ceiling in the upgraded part on the story
Figure 20. Windows in the school
Figure 21. School entrance
Figure 22. “ALFA PLAM” furnace, type “Vulkan”
Figure 23. “ALFA PLAM” furnace, type “Rustik”
Figure 24. Furnace in the classroom
Figure 25. Wood storage
6
Figure 26. Appropriateness of tehnological and tehnical solutions for biomass combustion
Figure 27. The schematics of the boiler facility wich burns wood pellets
Figure 28. Jumbo bag
Figure 29. Crain truck
7
TASK 1 – Analysis of the available biomass energy
resources in Munucipality of Kučevo
Inthis section – Task 1,it was necessary torealize theresearch ofthe literatureand field
workandthe resultsshowin a separatesection of the report.
In Task 1 need to do a detailed analysis biomass resources and potential as follows:
Provide an estimation of potential amount (quantity) of biomass available from forest,
wood industry, agriculture and food industry, which canbe usedfor energy purposes and
disaggregate per ownership typethat do not have damagingconsequences forthe
environment;
Provide an estimation of thermo-energy potentials of actual biomass potentials and
energy crops (including environment impact aspects);
Define dynamicsandformof collectingbiomass;
Propose location and storage methods for collected biomass;
Provide range of options for biomass utilization for energy purposes;
Provide a list of potential suppliers of biomass to boiler faciliti in accordadance with the
continuity of biomass production, type and quantity of available biomass, transportation
cost.
1.1. Analysis of available biomass resources in the municipality of Kučevo
and quantitative aspects of thermal energy that can be used for energy
purposes
Kuĉevo municipality is located in Eastern Serbia on the rim of Braniĉevo district (Figure 1),
coinciding with the middle of flow route of the river Pek. The river Pek and two important
roads transect the municipalities‟ territory. These roads are the M-24 road, Poţarevac -
Majdanpek – Negotin road and Beograd - Poţarevac - Majdanpek – Zajeĉar railway. Total
road length is 234 km.
The climate is humid continental with temperatures averaging at +11°C, the lowest being -
27°C and the highest +40°C. Annual precipitation amounts to 663-756 mm/year.
The center of the municipality is the city of Kuĉevo, with 25 villages located around it:
Blagojev Kamen, Brodica, Bukovska, Velika Bresnica, Voluja, Vuković, Duboka, Zelenik,
Kaona, Kuĉajna,Lješnica, Mala Bresnica, Mišljenovac, Mustapić, Neresnica, Rabrovo,
8
Ravnište, Radenka, Rakova Bara, Sena, Srpce, Turija, Ceremošnja, Cerovica and
Ševica.Kuĉevo city is located in the fertile Zviţd basin where southern slopes of
ZviţdMountains meet northern slopes of HomoljeMountains. According to 2011 census,
22.290 people live in 6.360 households, in 26 populated places. The city of Kuĉevo is the
biggest populated place in the area, representing at the same time the main administrative
center with 4.823 people in 2.218 households. The most important companies in the area are
‟‟Šik Kuĉevo‟‟ (wood industry), known for its waterproof plywood, and ‟‟USS Balkan‟‟,
leading stone and lime production plant in Serbia. Furthermore, an important factor in the
economy is agriculture, most importantly animal husbandry because of vast areas under
quality pastures.
Figure 1. The position of the municipality Kuĉevo compared with other municipalities of
Braniĉevo district
Agricultural land in Kuĉevo municipality is structured as follows:Arable land and gardens are
spread over 17.560 ha (cereals on 11.870 ha, industrial crops on 31 ha, vegetable farming on
571 ha, fodder crops on 2.603 ha, orchards on 2.348 ha and vineyards on 137 ha), meadows
over 8.773 ha and pastures over 7.421,6 ha. In total, it amounts to 32.215 ha. Forests strech
along 35.915 ha.
The share of major crops in the municipality of Kuĉevo sowing structure is shown in Table 1.
Table 1. Overview of biomass obtained from cereal and industrial crop production in Kuĉevo
municipality (Municipalities and regions of the Republic of Serbia (2011))
Crop Planted
area Average
yield Biomass
price Calorific
value Available energy
per year
Diesel to be
substituted per year
Fuel oil equivalent
(ha) (t/ha) (€/t) (MJ/t) (MJ) (t) (-)
Corn 6.600 5,4 41,9 13.500 48.114.0000 9.882,21 9.677,79
Wheat 4.150 3,2 34,9 14.000 185.920.000 3.818,64 3.739,65
Barley 1.100 3,0 35,2 14.200 46.860.000 962,46 942,56
Sunflower 20 1,9 38,5 14.500 1.102.000 22,63 22,17
TOTAL: 11.870 - - - 715.022.000 14.685,95 14382,17
9
As shown in Table 1, out of 17,560 ha allocated for agricultural production in Kuĉevo
municipality, leading crops which can be used for energy purpose are grown on 11.870 ha.
Leading crops are corn, wheat, barley and sunflower. Cornis planted on the majority of the
land, 6,600 ha exactly, followed by wheat on 4,150 ha, barley on 1,100 ha and sunflower on
20 ha. It is estimated that 52,296 t of crop biomass could be obtained annually from this area.
Average price of biomass is 39.75 €/t. Average calorific value of biomass is 13.651 kJ/kg. If
all of the available biomass should be converted to energy, it would yield 715,022,000 MJ,
with straw combustion energy efficiency coefficient of 0.80. Since diesel fuel has a calorific
value of 41 MJ/kg and the liquid fuel combustion energy efficiency coefficient is 0.95,
calculations show that this amount of biomass could substitute 14,685.95 t of diesel per year.
In order to convert these values and express them in fuel oil obtained from biomass per year, a
slightly higher calorific value of fuel must be used (41,866 MJ/kg). Thus, the amount of fuel
oil obtained from biomass would be 14,382.17 t per year. If diesel fuel price is assumed to be
1,36€/l or 1,60 €/kg, we come to an annual figure of 23,497,520 €. Sure enough, not all of the
available biomass would be used to produce heat energy, for several reasons: there is an
obligation to put some biomass back to the ground through plowing and thus increase soil
fertility, some of the biomass will be used for animal bedding, some of it for vegetable
farming and other purposes. Furthermore, it is assumed that 15% of the biomass could be used
for production of heat energy annually. This amounts to 7,844.4 t of biomass or 2,611.8 t of
fuel oil per year. Converted to money, the energy savings per year amount up to 4,178,884 €.
Table 2offers an overview of biomass production in orchards and vineyards.
Table 2. Overview of biomass obtained from orchards and vineyards in Kuĉevo municipality
Fruit and
grapevine
Planted
area
Number
of trees
Biomass
from pruning*
Biomas
s price
Calorifi
c value
Available
energy per year
Diesel to be
substituted per year
Fuel oil
equivalent
(ha) (kom) (t) (€/t) (MJ/t) (MJ) (t) (-)
Apple 33,4 26.250 96,4 35,50 15.300 1.474.968 30,29 29,67
Plum 501 290.000 1837,9 35,50 15.800 29.038.425 596,42 584,09
Grapevine 137 315.000 215,9 32,80 14.000 3.023.055 62,09 60,81
TOTAL: 671,4 631.250 2.150,2 - - 33.536.448 688,81 674,56 * In orchards, fruit to pruned biomass ratiois 1:0,325
* In vineyards, fruit to pruned biomass ratiois 1:0,457
Fruit and grapevine are grown in this municipality. Main cultures grown here are: apple, plum
and grapevine. Total area under orchards and vineyards is 534,4 ha and 137 ha, respectively.
It is estimated that 2,150.2 t of biomass could be obtained by pruning orchards and vineyards
per year (3.20 t/ha).If an average calorific value of pruned biomass is assumed to be 15,596.8
kJ/kg and the firebox efficiency is 80%, 33,536,448MJ of energy could be obtained. This
amount of energy could substitute 688.8 t of diesel fuel or 764.6 t of fuel oil. This means that
savings achieved from using pruned biomass from orchards and vineyards would be around
1,102,080€ per year. Since it is impossible to collect all of the biomass, we can assume that at
least 50% of the savings could be achieved, that is 551.040€ per year.
Table 3 offers an overview of biomass production in animal husbandry.
10
Table 3. Energy potential from manure in Kuĉevo municipality
Livestock
Number
of livestock
Livestock units
Biogas per day
Biomass price
Biogas
available in 365 days
Available
energy per year
Diesel to be
substituted per year
Fuel oil equivalent
(kom.) (kom.) (Nm3/UG) (€/t) (Nm3) (MJ) (t) (-)
Cattle 2.670 2.225,00 1,2 7,2 1055762,5 24979340,8 548,3 537,0
Swine 7.000 1.166,66 1,3 9,50 638750,0 15112825,0 331,7 324,9
Sheep 8.900 674,24 1,1 7,2 270708,3 6404959,2 140,6 137,7
Poultry 64.500 215,00 2 10,0 156950,0 3713437,0 81,5 79,8
TOTAL: 83.070 4.280,90 - - 2122170,8 50210561,9 1102,2 1079,4
Note: Calorific value ofbiogas with 65% methane content - hd=23,66 MJ/Nm3, that is 35,8 MJ/kg.
Manure is a product of animal husbandry. It can be used for production of biogas as well as
soil fertilization. In this region people raise cattle, swine, sheep and poultry. Livestock
population in units is: 2.670 cattle units, 7.000 swine units, 8.900 sheep units and 64.500
poultry units. These numbers translated to livestock units values amount to 4,289.9 in total.
This number of livestock units can produce 2,122,170.8 Nm3of biogas per year
(495,7Nm3/livestock unit). If an average calorific value of biogas with 65% methane content
is assumed to be 23,66MJ/nm3, that is 35,8 MJ/kg of gas,and with 98% firebox efficiency,
50,210,561.9MJ of energy could be obtained. This amount of energy could substitute
1,102.18t of diesel fuel or 1,079.38 t of fuel oil. Thus, this amount of biogas could save
1,763,488€ per year. Again, not all of the manure is available for biogas production, mainly
because of direct soil fertilization, dissemination of farmers, problems with manure collecting,
and so on. It is estimated that 25% of manure could be used for heat production. This would
ensure 440,872€ of savings.
Kuĉevo municipality has 35.721 ha of forests.Timber potentialis 8.923.500 m3. Table 4 offers
an overview of production areas and wood biomass availability.
Table 4. Biomass productionin forestryandwood industry (m3)
Type of ownership structure
Area Average amount of
wood Volumetric
growth Technical
wood Forestry residues
(ha) (m3) (m3/ha) (m3)* (m3)**
National forests 18.674 36.000 4,9 21.600 14.400
Private forests 17.047 18.000 2,1 10.800 7.200
TOTAL: 35.721 54.000 3,75 32.400 21.600
Despite the great potential of forest wood in the municipality Kuĉevo average annual lumber
volume is 54.000 m3.When logging forest wood will give technical and stacked woodand the
rest - waste which includes:stump with roots, thin branches to 7 cm in diameter, bark from
logs and scrap wood cutting in order to obtain the appropriate dimensions and shapes of
commercial productscommonly used for energy.
It is estimated that the cutting and clearing of forests and wood after treatment in the timber
industry, the rest of the wood - the waste is about 40% of the volume of felled timber, which
would give a total amount of 21,600 m3 per year for 440 kg/m
3 bulk density. It can be
11
concluded that the municipalities Kuĉevo has specified annually from 9,504 t of waste wood
biomass.
Calorific value of wood residue is 15,50 MJ/kg. Combining this data, we can conclude that
the total energy value of wood residue available is 117,849,600MJ, with 80% firebox
efficiency. This amount of energy potentially substitutes 3,018 t of diesel fuel with 95%
firebox efficiency, or 3,081.9 t of fuel oil equivalent. With this much residue a 4,828,800€
saving could be made yearly. If only 50% of said residue was used, the savings would amount
to 2,414,400€ per year.
Table 5 offers an overview of communal waste availability in Kuĉevo municipality.
Table 5. Communal waste availability in Kuĉevo municipality
Amount
of waste Waste weight Organic waste
Organic (biodegradable)
waste weight
(t) (kg/resident/day) (%) (t)
AVERAGE: 3.707,2 0,6 55 2.039
Table 5 shows that the total amount of biodegradable communal waste in Kuĉevo
municipality is 2.039 t per year. If we assume that the calorific value of this waste is 12
MJ/kg, we can calculate its total energy value. This value is 17.127.600 MJ per year with 70%
firebox efficiency. Since the calorific value of diesel fuel is 41 MJ/kg with combustion energy
efficiency coefficient of 0,95 , calculation show that 396,9 t of diesel fuel could be substituted
yearly with this amount of waste. This is equal to 388,7 t of fuel oil. By incorporating the
diesel fuel price of 1,6 €/kg in the equation, we conclude that waste could generate a 621.904
€ saving. This biodegradable waste will not be used only to generate heat due to many
reasons, but there is an estimation that every year 30% of waste may be used for this purpose.
This is 611,7 t of waste (116,6 t of fuel oil) per year. The savings generated this way would
amount to 183.502€ per year (wasteat a cost 5 €/t).
Table 6 offers an overview of biomass type, amounts available, usage percent, equivalent
amounts of liquid fuel and savings amount.
To summarize, table 6 shows that using agricultural and wood biomass as well as communal
biodegradable waste may generate savings for Kuĉevo municipality. These savings are:
biomass from crops – 4,178,884€; biomass from fruit and vine production – 551,040€;
biomass from animal husbandry – 440,872€; biomass from forestry and wood industry –
2,414,000€; biomass from communal biodegradable waste – 183.502€; total of 7,768,698€
per year.
Structure of the savings that can be achieved in the municipality Kuĉevo if using available
biomass is shown in Figure 2.
Namely, a quarter or half of the total available biomass (depending of type of production) can
generate energy value of 200,637,244 MJ, or 55,732.6 MWh. If a thermal facility would
operate during 6 months of a year (4.390 hours), the facilities‟ power would be 12.7 MW. We
can safely assume that full capacity of the facility will not be used all the time during these 6
months, just when the temperatures are low. This shows that biomass consumption would be
12
considerably below 25% (or 50% out of total available biomass, depending of production
type). The surplus could be used for new facilities or other needs. A conclusion could be
made that Kuĉevo municipality has enough biomass to power an 25 MW thermal facility.
This conclusion is made according to the calculations that do not include firewood as a
conventional fuel, which availability is 60% out of total lumber. Biomass from crop
production, fruit and vine production, forestry and wood industry could be used as an
alternative fuel in one thermal facility, while the biomass from animal husbandry (manure)
and communal waste could be used in a biogas production facility.
Table 6. Biomass type, amounts available, usage percent, equivalent amounts of liquid fuel
and savings amount.
Biomass type
Biomass
amounts
available
Usage
percent
Used
amounts
of biomass
Equivalent
amount of
liquid fuel
Savings
amount
(t/god) (%) (t/god) (t/god) (€)
Crop production 52.296,0 15 7.844,4 2.611,8 4.178.884
Fruit and vine production 2.150,2 50 539,7 344,4 551.040
Animal husbandry 35.938,2 25 8.984,6 1.102,8 440.872
Forestry and wood industry 9.504 50 4.752 3.018,0 2.414.400
Communal waste 2.039,0 30 611,7 116,6 183.502
TOTAL: 101.927,4 22.732,4 7.193,6 7.768.698
Figure 2. Structure of the savings that can be achieved in the municipality Kuĉevo using
biomass
13
1.2 Type, form and price of available biomass as an energy source
According to data about available potentials of biomass and its structure, mentioned in
Chapter 1.1, we may conclude that the main quantity of biomass in Kuĉevo municipality may
be collected from agricultural and forest production. They have more than sufficient potentials
for public facilities heating.
Form of biomass that will burn in power plants was adopted with the aim to meet the different
requirements. In this election there were several priority policies. The most important factors
in determining the form of biomass that will burn were related to:
- Available surface for construction of the boiler room and biomass storage that
would ensure the properly work of a thermal power plant of a few days,
- Fire load,
- The amount of a destructive impact on the surrounding environment (emission of
gaseous products of combustion, noise, vibration, distribution of biomass in its
transportation and handling, etc..)
- The possibility and cost of transport from the warehouse to the boiler,
- The need to use extra funds to manipulate biomass
The calculation of prices of different sorts and forms of biomass, which is used for making
enough energy in these facilities, is formed according to expenses existing, from collecting
biomass to its burning in the facilities.
Four different systems are analyzed here:
o classic bales (small, conventional), weight: 10-12kg each,
o roll bales, weight: 80-150kg each,
o large prismatic bales, weight: 250-300kg each,
o big square bales, weight: 500kg each;
Briquette, weight: 400g each,
Pellets of agricultural biomass, weight 20gr each;
Chippings of the forests cutting and of the 2nd class fire wood, weight: 20 g each;
Pellets of the remains of the forests cutting and 2nd class fire wood, weight: 20g, each.
Analytical calculations of prices of agricultural biomass to the known cost categories
are not shown, as is extensive. In order to implement this study as the initial parameters
for biomass production rate calculations used extensively adopted data.
It is assumed that the initial price of agricultural biomass in the amount of 0.55 din/kg,
which is very doubtful, since there is no market of biomass and its value is in reality
ranges from 0 to 1 din/kg.
Determination of the purchase price of wood as material for combustion is easier,
because there is a market for the wood, where the average price in the purchase of large
quantities of wood in the long term is for the rest of the timber harvest activities 20€/t,
14
and fuelwood second class 30-35 €/ t. Based on these data, adopted price of waste wood
biomass is 2,9 din/kg.
It is assumed that the loading and stacking bales does 2 workers. Manipulation of roll
bales is with a front tractor loader. Loading and stacking bales in the warehouse is
provided by using front tractor loader with a special attachment for manipulation with
big bales.
In addition, it was necessaryto adopt the appropriate values of many variable and fixed
costs, such as:
- - price of machines involved in the process of preparation biomass
- - potential annual efficiency of machines (ha or hours)
- - economic useful life of machinery (depreciation)
- - operating costs,
- - maintenance costs,
- - equipment and organization of transport systems,
- - price wage workers,
- - insurance costs, interest,
- - average yield of biomass.
The calculated unit costs of various forms of biomass bales made from agricultural production
in Serbia that has adequate machinery and technology work are shown in table 7 (Table 7).
Table 7. Prices of different forms of biomass bales
Expenses of biomass bale
preparation Small prismatic
bales
Roll baless Large
prismatic
bales
Big square
bales
Type of cost Value
Weight of bale (kg/com.) 10 – 12 120 – 160 250–300 500
Straw price (din/kg) 0,55 0,55 0,55 0,55
Pressing (din/kg) 1,32 1,21 1,32 1,32
Loading (din/kg) 0,66 0,55 0,55 0,44
Shipping (din/kg) 0,55
(to 30 km)
0,66
(to 30 km)
0,66
(to 50 km)
0,55
(to 100 km)
Unloading and
stacking (din/kg) 0,66 0,55 0,55 0,44
Handling (din/kg) 0,11 0,11 0,22 0,22
TOTAL PRICE: (din/kg) 3,85 3,63 3,85 3,52
Prices of some forms of biomass are shown in Tables 8 do 11.
15
Table 8. Price of briquettes from agricultural biomass 400 gr/com.
Type of cost Price of cost(din/kg)
Price of straw bale 3,3 – 3,74
Mulching 2,2
Pressing 5,5
Packing 1,65
Storage 1,1
Shipping 2,2 (to 300 km)
Total price: 15,95 to 16,39
Table 9. The price of pellets from agricultural biomass 20 gr/com.
Type of cost Price of cost (din/kg)
Price of straw bale 3,3 – 3,74
Mulching 2,75
Pressing 6,6
Packing 1,1
Storage 0,55
Shipping 3,3 (to 200 km)
Total price: 17,6 to 18,04
Table 10. Chips from waste woodfrom the forest and cut fire wood second class
Type of cost Price of cost (din/kg)
The starting material 2,97
Transport to storage 1,76
Chipping 1,98
Storage 1,1
Transport to furnace 0,55
Total price: 8,25
Table 11. The pelletsfrom wastewoodfrom theforest andcutfire woodsecond class - 20 gr/com.
Type of cost Price of cost (din/kg)
The starting material 2,97
Transport to storage 1,76
Chipping 1,98
Fine grinding 1,32
Pressure (pelleting) 6,6
Packing 1,1
Storage 0,55
Transport 3,3 (to 200 km)
Total price: 19,58
16
The municipality Kuĉevo has 32,215 ha of agricultural land, but only 11,870 ha is arable land
from which biomass can be taken and used for energy purposes. On these surfaces, each year,
as the rest of the primary agricultural production remains 52,296 t of biomass. Using only a
small part of these biomass would be more than enough to heat all the public facilities in the
city Kuĉevo.
The said biomass made from primary agricultural production availability, with its low price
made it impossible to overlook in terms of being the best option for heating public facilities in
Kuĉevo municipality. Even with the benefits it offers, biomass generated in the process of
agricultural production was discarded as a fuel source for public facilities in Kuĉevo
municipality, for several reasons, which in shortest can be summarized as:
great number of small lots (1 to 5 ha) which are located mainly on mountainous terrain
reduces the possibility of usage and profitability of high capacity machines (roll press,
big bale press, etc.) for collecting and baling of straw. This implies that small
prismatic bales with profitability up to 30 km of transport, are to be used,
public facilities in Kuĉevo are located in the city centre,
roads in Kuĉevo are narrow with not much parking space outside of road lanes, which
leads to frequent road blocks due to parked cars on the road. This conditions would
greatly impair movement of special vehicles needed to transport baled biomass made
obtained from agricultural production,
access roads to public facilities lead through the central city core which means that
street hygiene would suffer when baled biomass transport takes place, especially in
windy conditions,
if biomass obtained from agricultural production would be used for heating public
facilities, it would be necessary to provide adequate storage place for baled biomass
near the boiler room with special consideration for fire and hygiene regulations, which
are non-existent.
Taking into account the above, it is assumed that the municipality Kuĉevo uses pellets from
agriculture or from waste wood from forest cutting and secund class firewood.
Analytical price is formed based on a complex set of calculations that consider many variable
production expenses but cannot predict a dynamic market flow regarding supply & demand
and realistic market competition between the producers who are prepared to offer a better
price if a sale of pellets is made during summer. Because of this, a market research was made
and pellet-producing companies that are within an acceptable transport distance (200 km)
were approached. A list of companies with their price lists is shown in the table (Table 12).
17
Table 12. List of companies engaged in the production and distribution of pellets
Company name Type of pellet Production capacity Price
“MTMOP” d.o.o
Dunavski kej, 12223 Golubac
beech i ash 1400 kg/h
600 t/month
150 €/t *
180 €/t**
200 €/t***
“MIBORO PELET” d.o.o
12222, Braniĉevo
beech 500 kg/h
210 t/month
160 €/t *
185 €/t**
200 €/t***
“FONOS” d.o.o – pelet centar
Uĉiteljska 59a, Zvezdara,
Beograd
beech
beech+fir
Always in stock 175€/t*
190 €/t**
205 €/t***
“BIOENERGY POINT” d.o.o
Izvorski put bb, Boljevac 19370
beech 3.000t /month 160€/t*
180 €/t**
195 €/t***
*Price valid if a quantity of pellet is ordered by July
**Price valid for quantities over 20 t
***Retail price
Prices shown in the table (Table 12) are formed without transport expenses. Carriers charge
their transport services 100 din/km for a 20 t truck. The price is formed by accounting the
distance traveled to pick up and deliver the goods. The following table (Table 13) shows the
distances with transport expenses from the production facilities and pellet storage facilities to
Kuĉevo municipality.
Table 13. Transport costs of pellets from producer to municipalities Kuĉevo (Turija)
Transport relations Number of
kilometers
Total transport
cost
Total transport cost
per ton of pellets
(km) (din) (din./t)
Turija - Golubac 21 – 22,6 4.200 – 4.520 210 – 226
Turija – Braničevo 24,3 4.860 243
Turija – Beograd (Zvezdara) 125 25.000 1.250
Turija – Boljevac 143 - 153 28.600 – 30.600 1.430 – 1.530
By analyzing the supplier bids from Table 12 and transport expenses from Table 13, a
conclusion has been made that the cheapest pellet can be obtained from “MTMOP” d.o.o
from Kuĉevo. Thus, wood pellet with a price of 152,13 €/t (17,342 din/kg, with 1€=114 din)
is the fuel of choice.
24
TASK 2 – Analysis of thermal energy required in
selected facilities for public use
In this report - task No. 2 - it was necessary to complete the research based on data from
research literature and field study and to summarize data collected in a separate report.
In task No. 2 it is necessary to make a thorough analysis of chosen public facilities following
the listed steps:
Make an optimal selection of public facilities that potentially can use biomass as a fuel
for heating;
Provide a graphic display of the facility with the layout of the heating system (for each
chosen facility in each municipality);
Prepare energy passport of the technical characteristics of the heating systems and the
analysis of the heat loss for chosen public facilities in each municipality (age of the
building and installation, type of window and window glass used, heating system, type
of heating fuel);
Analyze possible improvements of the energy efficiency of the heating systems in
public facilities and provide recommendations for the facilities that are the most
efficient for energy saving in the case of biomass combustion plants.
2.1. The choice of public facilities in Kučevo location that will be heated by
biomass
Selection of the public facilities in which biomass will be used as fuel for heating was done in
coordination with all important institutions in chosen municipalities. Thus, in selection of
facility and collection of all necessary data related to the project documentation including
micro and macro aspects, technical characteristics of the facility with existing infrastructure
and potential opportunities for expansion of existing infrastructure, the following individuals
were included: management of the municipality with the participation of municipal energy
managers, representatives of the public companies (Chamber of Commerce, Planning Bureau,
Utility Supplier of Electric Power, Water Supply and Sewage Companies, Heating Supply
Companies, Agriculture and Forestry Sectors) as well as general manages of almost all public
companies in selected municipalities.
During selection process several important criteria tended to be met:
that selected public facilities are of great importance for the local government
that at least one or more facilities require larger amount of heating energy
that these facilities are located in the areas in which there will be no overlapping with
the existing local piping system, i.e. that they are placed in areas which the local
district network will not reach in record time
25
that in selected locations there is not enough space for the construction of a boiler
room and a smaller storage for biomass which had to be physically separated from the
existing facilities (especially due to hygienic and fire requirements)
that location for facility construction is near existing boiler rooms that use gas or
liquid fuel, so that the boiler systems can work compositely, i.e. can use the same
collectors
that facilities have adequate internal pipe heating network
that it is known who the owner of the premises on which the construction of a boiler
room and a storage is planned
that pipe installation is not too long and complex for the construction
that there are adequate access roads to storages to ensure transportation of biomass for
combustion etc.
Reviewing the situation on the terrain and taking into account the criteria listed in the
municipality Kuĉevo it was noted that the municipality has 26 local communities (1 urban and
25 rural) and covers an area of 721 km2. The municipality has 22,290 inhabitants, while the
town has a population of 4823. The climate is temperate - continental favorable for life and
work.
It was noted that city of Kuĉevo doesnt have the central district heating system, and objects
are heated separately. This has opened up great opportunities for selecting the heating system
facilities for public use.
City of Kuĉevo has: one elementary school, one kindergarden. In addition to these educational
institutions city has building of the municipality, house of culture, building of employment
agencies and others.
Because of the fact that there is no city central heating system in Kuĉevo, municipalities'
government suggested that the city should consider the possibility of introducing a central
heating system with biomass as a fuel for two buildings in the city and one in village Turija
near Kuĉevo.For this reason, multiple buildings were taken into consideration:
Building name Appearance
Directorate of Public communal enterprise
Kučevo
This building (Figure 3) is located in the city center,
at the Veljko Dugošević square. It was built during
the 70s using a classic building type using solid brick
and concrete bearing elements. The building has 5
floors where the first 3 floors have offices and are
being used by the Directorate of Public enterprise
Kuĉevo, while people living in private apartments
occupy the last two floors. The building is heated by
the central heating system via the boiler fitted in the
Figure 3. Direcorate of Public communal
enterprise Kuĉevo building
26
boiler room located in the buildings‟ basement. Two
hot water boilers made by ”EMO CELJE“are used to
generate heat, giving a total power output of 580 kW.
Heating oil is used to fuel the boilers, but due to poor
financial situation oil cannot be bought and the
boilers have not been used for 15 years.
House of Culture “Veljko Dugošević” in Kučevo
House of Culture “Veljko Dugošević” in Kuĉevo
(Figure 4) is located beside the Direcorate of Public
communal enterprise Kuĉevo building. It was built in
1972 using a classic building type with solid brick,
concrete bearing elements and large glass areas. The
building is spread over 860 m2 in its base and has 3
floors. It is heated via the boilers from the Direcorate
of Public communal enterprise Kuĉevo building, but
because of the situation described before, different
electric appliances are used to heat the rooms.
Figure 4. House of Culture“Veljko
Dugošević” in Kuĉevo
Elementary school“Veljko Dugošević”
Elementary school “Veljko Dugošević” (Figure 5)
was built in the end of 19th century. There are no
precise information about the year of the building
since there are no civil or building plans. The school
was built using an outdated building style with
bearing walls in the ground floor made of stone and
the rest of the walls made of old brick. School base is
spread over 600 m2. It is heated using individual
furnaces fitted in every room. Children and the staff
together take in the firewood into the school. The
school provides elementary education to children,
and as of next year, it will conduct a two-year adult
literacy program.
Figure 5. Elementary school “Veljko
Dugošević” in Turija
During the considerations about the possibility of building a biomass boiler facility (wood
pellet), other buildings were considered besides the three described before. The other
buildings considered could not fit some of the required goals, mainly those regarding the
availability of space for building a boiler room or having unresolved property rights.
Finally, according to building location evaluation, property rights over the land on which a
boiler rooms would be built and heating requirements in accord with UNDP Serbia
representative, a decision was made to design a heating system for Primary School “Veljko
Dugošević” in Turija.
27
2.2 Technical features of the heating system with heat loss analysis overview
for selected public facilities in Kučevo municipality
Technical features of existing heating systems in selected public facilities in Kuĉevo
municipality are as follows:
2.2.1. Primary School „Veljko Dugoševiće“ u Turiji
Primary School “Veljko Dugošević” building in Turija is a public, one-storied building
(ground floor+story) with a useful surface area of 624 m2 in its base. The ground floor is fitted
with 23 rooms: headmasters‟ office, 3 classrooms, 2 offices, corridors, kitchen, dining room,
storage, pantry, 2 changing rooms, gymnasium, 3 bathrooms, etc. The school was built using
a classic building type, with concrete supporting elements and solid bricks. Exterior walls are
made of 30 and 45 cm thick solid brick, plastered on one side with 2,5 cm thicklayer of
mortar and on the other with 2cm thick layer of lime mortar. Heat transfer coefficients for
these walls are U = 1.20 W/m2K and U = 1.59 W/m
2K (Figure 6 and Figure 7).
The northern part of the school had an 9,6 x 7 m upgrade. A bathroom was fitted in the
ground floor and a classroom on the story. Exterior wall features regarding the upgraded part
are: 2 cm thick layer of lime mortar, 25 cm thick hollow brick and a 2,5 thick layer ofmortar,
with a heat transfer coefficient of U = 1,53 W/m2K (Figure 8). The schools‟ interior is divided
with 45 cm thick solid brick bearing walls, plastered on both sides with 2,5 cm thick layer of
lime mortar (Figure 9) with a heat transfer coefficient of U = 1,2 W/m2K.
Figure 6. Exterior school wall, 45 cm thick Figure 7. Exterior school wall, 30 cm thick
Furthermore, schools‟ interior is fitted with two additional wall types, both made from solid
brick (15 and 30 cm, respectively) and plastered on both sides with a 2,5 cm layer of lime
mortar (Figure 10 and Figure 11), with heat transfer coefficients of U = 1,91 W/m2K and U =
1,38 W/m2K, respectively. The flooring in the ground floor was fitted in layers: gravel,
waterproofing, charged concrete, cement layer and decking floor, with a heat transfer
28
coefficient of U = 2,35 W/m2K (Figure 12). The corridor floor in the schools‟ ground floor
has a top layer of ceramic tiles and has a heat transfer coefficient of U = 3,66 W/m2K (Figure
13).The floor in the ground floor of the upgraded part of the school has a top layer of ceramic
tiles followed by a 5 cm thick layer of thermal insulation (Tervol) and has aheat transfer
coefficient of U = 0,68 W/m2K (Figure 14). The floor in the room above the open area of the
schools‟ entrance is fitted with decking boards and thermally insulated with a 30 cm layer of
air, 3 cm thick lath, 1,5 cm thick layer of reed and a 2 cm thick layer of reedy mortaron the
bottom to finish. This floor has aheat transfer coefficient of U = 0,79 W/m2K (Figure 15).
Figure 8. Exterior wall of the upgrade Figure 9. Interior bearing wall
Figure 10. Interior dividing wall, 15 cm thick Figure 11. Interior wall, 30 cm thick
29
Figure 12. Floor in the classrooms in the
ground floor
Figure 13. Floor in the corridors in the ground
floor
Figure 14. Floor in the upgraded part of the
school, in the ground floor
Figure 15. Floor above the open area of the
school
Above the rooms in the ground floor there is a floor made of 10 cm thick reinforced concrete
slab, covered on top with decking and fitted below with board ceiling made of 3 cm thick
wooden boards. To follow the boards, there is a 1,5 cm thick layer of reed and a final layer of
reedy mortar, which altogether has aheat transfer coefficient of U = 0,74 W/m2K (Figure 16).
The floor on the story of the upgraded part is covered with parquet and has aheat transfer
coefficient of U = 1,38 W/m2K (Figure 17). The ceiling on the schools‟ floor is made of a 10
cm thick reinforced concrete slab, covered with a 8 cm thick layer of „karatavan‟ (mud+straw)
and a 3 cm thick layer of mud, on the top side. Below the slab, there is a board ceiling made
of 3 cm thick boards, covered with a 1,5 thick layer of reed on top and plastered with reedy
mortar below, with a total heat transfer coefficient of U = 0,86 W/m2K (Figure 18). The
30
ceiling in the upgraded part is made of modern building elements and is thermally insulated
with 5 cm thick layer of Tervol and has a heat transfer coefficient of U = 0,58 W/m2K (Figure
19).
Figure 16. Floor on the story Figure 17. Floor in the upgraded part on the story
Figure 18. Ceiling on the story Figure 19. Ceiling in the upgraded part on the story
Doors and window frames in the school are made of wood, except in the upgraded part of the
school,where PVC doors and windows are fitted. They are old and in poor condition, which
causes major heat loss thus making heating problem that much bigger. Heat transfer
coefficients for doors and windows with wooden frames vary from 2,9 W/m2K for exterior
wooden windows with parted sashes (Figure 20), to 3,5 W/m2K for exterior doors with
sections made of glass (Figure 21).
31
Figure 20. Windows in the school
Figure 21. School entrance
Due to a lack of a central heating system, school is heated by means of fireplaces and furnaces
burning solid fuels made by “Alfa-plam” from Vranje (Figure 22), with the output power of 7
kW for type “Vulkan” and 14 kW for type “Rustik”(Figure 23). All of the classrooms, offices,
dining room and the gymnasium are fitted with furnaces and the firewood is brought and
stoked manually. This type of heating hinders the teaching process. Since the school is fitted
with 13 furnaces (total output power of 175 kW), the children, along with the janitor,
sometimes need to bring in firewood (Figure 25)and put it in the furnaces. During the stoking
process, furnace door needs to be open andsome of the products of combustion enter the
classroom (Figure 24) thus becoming an issue since the children are left without supervision
during breaks between classes.
Figure 22. “ALFA PLAM” furnace, type “Vulkan”
Figure 23. “ALFA PLAM” furnace, type “Rustik”
Figure 24. Furnace in the classroom Figure 25. Wood storage
32
To determine accurate (real) heat requirements for a building, heat loss calculations due to
transmission and ventilation through construction elements must be made. The calculations
are available in Chapter 4 Appendix, while the following table offers heat loss for individual
rooms (Table 14).
Table 14. View of room heat lossof the school building
STATUS OF ROOMS
Room
number Room name
Temperature in
winter mode
Heat losses
in the room Room status
- - tp Q -
- - oC W -
(1) (2) (3) (4) (5)
G R O U N D F L O O R
1 WINDSHIELD 15 1448 TREATED
2 HALL 15 8411 TREATED
3 CLASSROOM 15 10050 TREATED
4 OFFICE 15 2584 TREATED
5 OFFICE 15 2314 TREATED
6 PRINCIPAL'S OFFICE 15 4941 TREATED
7 CLASSROOM 15 10925 TREATED
8 CLASSROOM 20 7700 TREATED
9 DINING ROOM 15 17213 TREATED
10 KITCHEN 20 2509 TREATED
11 KITCHEN - FOOD ISSUE 18 2741 TREATED
12 STORAGE 18 - NOT TREATED
13 SPORTS ROOM 20 13053 TREATED
14 DRESSING ROOM FOR TEACHERS 20 1814 TREATED
15 WAREHOUSE 15 - NOT TREATED
16 DRESSING ROOM 1 10 1682 TREATED
17 DRESSING ROOM 2 18 1200 TREATED
18 HALL 18 1647 TREATED
19 MALE TOILET - STUDENTS 18 1367 TREATED
20 MALE TOILET - TEACHERS 18 179 TREATED
21 FEMALE TOILET - TEACHERS 20 896 TREATED
22 TOILET - HALL 20 748 TREATED
23 FEMALE TOILET - STUDENTS 20 1367 TREATED
TOTAL:
94.789
F I R S T F L O O R
1.1 HALL 20 814 TREATED
1.2 CLASSROOM 20 3509 TREATED
1.3 CLASSROOM 20 2456 TREATED
1.4 CLASSROOM 20 3634 TREATED
(1) (2) (3) (4) (5)
33
1.5 CLASSROOM 20 3988 TREATED
1.6 CLASSROOM 20 348 TREATED
1.7 CLASSROOM 20 39 TREATED
1.8 CLASSROOM 20 1326 TREATED
1.9 CLASSROOM 20 1378 TREATED
1.10 LIBRARY 20 1032 TREATED
1.11 HALL 20 -1006 TREATED
1.12 STAIRS 20 7061 TREATED
1.13 CLASSROOM 20 11884 TREATED
TOTAL:
101.847
Table 15 shows the total losses of the entire recap of the building and kitchen.
Table 15. Display summaries of the complex ES "Veljko Dugošević" in Turija
RECAPITULATION
G R O U N D F L O O R
94.789
F I R S T F L O O R
101.847
TOTAL:
196.636 W
According to data from the table (Table 15), a conclusion can be made that the ground floor
is spread over 624 m2 with required heating volume of 2.308,8 m
3. Necessary power
requirements according to heat loss calculations due to transmission and ventilation are
94.789 W, that is 147,64 W/m2 (heated area) or 41,06 W/m
3 (heated space).
The story has an area of 640 m2 and heating volume of 2.432 m
3. Necessary power
requirements according to heat loss calculations are 101.847 W, that is 159,14 W/m2 (heated
area) or 41,88 W/m3 (heated space).
Total heating requirements for the complex are 196.636 W, which is 197 kW.
2.3.Analysis of the measures for the increase of energy efficiency in
buildings for public use
The analysis of the measures for the increase of energy efficiency in buildings for public use
in Kuĉevo municipality has to be done from two aspects. One aspect is the general, i.e. global
approach to the problem of increasing the energy efficiency in municipalities, while the other
one is the increase of energy efficiency in individual buildings.
When observing the use of energy for central heating of individual buildings for public use, as
has been stated already, it can be established that the energy is used irrationally and with poor
quality (large deviations from assigned temperatures in heated rooms).
According to the present condition of the chosen public usage buildings in Kuĉevo, we may
conclude that by the usage of proper organizational and technical activities significant energy
sufficiency improvements may be achieved.
34
2.3.1 Power consumption in coplex ES„Veljko Dugošević“ in Turiji andsuggestions of
practical measures for increasing the energy efficiency of facility
Beside the technical analysis of the buildings, an economic analysis of energy loss must be
done in order to get a whole pictureregarding energy efficiency and to be able to suggest
measures for improving energy efficiency and determine its profitability. The following table
(Table 16) offers an overview of consumption of fuel used for school and kitchen heating and
overall power consumption. The data is available for a heating period from 15/10/2011 until
15/4/2012. In order to make an economic analysis of overall energy consumption, all
available forms of energy must be converted to the same unit ([kWh]/[din./kWh]), that is
equalize with wood and coal consumption (and their price). To make the conversions, brown
coal and oak wood are adopted as reference fuels with following characteristics: brown coal -
Hd =15,927 kJ/kg, ρ = 1,25 t/m3;oak wood - Hd =16,100 kJ/kg, ρ = 0,72 t/m
3.
By analyzing the table (Table 16) a conclusion can be made that the wood used to heat the
building accounts for 84.00% of the total consumption expenditure energies, while electricity
is 16.00%. When referring to the concerns expressed by the energies consumed in kWh then
wood accounts for 94.61%, and the current 5.39%.
Table 16. Display power consumption based on kWh
Quantity Price Total price
[m3] [t] [kWh] [din/m
3] [din/t] [din/kWh] [din]
Consumption of wood 80 57,6 257.600 4.200 5.833 1,30 336.000
Electricity
consumption - - 14.666 - - 1,55 64.000
UKUPNO: - - 272.266 - - - 400.000
The following are some practical organizational and technical measures fit to increase energy
efficiency in selected public facilities in Kuĉevo:
All of the windows and doorsshould be replaced with new PVC (profiles with five
chambers and thermo-insulated glass) windows and doors. The worst heat transfer
coefficient forthis kind of windows is U = 1,2 W/m2K.
Thermal insulation should be mounted on the exterior facade walls (5 cm thick
Styrofoam, λ=0,035)and covered with protective façade casing (such as “demit”
facade), to prevent negative atmospheric impact on the Styrofoam.
A central heating system should be designed presuming the availability of
thermostatic valves.
By caring out the energy efficiency improvement measures stated before, heat loss can be
reduced to a great extent, that is overall heat requirements could be decreased, which would
result with overall energy savings, essentially saving money. In order to make a techno-
economic analysis of potential savings by implementing the measures stated before, some
base system operating parameters must be defined, such as:
35
duration (timeframe) of wintertime heating
fuel consumption during wintertime heating
number of working days during wintertime heating
average daily temperature.
Wintertime heating starts on the October 15th and ends on the April 15
th. The wintertime
heating lasts 185 days. Average temperature is 15ºC. By multiplying the number of working
days with average daily temperature, a value of 2775 DD per wintertime heating for heating
system installed in primary school “Veljko Dugošević” together with the kitchen, is obtained.
Using the previously gathered results, fuel consumption for wintertime heating can be
calculated by using the following formulae:
mF/year= 24·3,600·e·y·DD·Q/(hd··(tu-ts)) [kg/winter time_heating]
gde su:
e = et·eb - temperature and exploatation limitation coefficient, 0,9 x 0,9 = 0,81,
y - corrective coefficient (interruptions in stocking, wind), 0,8,
SD - degree – day value, 185 day · 15oC = 2775days
oC,
Q - heating requirement, amount of heat,[kW],
Hd - lower heating value (16.900) [kJ/kg],
- efficiency of the facility (0,85),
tu - interior temperature of heated rooms (20oC) i
ts - exterior project temperature, (-18oC).
By using organizational and technical measures of savings which should result in increasing
overall energy efficiency of the facility, the following results may ensue:
- By exchanging old and decrepit windows and metal doors with new PVC (profiles
with five chambers and thermo-insulated glass) windows and doors, heat loss due to
transmission and ventilation could be mitigated. Energy savings were calculated using
heat transfer coefficient of Uw = 1,2 W/m2K (windows) and Ud = 1,8 W/m
2K (doors).
- If thermal insulation should be mounted on the exterior façade walls, transmission heat
loss could be mitigated to a great extent. Should a 5 cm thick Styrofoam be mounted
on the exterior facade walls (λ=0,035 W/mK) and covered with protective facade
casing (“demit” facade), it would yield a heat transfer coefficient of U = 0,51 W/m2K
for the exterior walls, instead of current U = 1,84 W/m2K.
Detailed overview of the calculation will not be shown due to its ampleness; however, a
savings amount recap is available in the table (Table 25). Energy savings were obtained using
calculated fuel consumption, which is not far off the data presented by the municipalities‟
people in charge.
Comparative analysis of Table 16 and Table 17 can be seen that devatation of costs which are
obtained from municipality and and those obtained by calculation is 31%, which is caused by
the specific situation on the terrain. As already stated in the facility the furnaces are manually
fed with fuel and information on their actual fuel consumption and efficiency are not available
36
and they could only be estemated by experiments. A rough estimate of the heating power
based on a vendor declared their total thermal power is 175 kW. The calculation takes power
required heat loss of 197 kW and an efficiency of η = 0.6.
By replacing the old wooden doors and windows with new doors and windows made of PVC
profile and insulating glass, required thermal power can be reduced to 178.2 kW, which could
lead to fuel savings of 45,526.97 dinars, or 399.36 € for a heating season. By placing thermal
insulation on the outside wall of the object facade, required thermal power can be reduced to
158.3 kW, which could lead to fuel savings of 94,675.85 dinars, or 830.49 € for a heating
season.Total savings by performing all previous works could reach 140,202.81 dinars, or
1229.85 € for heating season.
The necessary amount of investment to these austerity measures and increasing energy
efficiency and implement their effectiveness will be presented in the Chapter 3.6.
41
Table 17. Display seasonal fuel consumption of the existing boiler and the savings that can be achieved by applying technical - organizational
measures to increase efficiency
Type of
fuel
Consta
nt e y
Degree -
dayDD Q hd η Δt mF/year.
Fuel
consumption
Fuel
consumption
Price of
fuel
Cost of
heating
season
Cost of*
heating
season
Energy
savings
Energy
savings
[-] [-] [-] [-] [°Cday] [kW] [kJ] [-] [°C] [kg/god.] [kg] [t], [m³] [din./t]
[din/m³] [din./season] [€/sezonu] [€/season] [din./season]
OLD BOILER FACILITY WOOD
Coal 86400 0,81 0,8 2775 196,6 15927 0,60 38 84129,04 0,00 0,00 7500 0,00 0,00 - -
Wood 86400 0,81 0,8 2775 196,6 16100 0,60 38 83225,05 83225,05 115,59 4200 485479,44 4258,59 - -
TOTAL: 485479,44 4258,59
UNDERWENT REPLACEMENT OF OLD WOODEN WINDOWS WITH NEW PVC WINDOWS
Coal 86400 0,81 0,8 2775 178,2 15927 0,60 38 76239,64 0,00 0,00 7500 0,00 0,00 0,00 0,00
Wood 86400 0,81 0,8 2775 178,2 16100 0,60 38 75420,42 75420,42 104,75 4200 439952,47 3859,23 399,36 45526,97
TOTAL: 399,36 45526,97
UNDERWENT PLACINGTHERMAL INSULATION OF STYROFOAM5 cm THICKNES
Coal 86400 0,81 0,8 2775 158,3 15927 0,60 38 67722,60 0,00 0,00 7500 0,00 0,00 0,00 0,00
Wood 86400 0,81 0,8 2775 158,3 16100 0,60 38 66994,90 66994,90 93,05 4200 390803,59 3428,10 830,49 94675,85
TOTAL: 830,49 94675,85
THE SUM TOTAL SAVINGS: 1229,85 140202,81
42
TASK 3 – Techno-economic analysisfor thermal facility which
uses biomass as a fuel, for heating chosen buildings
3.1.Technologyof available biomass form combustion
Adequate choice of terminology for intentional combustion of biomass with the goal of
obtaining heat energy is of the highest importance for the energy, economical and ecological
efficiency of that process.
A schematic presentation of the appropriateness of technical-technological solutions for
thermal solutions for thermal power of a 100 MW furnace and certain forms of biomass for
combustion is shown in (Figure 26).
Figure 26. Appropriateness of tehnological and tehnical solutions for biomass combustion
S– batch, with fixed grate; V– with movable grate; U– with lower firing (crucible); E– with
combustion in space (cyclon or votex firebox), W– flidized bed; Z–with helical combustion
(cigarret combustion);
3.2. Selection of combustion technologies and technical solutions for the
thermal power plants and defining the maximum boiler plant thermal
power for continuous heating of public buildings
Starting with the chosen types and forms of biomass to be combusted, spatial limitations,
environmental and legal norms and standards, it was decided upon the thermal energy plant
for combusting wood pellets that are to be purchased at market value.
Combustion of wood pellets will be performed in a stoker with a moving andiron.
43
The technology suggested has several important advantages that could be briefly described as
the following:
It combusts fuel (wood pellets) which is very common on the Serbian market. The fuel
could be bought successively, i. e. as needed, which means that it is not necessary to
buy the total amount of fuel needed once a year.
Combustion of wood pellets could be completely automated with a total mechanization
of the pellet manipulation process.
Emission of harmful gasses could be maintained in the allowed limits.
The wood pallet combustion plant could be put in various modes.
While working in this plant, the wood pellets will not be affected by the problems of
solubility as is the case with combustion of biomass form the agricultural production.
The negative side of the chosen technology is the expensiveness of the combustion plant,
which could be justified by the tendency to automate the combustion process as much as
possible.
General requirements for the construction of the boiler facility
It was defined that the thermal energy plant for heating the chosen object in Kuĉevo, should
work as a wood pellet furnace.It has to satisfy the following basic technical, economic and
environmental requests:
It should produce the required amount of energy (300 kW). This range of boiler power
is taken as a certitude due to the unknown quality of pellet.
It should be possible to combust wood pellets in it.
The plant should work in an economic way, i. e. it should provide a competitive price of
thermal energy in relation to the production where the basic fuel is electricity only.
The pollution of the environment should be in accordance with the domestic and
European norms.
A contemporary level of pairing and work control should be secured.
A contemporary level of plant maintenance with minimal costs should be secured.
Hygienic conditions should be satisfying during the pellets manipulation.
3.3. Definingthe optimalplacefor the construction ofthermal
powerplants(with thetechnical,economic and environmentalaspects)
The choice of the public use property in Kuĉevo that are to be heated by the thermal energy
from the biomass was not easy. The biggest problem with this choice was the adequate
location for building of the boiler-room with a warehouse for the biomass. The problem was
made more complex by the hindered transport during the supply of the facilities with
biomass.Therefore, the Primary School "Veljko Dugošević" in Turija was selected, because it
has own spacious garden complex. After determining heat losses of school facilitie and
defining dimensions of hot water boiler plant, the location was selected. It is desided that a
new boiler building shoud be near the old building for storage of wood. It is anticipated that
44
the new facility building should be made from prefabricated lightweight thermal insulated
metal panels, that will be attached to the metal support construction. The building is
sufficiently far from the elementary school, thus avoiding any possibility ofof children being
affected in the event of a fire in the boiler room. Facility is also very accessible for access by
the transportation unit, which should bring in pellets.
3.4. Technical description of the biomass boiler facility (thermo-technical
equipment, boiler room, hot water piping) with the extended bill of
quantities for the Kučevo municipality, along with the expected energy and
ecology efficiency
This study provides a construction of boiler house for hot water boiler on pellets, which
should be used for heating the primary school „Veljko Dugošević” in Turija.
The boiler plant includes the purchase and installation of the boiler with accessories(collectors
for hot and cold water circulating pumps, thermostats, valves, filters, etc.) whose system will
be connected with the heating network in the district heating system of the school.
Thermal capacity of new boiler facility Q=300 kW.
The boiler will operate in the mode 90/70oC.
Technical features of the new boiler pellet wood are:
Fuel
The wood pellets are planned to be used as fuel.
Dimensions of wood pellets: Ø 6 – 12 mm x 25 - 35 mm
Density of the biomass bales ρ= 650 kg/m3
Special demands: maximal humidity wmax= 10%
Kotao na biomasu
Hot water boiler with movable grate, the company "Eco-products", Novi Sad.
The furnace thermal power: N= 300 kW
The degree of boiler efficiency: η= 0,85%
The schematics of boiler facility, wich burns wood pellets Figure 27.
For the preparation of the sanitary water, in the new boiler room, provided is a standing hot
water boiler made of stainless material, with a volume of V=300 l.The water from the boiler
to be used as domestic water.
A new boiler has a water softener systems, closed expansion tank, associated fittings, pumps
that are dimensioned that overcame all resistance in the installation, regulatory elements for
automatic operation of the boiler, etc.
45
Figure 27. The schematics of the boiler facility wich burns wood pellets
(1. bunkerfor pellets, 2. flexible screw conveyor for pellets, 3. barrieragainstflame, 4.screw
feeder for pellets 5. hot-water boiler, 6. primary airfan, 7.secondary airfan, 8.multicyclone, 9.
flue gas fan, 10. Container for ash, 11. chimney)
Bill of quantities for delivery, installation and other works on HVAC equipment in the
construction of thermal power plants, plants building and external pipingthat is shown in
graphical documentation.
Summary of costs for the purchase of HVAC and process equipment and construction works
can be represented as follows:
46
SUMMARY
BUILDING COSTS OF THERMAL ENERGY FACILIY FOR THE HEATING OF PUBLIC
BUILDING IN KUĈEVO
(The value of 1€ is 114 din)
I THERMOTECHNICS AND PROCESS EQUIPMENT 5.136.820
II CONSTRUCTION OF A BOILERROOM BUILDING 1.077.780
III HEATING PIPES 926.509
IV
IMPROVEMENT OF TECHNICAL
CHARACTERISTICS OF INTERNAL HEATING
INSTALLATIONS
1.583.600
V PROJECT DOCUMENTATION (5%) 413.185
TOTAL: 9.137.894
INDIVIDUAL INVESTMENT PRICES ARE:
In relation to the installed power: 30.459,65 din/kW
In relation to the heated area : 7.229,35 din/m2
47
3.4.1. Expected energy efficiency and ecological efficiency for biomass combustion in
boiler facilities
Based on several year of boiler facilities research in Serbia in which baled biomass is
combusted, in general, it can be stated that they have low energy efficiency. Low energy
efficiency is also a signal for high gass emission that pollutes work and life environment.
This causes financial loses and problems for the environment. It is expected that the energy
efficiency of combustion facilities of wood pellets in Kuĉevo will be 85% when working with
wood pellets with humidity of up to 10%.
Ecological efficiency:
Biomass is declared as ecological fuel. First and foremost it is implied since the chemical
composition of biomass is very favourable, and as an alternative fuel it pollutes the
environment significantly less in comparison to conventional energy sources. Biomass does
not create the greenhouse effect, i.e. the pollution takes in during the plant growth as much
pollution as the combustion produces. There is no sulphur in the biomass nor can it be found
in traces. The combustion of biomass does not create large amounts of nitric oxide, since the
combustion temperatures need to be kept at lower values because of possible melting of ashes.
Biomass ashes do not pollute the soil, water, flora and fauna and they can be used as fertilizer
for vegetable gardens and gardens, under the condition that the floating ashes are excluded
because they can contain heavy metals that are harmful to the environment.
During the biomass combustion carbon monoxide can appear in larger amounts, mostly
because of some technical faults of the facilities or due to unprofessional handling of
combustion technology. In combustion products, there is very little sulphur dioxide and
sulphur trioxide, since sulphur can be found in bio-fuel in very small amounts, so the
combustion facilities are spared from low temperature corrosion, and the environment from
acid rains. The incorrect handling of combustion facilities can cause the occurrence of
chloride compounds and cyclic hydrocarbons. (dioxin, furans and polyaromatic hydrocarbons)
It is expected that from this combustion facilities for wood pellets, in Kuĉevo, with 300 kW
thermal power, during a year emitted to the atmosphere will be:
Carbon dioxide:
101,638.66 kg CO2, respectively101.64 t CO2at combustion of wood,
123,550.14 kg CO2, respectively123.55 t CO2at combustion of wood pellet.
The new facility will make a greater amount of emissions of carbon dioxide by 21.91 t, but
calculated on the basis of greater thermal power of plant.
Nitric oxides
2,967.55 g NOx, respectively2.97 kg Nox, at combustion of wood,
3,607.30 g NOx, respectively3.61 kg NOx, at combustion of wood pellet.
48
The new facility will make a greater amount of emissions of nitric oxides by 0.64 kg, but
calculated on the basis of greater thermal power of plant.
Sulphur oxide
In both cases, there is no sulfur oxide emissions.
Particles
The emission of particles for specified boilerpower is:
185,472.00 g particles, respectively185.47 kg particles, at combustion of wood,
225,456.47 g particles, respectively225.46 kg at combustion of wood pellet.
The new facility will make a greater amount of emissions of particles by 39.99 kg, but
calculated on the basis of greater thermal power of plant.
In the biomass storages and the boiler room dust must not be produced, since dust has a
harmful effect on the human, animal and bird respiratory organs, it is easily combustible and
can easily explode if the right conditions are met. Because of this, dust needs to be efficiently
caught before and after the combustion. The installed equipment must satisfy the prescribed
marginal values for permitted amounts of dust as well as gasses harmful to the environment.
In Table 18 are given marginal values for the content of the most important elements in the
biomass, that could have a harmful effect on the functioning of the facility as well as on the
environment.
Table 18. Possible harmful effects of certain elements and corrective technologicalmeasures
Element
Approxi- mate limit
Limiting parameter Biomass in which problems can be
expected
Technological capabilities in case of exceeding the limit values
N* <0,6 Emissions NOx Straw, grain, grass, tree bark
Multi-stage intake air, a reducing furnace
Cl* <0,1 Corrosion
Emissions HCl
Straw, grain, grass Anti-corrosion: temperature control, automatic cleaning of heating surfaces, protective coatings on pipes. Against the emission of HCl: purification of flue gases
S* <0,1 Corrosion Straw, grain, grass Anti-corrosion: see for Cl
Ca** < 15 Deposit formation Straw, grain, grass Control of temperature in the furnace
Mg** > 2,5 Deposit formation Rare species See for Ca
K* <7,0 Deposit formation
Corrosion
Straw, grain, corn, grass
Anti-corrosion: see for Cl
Against deposit formation: see for Ca
Na** <0,6 Fusibility
Build-up
Corrosion
Straw, grain, grass Anti-corrosion: see for Cl
Against deposit formation: see for Ca
Zn** <0,08 Recyclingof ashes Bark,wood mass Fractional separation of heavy metals
Cd** < 0,0005 Recyclingof ashes Bark,wood mass Fractional separation of heavy metals
49
* Given on the basis of dry coal
** Given on the basis of dry ash
Appropriate micro-climate has to be sustained within the boiler room. It must not have
negative effects on the personnel.
Maximum allowed levels of smoke gases in air for work and life environment to be secured
by thermal energy equipment and boiler operators are listed in Table 19.
Table 19. Maximum allowed levels (MAL) of smoke gases in air for work and life
environment (SRPS Z.BO 001)
Chemical substance Unit
MDK* for life
environment
8h
MDK* for life
environment
24 h 1h
Nitric oxides (NOx) mg/m3 6,0 0,085 0,15
Aliphatic hydrocarbons
(AlCH), Tk = 141-200ºC mg/m
3 300 -
Benzene (C6H6) mg/m3 3,0 0,8
Toluene (C6H5CH3) mg/m3 375 7,5
Xylene (C6H4(CH3)2) mg/m3 435 -
Carbon monoxide (CO) ppm (ml/m3 ) 50 (55) 4,4 (5) 8(10)
Carbon dioxide (CO2) mg/m3 - -
Sulfur dioxide (SO2) mg/m3 5,0 -
* MALK – Maximum allowed levels of smoke gases in air during 8h exposure within work
environment in accordance with maximum allowed levels of harmful gases, steam, and
aerosols in the work and auxiliary rooms‟ atmosphere, SRPS Z.BO 001.
3.4.2. Marginal values of gas emission for specific types of furnaces
Regulations in Serbia
Boiler facilities in Serbia have to meet the regulations of the Government of Republic of
Serbia concerning the marginal values of hazardous air pollutants (Official Gazette of the
Republic of Serbia, no. 71/2010), for low power furnaces - less than 1 MWth (article 19,
apendix II). One should also take into consideration the immission values regulated by the
rulebook on borderline values, imission measuring methods, measure locations set up criteria
and data records (Official Gazette of the Republic of Serbia, No. 19/2006)
In
50
Table 20 are givenemission limitsforcombustionof biomass.
Table 20. Borderline emission values (BEV) for small solid fuel combustion facilites
(Regulation, Official Gazette of the Republic of Serbia, No. 71/2010)
Table 21 provides marginal values of emissions for gas fuelled furnaces (natural gas).
Table 21. Marginal values of emissions(MVE) for small facilities for the combustion of gas
fuel (Regulation, “Official Gazette of the Republic of Serbia”, no 71/2010)
Table 22 provides marginal values of imissions (MVI) of gases in inhabited locations in open
space.
Table 22. Marginal values of emissions (MVI) of gases, soot, suspended particles and heavy
metals, sediment andaerosediment content, (Rulebook, “Official Gazette of the
Republic of Serbia”, no 54/92, 30/99 and 19/2006)
Contaminat.
matter
Unit of
measurem. Total CO NO2 SO2
Soot Susp.
particles Pb Cd Zn Hg
Gases, soot
and susp.
particle
µg/m3/dan 413,01 5 85 150 50 120 1 0,01 1 1
Sediments µg/m2/dan 655 - - 250 5 400
Sediment
matter mg/m
2/mes. 450 - - - - - - -
Parametar Vrednost
Smoke number < 1
Carbon monoxide , CO (500 kW do 1 MW) 1.000 mg/nm3
Nitric oxides, as N2 (100 kW do 1 MW) 250 mg/nm3
Volume of O2 (other solid fuels (biomass)) 13%
Allowed heat loss (50 kW do 1 MW) 12%
Parameter Value
Carbon monoxide , CO (400 kW do 10 MW) 80 mg/nm3
Nitric oxides, as N2 ( water< 110oC, > 0,05 MPa) 100 mg/nm
3
Volume of O2 3%
51
3.5. Necessary amount of biomass for hourly and seasonal work of the
boiler facility
3.5.1. Hourly consumption of biomass
Maximum declared hourly consumption of biomass of the boiler facility in Kuĉevo can be
calculated as a quotient of declared thermal power of the facility and the product of the degree
of usefulness of the facility and thermal power of the fuel (biomass) to be burnt. For the
approved starting information, hourly biomass consumption of the facility is:
mH = Q / x hd = (300 x 3600) / (0,85 x 18.000) = 70,59 kg/h
where are:
mH [kg/h] - fuel consumption.
Q [kW] - power of the hot water boiler facility,
- - -level of efficiency of the boiler facility,
hd [kJ/kg] - lowest thermal power of selected biomass.
3.5.2. Seasonal consumption of biomass
Seasonal consumption of biomass as fuel is subject to change and mostly depends on external
i.e. exploitation conditions during the heating season. It has been confirmed that maximum
thermal power of heating facility fuelled by biomass is 300 kW and that all larger heat losses
will be compensated for by light fuel oil.
Based on this, yearly biomass consumption can be calculated by the following equation:
mF/year= 24 · 3.600 · e ·y ·DD ·Q / (hd· · (tu - ts)) = 24 · 3.600 · 0,81 · 0,8 · 2.775 · 300 /
(18,000·x 0,85·x (20-(-18)) = 62.626,8 kg/year
e = et·eb - temperature and exploatation limitation coefficient, 0,9 x 0,9 = 0,81,
y - corrective coefficient (interruptions in stocking, wind), 0,8,
SD - degree – day value, 185 day x 15oC = 2775 days
oC,
Q - heating requirement, amount of heat,[kW],
Hd - lower heating value (18.000) [kJ/kg],
- efficiency of the facility (0,85),
tu - interior temperature of heated rooms (20oC) i
ts - exterior project temperature, (-18oC).
Since the plan is to store pellets in jumbo size bags 91 · 91 · 180 cm (Figure 28),which
contains 1030 kg of pellets, for the total season is needed 61 jumbo bag. But, because pellets
can successively be purchased and ordered to ensure enough supply of pellets for a month,
which is 10,323 kg, or 11 jumbo bags the boiler plant house must have 11 m2 of store space.
52
Transport jumbo bag is best to be done with a crane truck (Figure 29) or it can be trasporeted
by ordinary truck but there must be a machine which is going to unload the truck.
Figure 28. Jumbo bag
Figure 29. Crain truck
53
3.6. Economic analyses of construction the heating facility
3.6.1. Current price of the heating energhy from the used components
In thermo-energetic facility with the purpose of heating public facilities in Kuĉevo main
source will be wooden pellets purchased based on the market prices which are based on
calculation in Chapter 1.2. is 18,3 din/kg. Price of the usage of wood which will be used for
comparison in the calculations is 5.833 din/t respectfully with the trend of constant increasing
in prices.
Comparative prices of the current heating energy produced from 196,6 kW by combusting
wood and new investment where 100% of the required heat energy is produced from biomass,
estimated average rate of the efficiency in the facility are submitted in Table 23.
Table 23. Analyses of the quantity and prices of heating energy for the period 2011/2012
No. Parameters for analyse
Used materials
Current boilers With new boiler
Wood Biomass
1. Price of energy 5,83 din/kg 18,3 din/kg
2. Thermal power (hd) 16.100 kJ/kg 18.000 kJ/kg
3. Energy power 4,47 kW/kg 5,0 kWh/kg
4. The number of heating days per year 185 days 185 days
5. The number of heating hours per year 1850 hours 1850 hours
6. Nominal thermal power plants (kW) 196,6 kW 196,6 kW
7. Hourly energy consumption 87,94 kg/h 46,27 kg/h
8. The degree of utility plant 0,5 0,85
9. The total annual fuel consumption 99.870,06 kg 41.048,94 kg
10. The total annual enrgy consumption 1.607.907.888,9 738.880.966,4
11. The total annual enrgy consumption (kWh) 446.641,08 205.244,71
12. Unit cost of thermal energy 1,30 din/kWh 3,66 din/kWh
13. Total annual energy costs (din) 582.420 din 751.196 din
15. TOTAL: 5.154 eur 6.589 eur
From the Table 23 above with the simple comparison we can see that wooden pellets are 29%
cheaper from the usage of wood, technically speaking. This ratio will be lower when we add
in calculation all other related costs mainly in old facility: higher maintenance costs, labor
costs, poor boiler efficiency rate,etc
54
Table 24. Structure of the total investment
INVESTMENT
FINANCIAL SOURCES
Bank-funds Own TOTAL
I Fixed assets 7.852.238 872.471 8.724.709
1 Construction of the boiler facility 1.425.240 158.360 1.583.600
2 Equipment – boiler and process equipment 4.623.138 513.682 5.136.820
3 Heating pipes-instalation and related works 1.803.860 200.429 2.004.289
II Project documentation 0 436.235 436.235
III Working capital 0 87.554 87.554
TOTAL INVESTMENT VALUE
(I+II+III) 7.852.238 1.396.260 9.248.498
In the structure of the investment cost of preparation of project documentation is calculated at
the rate of 5%. It is estimated that from the own resources 10% of the total investment value
will be financed which is on the line with financing conditions from the development funds
mentioned bellow in the section 3.8.2.2.b.
3.6.2. Financial effectiveness with the profitability analyses
3.6.2.1. Calculation of incomes and expenses
Projection the cost structure of heating energy is showed in Table 25.
Table 25. Cost projection of 1kWh of required energy
Structure of production Produced energy Unit price Total amount
kWh din/kWh din
Heater – biomass (100%) 205.244,71 3,66 751.196
TOTAL: 205.244,71 - 751.196
In the projected structure of the cost for 1 kW producesd energy, 100% will be used from new
biomass boilers.
The average seasonal price of produced 1 kWh of energy for heating 1264 m2 facility in
Turija will be 3,66 din/kWh.
Table 26. Income statement - current operations
ELEMENTS Unit Unit price Quantity Total amount
(2011.)
Structure
(%)
(1) (2) (3) (4) (5) (6) (7)
A REVENUE - - - 3.191.600 -
Heating of the premises (production costs) m2 2525,000 1264,00 3.191.600 -
B OPERATING COSTS - - - 602.420 -
Material costs(produced energy) din/kWh 1,30 446641,08 582.420 18,25
55
(1) (2) (3) (4) (5) (6) (7)
Costs of energy (electricity,water) - - 20000,00 20.000 0,63
C TOTAL COSTS (B+E+F1+G1) - - - 3.191.462 -
D GROSS PROFIT (A-B) - - - 2.589.180 -
E GENERAL/ADMIN. EXPENCES - - - 2.534.042 -
Gross salaries workers 813600,00 3,00 2.440.800 76,48
Cost of services(maintainance costs,etc.) - - 58242,00 58.242 1,82
Nonmaterial costs - - - 35.000 1,10
F INCOME WITH DEPRECIATION (D-E) - - - 55.138 -
F1 Depreciation - - - 55.000 1,72
G OPERATING INCOME (F-F1) - - - 138 -
G1 Interest costs - - - 0 0,00
H INCOME BEFORE INCOME TAXES (G-G1) - - - 138 -
Income taxes - - - 0 -
I NET INCOME (NI) - - - 138 -
Purpose of this study was to analyze economic feasibility of the investment in construction
and equipping new boiler facility on biomass fuel.
Analyses of the current oil boiler facility shows that total costs of production of energy are
taken as a base for calculating cost of production of energy in facility of 1.264 m2
and are
2,525 din/m2 so profit basically does not exist since we are calculating savings in costs as a
feasibility of the new investment.
Table 27. Projected income statement - first year of operations
ELEMENTS Unit Unit price Quantity Total
amount
(2012.)
Structure
(%)
(1) (2) (3) (4) (5) (6) (7)
A REVENUE - - - 3.191.600 -
Heating of the premises (production costs 2011.) m2 2525,00 1264,00 3.191.600 -
B OPERATING COSTS - - - 790.196 -
Material costs (produced energy) din/kWh 3,66 205244,71 751.196 26,17
Costs of energy (electricity,water) - - 39000,00 39.000 1,36
C TOTAL COSTS (B+E+F1+G1) - - - 2.870.706 -
D GROSS PROFIT (A-B) - - - 2.401.404 -
E GENERAL/ADMIN. EXPENCES - - - 1.376.955 -
Gross salaries worker 813600,00 1 813.600 28,34
Cost of services (maintainance costs,etc.) - - 75119,56 75.120 2,62
56
(1) (2) (3) (4) (5) (6) (7)
Nonmaterial costs - - - 488.235 17,01
F INCOME WITH DEPRECIATION (D-E) - - - 1.024.449 -
F1 Depreciation - - - 428.727 14,93
G OPERATING INCOME (F-F1) - - - 595.722 -
G1 Interest costs - - - 274.828 9,57
H INCOME BEFORE INCOME TAXES (G-G1) - - - 320.894 -
Income taxes - - - 0 -
I NET INCOME (NI) - - - 320.894 -
In the structure of the revenues in upper table total costs of heating are calculated and based
on those costs and lower costs of new investment net income is calculated. This net income
represents savings in costs based on new technology and investment in construction and
equipping of biomass boiler.
Due to the usage of new biomass boilers costs of energy has been gradually increased
specially in old boilers since maintenance costs are rather high (30%) due to the very old
technology.
In firts year of the new investment business is positive with net income of 320.894 din.
while in the following years net income is gradually positive.
Projected income statement has been prepared for 5 years with proportional increase of
incomes and expences.
Year 2012 2013 2014 2015 2016
(1) (2) (3) (4) (5) (6) (7)
A REVENUE 3.191.600 3.415.012 3.654.063 3.909.847 4.183.537
Heating of the premises (production
costs 2011) 3.191.600 3.415.012 3.654.063 3.909.847 4.183.537
B OPERATING COSTS 790.196 798.098 806.079 814.139 822.281
Material costs (produced energy) 751.196 758.708 766.295 773.958 781.697
Costs of energy (electricity,water) 39.000 39.390 39.784 40.182 40.584
C GROSS PROFIT (A-B) 2.401.404 2.616.914 2.847.984 3.095.708 3.361.256
D GENERAL/ADMIN. EXPENCES 1.376.955 932.607 941.583 950.649 959.805
Gross salaries 813.600 821.736 829.953 838.253 846.635
Cost of services(maintainance
costs,etc.) 75.120 75.871 76.629 77.396 78.170
Nonmaterial costs 488.235 35.000 35.000 35.000 35.000
E INCOME WITH
DEPRECIATION (C- D) 1.024.449 1.684.308 1.906.401 2.145.059 2.401.451
57
(1) (2) (3) (4) (5) (6) (7)
Depreciation 428.727 404.109 381.023 359.372 339.062
F OPERATING INCOME (E-E1) 595.722 1.280.199 1.525.378 1.785.687 2.062.389
Interest costs 274.828 223.578 170.534 115.633 58.811
G INCOME BEFORE INCOME
TAXES (F-F1) 320.894 1.056.621 1.354.844 1.670.054 2.003.578
Income taxes 0 0 0 0 0
H NET INCOME (NI) 320.894 1.056.621 1.354.844 1.670.054 2.003.578
Income structure
Projected income statement is prepared for 5 years.
In the first year operating income is equal to total costs with old boilers. Further in remaining
years 7% annual increase is calculated based on the yearly increase of raw energy sources.
Structure of the costs
Operating costs as well as general/admin. expences are increased 1% on annual bases.
In the structure of income statement income tax is not calculated since there is no realized
incomes hence investment should decrease cost of energy production.
We can conclude that project is profitable from the first year of implementation since net
income is positive from the second year.
Table 28. Depreciation calculation
No. Description of the fixed assests Investment value Depriciation
rate Value 2012.
1. Construction of the boiler
facility 5.136.820 0,066 339.030
2. Equipment – boiler and process
equipment 1.583.600 0,025 39.590
3. Heating pipes-instalation and
related works 2.004.289 0,025 50.107
TOTAL: 8.724.709
428.727
In calculation of the depreciation rate for item 1, rate is 6,6% for the depreciation period of 15
years. In calculation of the depreciation rate for item 2 and 3, rate is 2,5% for the depreciation
period of 40 years.
3.6.2.2. Financial and economic cash flow
a) Financial cash flow – is specific cash-flow which purpose is to show enterprise liquidity.
As well as income statmenet shows all incomes and expences also financial cash-flow shows
all money incomes and costs.
58
Table 29. Financial cash-flow
Years 0 1 2 3 4 5
A INFLOW (1+2+3+4) 9.248.498 3.191.600 3.415.012 3.654.063 3.909.847 11.083.506
1 Total revenue - 3.191.600 3.415.012 3.654.063 3.909.847 4.183.537
2 Source of financing 9.248.498 - - - - -
a/ Loan sources 7.852.238 - - - - -
b/Own capital 1.396.260 - - - - -
3
Remaining value-fixed
assets - - - - - 6.812.416
4 Remaining value-
working capital - - - - - 87.554
B OUTFLOW
(5+6+7+8+9+10) 9.248.498 3.946.270 3.479.876 3.498.653 3.516.397 3.534.372
5 Investments 9.248.498 - - - - -
a/Fixed assets 8.724.709 - - - - -
b/Working capital 87.554 39.995 10.047 11.867 12.484 13.161
c/Project
documentation 436.235 - - - - -
6 Material costs
(produced energy) - 751.196 758.708 766.295 773.958 781.697
7 Costs of energy
(electricity,water) - 39.000 39.390 39.784 40.182 40.584
8 Gross salaries - 813.600 821.736 829.953 838.253 846.635
9 General/admin.
expences - 1.376.955 932.607 941.583 950.649 959.805
10 Annuity (1+2) - 1.739.124 1.739.124 1.739.124 1.739.124 1.739.124
1. Interest costs - 274.828 223.578 170.534 115.633 58.811
2.Instalment - 1.464.296 1.515.547 1.568.591 1.623.491 1.680.314
C INCOME (A-B) 0 -754.670 -64.864 155.410 393.451 7.549.135
b) Loan repayment plan
In exploring financing sources for the investment current possible funds are:
Serbian development fund
Loans are available for repayment period of 5 years with the possibility of grace period of one
year. Turija is in the third group with the annual interest rate from 1,5-2,5% 3% with the
down payment of 10-30% depends on loan securities. Biggest amount of loans available is 50
million dinars.
59
Table 30. Loan repayment plan
Investment-fixed assets 8.724.709
Loan amount (90%) 7.852.238
Interest rate 3,5%
Years 5
Yearly number of instalments 4
No. Annual instalment Annual interest rate Annual annuity
1 1.464.296 274.828 1.739.124
2 1.515.547 223.578 1.739.124
3 1.568.591 170.534 1.739.124
4 1.623.491 115.633 1.739.124
5 1.680.314 58.811 1.739.124
6 7.852.238 843.384 8.695.622
When loan repayment calculated it was considered that loan money for this purposes could be
obtained under preffered rates of 3,5% which is the highest than available at the fund.
c) Economic flow is cash-flow projected to provide estimation of the profitability but
considered over the year of the project implementation. Economic flow in his inflows
consider total revenue plus remaining value of the fixed assets and does not include source of
financing. They are not considered since in the profitability computation should be seen at
what extend and period project can pay back investments.
On the other hand in the outflows all investment costs are considered. Becouse of this in the
expences depreciation is not calculated, if this should have been done “costs” related to fixed
assets would be counted twice.
Table 31. Economic flow of the project
Years 0 2012 2013 2014 2015 2016
(1) (2) (3) (4) (5) (6) (7) (8)
A INFLOW (1+2+3) 0 3.191.600 3.415.012 3.654.063 3.909.847 11.083.506
1 Total revenue 0 3.191.600 3.415.012 3.654.063 3.909.847 4.183.537
2 Remaining value-fixed
assets - - - - - 6.812.416
3 Remaining value-
working capital - - - - - 87.554
B OUTFLOW
(4+5+6+7+8) 9.248.498 2.207.145 1.740.751 1.759.528 1.777.272 1.795.247
4 Investments 9.248.498 - - - - -
60
(1) (2) (3) (4) (5) (6) (7) (8)
a/Fixed assets 8.724.709 - - - - -
b/Working capital 87.554 39.995 10.047 11.867 12.484 13.161
c/Project
documentation 436.235 - - - - -
5 Material costs (produced
energy) - 751.196 758.708 766.295 773.958 781.697
6 Costs of energy
(electricity,water) - 39.000 39.390 39.784 40.182 40.584
7 Gross salaries - 813.600 821.736 829.953 838.253 846.635
8 General/admin.
expences - 1.376.955 932.607 941.583 950.649 959.805
C INCOME (A-B) -9.248.498 984.455 1.674.261 1.894.535 2.132.575 9.288.259
3.6.2.3. Feasibility evaluation of the project
When the table of the economic flow is projected and appropriate incomes are calculated (net-
incomes) this is the point when project valuation can start. Investment projects are basically
rated according to the two type of the ratios: first is based on the static parameters (static
evaluation) and second are based on dynamic parameters (dynamic evaluation) of the project
efficiency.
Static evaluation is based on individual ratios that are calculated from the income statement
and financial cash-flow and from balance sheet from the “representative year” of the project
implementation (normaly it is 5th
year). In our case we will use as reference year third year
of project implementation.
Number of ratios that will be calculated are:
Profitability ratio
Cost of the project ratio
Accumulation ratio
Dynamic evaluation - with this evaluation is is foreseen to calculate two major
parametars, liquidity and profitability of the investments.
Numbers of ratios that will be calculated are:
Time of return of investments
Liquidity of the project (liquidity in certain year of the implementation and general
liquidity which will be assessed by comparing cumulative inflows and outflows)
Internal rate of return
Net present value
61
3.6.2.3.1 Static evaluation of the project
In order to asses static parametars values from the income statement are used for the year
2014 since project liquidity is from the first year of project implementation.
a) Profitability ratio
Profitability rate = ( Net income : Total revenues x 100 )
R = 1.354.844 / 3.654.063 x 100 = 37,1%
b) Cost of the project ratio
Cost of the project rate (Total revenues : Total expences x 100 )
E = 3.654.063 / 2.299.219 x 100 = 159%
c) Accumulation ratio
Accumulation rate (Net income / Total investment x 100)
A = 1.354.844 / 9.248.498 X 100 = 14,6%
Accumulation rate was calculated in relation to the total investment value for the project.
3.6.2.3.1 Dynamic evaluation of the project
a) Time of return of investments
Time of return of investments shows the period of time that money invested in project will be
returned to investor. In this calculation time of return was calculated based on the value
of total investment. Net incomes are basicaly decreased costs compared to ”old
investment”.
Calculation of this ratio is relatively strait: amounts of annual net incomes are deducted from
amounts of annual investments in economic flow.
Table 32. Time of return of investments
Years in project implementation Net incomes Unpaid investment instalment
"O" -9.248.498
2012 984.455 8.264.044
2013 1.674.261 6.589.783
2014 1.894.535 4.695.249
2015 2.132.575 2.562.673
2016 9.288.259 -6.725.586
VPI = 4,3
Time of return of investments is 4,3 years. Since investment amount is relatively high this is
optimum period of return of investments having in mind that 100% of the investment is
compared, amount that will be borrowed from investment funds. Structure of net incomes is
62
optimal and this time of return could be shorter which will depend on costs of materials,
amount of the investments as well as from management which will be separately evaluated
later in sensitivity analyses.
b) Liquidity of the project
Based on the projected financial cash-flow analyses it can be concluded that project liquidity
is full in whole implementation period of 5 years.
We can conclude that project is liquid from the third year of project implementation. This is
mainly becouse of high reduction in costs and investment is feasible since liquidity is not in
danger.
c) Internal rate of return
Table 33. Internal rate of return calculation
Discount rate 10,00%
Year Net incomes Discount rate Net present value
0 -9.248.498 1,00000000 -9.248.498
1 984.455 0,90909091 894.959
2 1.674.261 0,82644628 1.383.686
3 1.894.535 0,75131480 1.423.392
4 2.132.575 0,68301346 1.456.578
5 9.288.259 0,62092132 5.767.278
NPV: 1.677.394
Discount rate 15,00%
Year Net incomes Discount rate Net present value
0 -9.248.498 1,00000000 -9.248.498
1 984.455 0,86956522 856.047
2 1.674.261 0,75614367 1.265.981
3 1.894.535 0,65751623 1.245.687
4 2.132.575 0,57175325 1.219.307
5 9.288.259 0,49717674 4.617.906
NPV: -43.569
IRR= 14,9
63
Internal rate of return is calculated as follows:
10 + [1.677.394 x (15 - 10) : (1.677.394 +43.569)]= 14,9%
Since calculated amount of IRR = 14,9% is higher from weighted value of the discount rate
which relates to the financial interest rate (3,5%), and based of this calculation project is
acceptable to be implemented.
d) Net present value of the project
Method of discounted cash-flow (DCF) value represents sum of present values of future cash-
flows that company generates. It is important to calculate future values of cash-flows which
are further discounted with related rate which represents business risk with evaluate present
values.
Table 34. Relative net present value calculation
Discount rate 10,00%
Year Net incomes Discount rate Net present value
0 -9.248.498 1,00000000 -9.248.498
1 984.455 0,90909091 894.959
2 1.674.261 0,82644628 1.383.686
3 1.894.535 0,75131480 1.423.392
4 2.132.575 0,68301346 1.456.578
5 9.288.259 0,62092132 5.767.278
6.725.586 NPV: 1.677.394
RNPV= 18,1
Relative net present value is calculated as follows:
RNPV= 1.677.394 / 9.248.498 X 100 = 18,1%
3.6.2.4. Sensitivity analyses and risk assesment
3.6.2.4.1. Static sensitivity analyses
Is related to the analyses of the critical break-even point, to evaluate static points in business
where results are changed from positive to negative.
Variables that are mostly calculated are: (i) minimum utilization rate; (ii) profitability break-
even point
a) Minimum utilization rate ratio
This indicator represents break even point in utilization of the production capacity, i.e.
determines the lowest capacity utilization where business is still generates profit.
This ratio is calculated as follows:
64
Utilization rate ratio (%)= Total fixed costs / Revenues – variable costs
Utilization rate ratio = 52,4% compared to year 2014
Table 35. Profitability break even point
Years 2012 2013 2014 2015 2016
1 Total revenue 3.191.600 3.415.012 3.654.063 3.909.847 4.183.537
2 Variable costs 790.196 798.098 806.079 814.139 822.281
3 Fixed costs 2.080.511 1.560.294 1.493.140 1.425.654 1.357.678
4 Gross margin(TR-VC) 2.401.404 2.616.914 2.847.984 3.095.708 3.361.256
5 Profitability brak even
point FC/TR-VC 2.765.114 2.036.147 1.915.751 1.800.586 1.689.814
Fixed/margin rate 86,6% 59,6% 52,4% 46,1% 40,4%
From the above calculations we can conclude that project for construction and instalation of
thermoenergetic facility is profitable, break even point-costs of production per 1m2decrease is
from 40,4% untill 59,6% in full implementation year.
3.6.2.4.2. Dynamic sensitivity analyses
Is related to the analyses of the type and direction of the changes of dynamic parametars of
effectiveness when chosed variables are changed.
Variables that are most commonly analysed are:
Input costs – changes are analysed based on the changes of input costs for the related
investment
Investment costs – changes related to the different construction, equipment costs, etc.
are analysed
Table 36. Dynamic sensitivity analyses
Parametars % change TRoI PR IRR RNPV
Input costs
Cost of produced energy -10,00 4,0 39,00% 15,7 21,6
Cost of produced energy 10,00 4,4 35,00% 14,0 14,7
Investment costs
IV -15,00 4,2 38,00% 16,2 24,0
Own contribution : loan 30 - 70 3,9 38,00% 16,7 39,6
Own contribution : loan 50 - 50 3,1 39,00% 27,5 123,6
Best scenario
IV
Own contribution : loan
-10,00
50 - 50 2,9 39,00% 28,4 133,4
65
TRoI – Time of return of investments, PR – Profitability rate, IRR – Internal rate of return,
RNPV – Relative net present value, IV – Investment value
From the results of this analyses the following conclusions are:
Scenario - Input costs changed
There is much lower degree of sensitivity to variation in the price of pellets which has
a positive effect on profitability and payback time. If contracted supply of pellets from
local companies it is expected that price will be stable.
Scenario - Investment costs changed
Higher degree of sensitivity is If investments are more efficient i.e. lower, there will
be decrease in TRoI, IRR and RNPV will be higher. It is expected that when business
plan for final investment and tender will be realized prices of investment will drop
from 5-15% respectively.
If investment would be financed 100% by loans it would be still possible to take loan
from commercial banks since IRR is slightly positive while profitability is still high
thus development funds will be the main sources of financing.
Best case scenario
Focus in next period should be in optimization of the investments and usage of
development funds from IPA preaccesion programs for financing projects
3.6.2.4.3. Potential risk analyses
In this chapter we will analyze the following:
1. Rekonstruction of the existing boiler facility and exchange of the current boiler
with the biomass one
In Table 37 potential risk analyses is presented with type of risk and preventive measures for
the investment of thermoenergetic facility
Table 37. Potential risk analyses
No
. Risk type
NO/Y
ES Preventive measure
1. Reducing the need for service NO Keeping energy prices on stable level. Prices of energy
could be controled, even decreased if boilers are
replaced
2. Irregularity in supply of raw
materials or spare parts
NO Slabile contracts for biomass suply
3. Unequal quality of raw materials or
spare parts
NO Slabile contracts for biomass suply
4. Lack of skilled labor NO Additional training for working with new boilers
5. Changing the value of money in
country YES Stable financing resources
6. Changing prices for raw materials YES Slabile contracts for biomass suply
66
7. Changed market regulations YES Project should be fully adopted with the EU
requirements in next 5-10 years
2. Improving current efficiency of the boilers and heating systems by introducing
short term investments
Table 38. Anylizes of the cost savings vs. new investments
TYPE OF WORKS
Energy savings
(per year)
Investments
(din)
Ratio-energy savings vs. investments
Styrofoam instalation 191.771,73 1.326.629,00 1:6,9
Instalation of windows 142.622,85 266.690,00 1:1,9
UKUPNO: 334.394,59 1.593.319,00 1:4,4
From the current table we can see overview of the potential construction works. We could
notice that with the styrofoam instalation investment value is 6,9 times higher compared to
annual cost savings. With the instalation of windows investment is 1,9 times higher compared
to annual cost savings.
From this analyse we can conclude the following:
- since the age of the current boilers is over 40 years, there is a very high risk to finance
full investment while still old boilers needs to be changed sooner or later
- only feasible short term action is instalation of termostatic valves since their value
could be returned in short period of time
3.6.2.5. Analyses of financial sources and financial liabilities
In the projected investment 90% of the investment will be provided from the loan, while
another 10% will be from own resources or other grant sources. It is estimated that loans will
be taken from domestic resources (National investment fund, Vojvodina development fund,
Serbian development fund, etc.). For the remaining 10% there should be subsidies obtained
from Serbian funds as well as EU pre accesion funds for improving energy efficiency on local
level.
3.6.3. Economic evaluation of the project
Major conclusions of the economic evaluation – investment feasibility of the thermoenergetic
facility for heating public facility in Kuĉevo Municipality are as follows:
Liquidity of the project after third year of investment
Project need to provide 10% of own financial resources
Cost of the project ratio is (159%) and accumulation ratio is (14,6%)
Project is profitable (37,1%) in all implementation years
Time of return of investments is 4 years and 3 months
Project is with low risk
67
Public approval is high – biomass will be obtained from local companies and
dependance on used wood will be reduced with the good impact of environment
3.6.4. Summarized economic feasibility investment evaluation
Based on the proposed technology, analyses of economic parameters as well as finacial
analyses overall conclusions are:
Study shows that investment in biomass boilers is feasible for heating choosed public
facilities in Turija Municipality
Economic parameters are positive for usage of biomass in region of Turija
Municipality which affects increased household incomes
Looking in the long term there will be reduced usage of natural wood which will have
positive impact on the environment as well as reduction of gas emmisions with usage
of modern boilers
Stability of supply of raw materials and price stability of heating costs will be
achieved as well as decrease of heating costs will be obtained on the long run
Worst case scenario – is if 90% of the loan is taken from development fund and if energy
price increase for 10% (Table 36), but in this scenario all results are positive, profitability rate
is 35%, IRR is 14,0%, time of the investment return is 4,4 years.
Optimum scenario – 30% potential subsidy/grant and loan from development fund of 70%
(Table 36). Results are very positive, time of the ivestment return is 3,9 years, IRR is 16,7%
and after this period price of heating per 1 m2 could drop by 52-54% (Table 35).
The best case scenario – 50% potential subsidy/grant and loan from even commertial of
50% (Table 36). and increase in investment costs of 10%. IRR here is 28,4% , time of the
ivestment return is 2,9 years and after this period price of heating per 1 m2 could drop by 46-
48% (Table 35)
68
3.7. Conclusions
Kuĉevo municipality has at its disposal 32.215 ha of agricultural soil and 35.915 ha of forests.
Total average sown area is 11.870 ha, with 6.600 ha under corn, 4.150 ha under wheat, 1.100
ha under barley and 20 ha under sunflower. Other cultures hold less area.
It is estimated that the total amount of agricultural biomass that can be gained from
aforementioned agricultural land is 52.296 t annually, when it would be converted into energy
715.022.000 MJ of thermal energy would be gained.
The total savings that can be achieved in terms of energy amounts are 933.746.210 MJ, and
that amount of energy would enable the municipality of Kuĉevo to build thermal power plant
of over 10 MW.
In paricular it can be saved 7.768.698 € from all available biomass.
The most important criteria when selecting public use property to be heated by thermal energy
gained from biomass combustion are:
that they are public use properties significant to local self-government,
that there is one or more facilities, that have need for large amount of thermal energy,
taht facilities location is not intertwined with existing piping systems (central heating
system of city), i.e. that they are located in places where city‟s central heating network
will not reach in foreseeable future,
that selected locations have enough space for the construction the boiler plant and
smaller biomass depot, including physical separation from existing units, (manly due to
hygienic and fire safety requirements),
that the location for construction of the facility is in the vicinity of existing gas or liquid
fuel powered boilers, so that systems of boiler facilities can work complementarily, i.e.
to use joint collectors,
that properties have satisfactory internal pipe network of heating units or that it doesn‟t
have any installations so the internal heating installation of adequate technical
characteristics can be designed and built,
that the owner of the location where the boiler plant and depot are planned is known,
that pipe installation between several selected objects will not be overly long and
complex for construction,
that there are adequate access roads for depot facilities for delivery of biomass for
combustion and other purposes.
Considering set criteria and on the basis of the perceived situation of properties of stated
public services and institutions in the Kuĉevo municipality, as well as on the basis of the
proposal of municipal management, and in agreement with the representative of UNDP
Serbia, it has been decided that heating with the system powered by biomass uses for
generating heat for two public facilities in Kuĉevo:
Elementary School „Veljko Dugošević“ in Turija
69
Starting with selected types and forms of biomass to be used for combustion, spatial
limitations, ecological and legal norms and standards with the imperative for minimal
expenses for the Kuĉevo municipality thermo energetic facility where wood pellets burned by
a stoker with a moving andiron.
The technology suggested has several important advantages that could be briefly described as
the following:
It combusts fuel (wood pellets) which is very common on the Serbian market. The
fuel could be bought successively, i. e. as needed, which means that it is not
necessary to buy the total amount of fuel needed once a year,
Combustion of wood pellets could be completely automated with a total
mechanization of the pellet manipulation process,
Emission of harmful gasses could be maintained in the allowed limits,
The wood pallet combustion plant could be put in various modes,
While working in this plant, the wood pellets will not be affected by the problems of
solubility as is the case with combustion of biomass form the agricultural production.
It is defined that thermal energy facility for heating of selected facilitirs in Kuĉevo should
operate on wood pellets, and as such must satisfy the following technical, economic and
ecological requirements:
That it produces required quantity of energy (300 kW),
That existing equipment and infrastructure be used optimally,
That high level of cost effectiveness ensured in the operation of the facility, i.e. a
competitive cost of production of thermal energy compared to production where wood and coal is used,
That environment pollution is in accordance with local and European norms,
That a high level of reliability and availability of the facility be ensured in all work
modes,
That modern level of work management and control be ensured in both facilities,
That modern level of maintenance beensured with minimal expenses,
That during the manipulation of bales of biomass for combustion satisfactory hygienic
conditions be maintained,
It is expected that energy efficiency of the facilities for combustion of wood pellets in
Kuĉevo, during the work with wood pellets of 12% moisture,will be 85%.
The new boiler is going to work in 90/70oC regime, since the current heating system operates
in that regime.
For the preparation of the sanitary water, in the new boiler room, provided is a standing hot
water boiler made of stainless material, with a volume of V = 300 l.
70
Expenses for the construction of the thermal energy facility for heating of public use
properties in Kuĉevo are 9.137.894 din, for the value of euro of 114 din/€.
Termo – tecnical an processing equipment 5.136.820 din
Building a boiler house 1.583.600 din
Hot water pipe lines 926.509 din
Makeing of internal termotehnical installation 1.077.780 din
Project documentation 413.185 din
Unit costs of the investment are:
Compared to installed power: 30.459,65 din/kW
Compared to heating area: 7.229,35 din/m2
Maximum declared hourly expenditure of biomass in the boiler facility is 70,59 kg/h.
Seasonal consumption of biomass as fuel is subject to change and mostly depends of external
i.e. exploitation conditions during the heating season. According to total losses of selected
public use properties in Kuĉevo is necessary to provide 62.627 t/heating season of biomass
(decided on wood pellets).
Pellets will be purchased in the continuity from the market and they will be stored in the
existing coal storage in jumbo bags, so there is no need for construction of any storages.
Transport of pellets to boiler facility should be conceived that onecs a mounth a truck with
crain brings 11 jumbo bags with pellets.
3.6.3. Economic evaluation of the project
Major conclusions of the economic evaluation – investment feasibility of the thermoenergetic
facility for heating public facility in Kuĉevo Municipality are as follows:
Liquidity of the project after third year of investment
Project need to provide 10% of own financial resources
Cost of the project ratio is (159%) and accumulation ratio is (14,6%)
Project is profitable (37,1%) in all implementation years
Time of return of investments is 4 years and 3 months
Project is with low risk
Public approval is high – biomass will be obtained from local companies and
dependance on used wood will be reduced with the good impact of environment
Summarized economic feasibility investment evaluation
Based on the proposed technology, analyses of economic parameters as well as finacial
analyses overall conclusions are:
Study shows that investment in biomass boilers is feasible for heating choosed public
facilities in Kuĉevo municipality
71
Economic parameters are positive for usage of biomass in region of Turija
Municipality which affects increased household incomes
Looking in the long term there will be reduced usage of natural wood which will have
positive impact on the environment as well as reduction of gas emmisions with usage
of modern boilers
Stability of supply of raw materials and price stability of heating costs will be
achieved as well as decrease of heating costs will be obtained on the long run
72
3.8. Literature
[1] Bogdanović, Darinka: “Biološko ratarenje – stvarnost ili utopija”, Zbornik radova, 16, XXIV Seminar Agronoma, Pula, 1989.
[2] Brkić, M, Janić, T.: Mogućnosti korišćenja biomase u poljoprivredi, Zbornik radova sa
II savetovanja: “Briketiranje i peletiranje biomase iz poljoprivrede i šumarstva“, Regionalna privredna komora, Sombor, »Dacom«, Apatin, 1998, s. 5-9.
[3] Brkić, M, Janić, T, Somer, D.: Termotehnika u poljoproivredi, II – deo: Procesna
tehnika i energetika, udţbenik, Poljoprivredni fakultet, Novi Sad, 2006. s. 323.
[4] Brkić, M, Tešić, M, Radojević, V, Potkonjak, V, Janić, T, Mehandţić, R, Dakić, D,
Mesarović, M, Radojević, Vuk, Tehno-ekonomska karakterizacija, tipizacija i izbor
kapaciteta i postrojenja za korišćenje biomase u sušarama i proizvodnim pognima ZZ
“Bag-Deko“ u Baĉkom Gradištu, studija, Poljoprivredni fakultet, Novi Sad, 2007, s.
151.
[5] Brkić, M, Janić, T.: Briketiranje i peletiranje biomase, monografija, Poljoprivredni fakultet, Novi Sad, 2009., s. 277.
[6] Brkić, M, Janić, T: Nova procena vrsta i koliĉina biomasa Vojvodine za proizvodnju
energije , ĉasopis: “Savremena poljoprivredna tehnika“, JNDPT, Novi Sad, 36(2010)2, s. 178-188.
[7] Brkić, M, Janić, T, Pejanović, R, Zekić, V: Studija: Sistem za toplovodno grejanje
naselja Petrovaradin, Poljoprivredni fakultet, Novi Sad, 2010, s. 420.
[8] Burk H., Hentschel A., 2000: Brennkegel-Rostfeuerung fur Gebrauchtholz. In:
Proceedings of the VDI Seminar "Stand der Feuerungstechnik fur Holz, Gebrauchtholz
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76
4. APPENDIX
A. TEXT APPEDNDIX
01. CALCULATION OF HEAT LOSS OF HEAT
02. BILL OF QUANTITIES OF BUILDING A NEW BOILER ROOM
B. GRAPHICAL APPENDIX
01. OVERVIEW OF OBJECT TO SETTLEMENT SATELLITE IMAGE
02. SITE PLAN
03. GOROUND FLOOR WITH HEATING INSTALLATIONS
04. FIRST FLOOR WITH HEATING INSTALLATIONS
05. SITE PLAN WITH HOT WATER PIPE LINES
06. TECHNOLOGICAL SCHEME
07. CONNECTION OF ELEMETS IN THE BOILER ROOM - SCHEME
08. CONNECTING OF ELEMENTS IN THE BOILER ROOM
TECHNICAL CALCULATIONS
STATUS OF ROOMS
Room Room Temp. in Temp. in Heat losses Room
number name win. mode summ. mode in the room status
- - tp tp Q -
- - oC
oC W -
01 02 03 04 05 06
G R O U N D F L O O R
1 WINDSHIELD 15 26 1448 TREATED
2 HALL 20 26 8411 TREATED
3 CLASSROOM 20 26 10050 TREATED
4 OFFICE 20 26 2584 TREATED
5 OFFICE 20 26 2314 TREATED
6 PRINCIPAL'S OFFICE 20 26 4941 TREATED
7 CLASSROOM 20 26 10925 TREATED
8 CLASSROOM 20 26 7700 TREATED
9 DINING ROOM 20 26 17213 TREATED
10 KITCHEN 18 26 2509 TREATED
11 KITCHEN - FOOD ISSUE 18 26 2741 TREATED
12 STORAGE 3 26 - NOT TREATED
13 SPORTS ROOM 20 26 13053 TREATED
14 DRESSING ROOM FOR TEACHERS 24 26 1814 TREATED
15 WAREHOUSE 3 26 - NOT TREATED
16 DRESSING ROOM 1 24 26 1682 TREATED
17 DRESSING ROOM 2 24 26 1200 TREATED
18 HALL 20 26 1647 TREATED
19 MALE TOILET - STUDENTS 20 26 1367 TREATED
20 MALE TOILET - TEACHERS 20 26 179 TREATED
21 FEMALE TOILET - TEACHERS 20 26 896 TREATED
22 TOILET - HALL 20 26 748 TREATED
23 FEMALE TOILET - STUDENTS 15 26 1367 TREATED
T O T A L: 94789
F I R S T F L O O R
1,1 HALL 20 26 2982 TREATED
1,2 CLASSROOM 20 26 10242 TREATED
1,3 CLASSROOM 20 26 5934 TREATED
1,4 CLASSROOM 20 26 8026 TREATED
1,5 CLASSROOM 20 26 11557 TREATED
1,6 CLASSROOM 20 26 7497 TREATED
1,7 CLASSROOM 20 26 7747 TREATED
1,8 CLASSROOM 20 26 7776 TREATED
1,9 CLASSROOM 20 26 7662 TREATED
1,10 LIBRARY 20 26 3873 TREATED
1,11 HALL 20 26 17396 TREATED
1,12 STAIRS 20 26 2883 TREATED
1,13 CLASSROOM 20 26 8274 TREATED
T O T A L: 101847
S U M M A R Y
G R O U N D F L O O R 94789
F I R S T F L O O R 101847
T O T A L: 196636
HEAT TRANSFER COEFFICIENT TECHNICAL CALCULATIONS
Material Thickness Heat transf. coeff. Thermal resist.
- d l R
- m W/mK m2K/W
01 02 03 04
FRONTAL WALL 1
Mortar 0,025 0,870 0,029
Solid brick 0,450 0,740 0,608
Lime mortar 0,020 0,810 0,025
T O T A L: 0,50 0,662
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 0,832
HEAT TRANSFER COEFFICIENT k W/m2K 1,20
FRONTAL WALL 2
Mortar 0,025 0,870 0,029
Solid brick 0,300 0,740 0,405
Lime mortar 0,020 0,810 0,025
T O T A L: 0,35 0,459
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 0,629
HEAT TRANSFER COEFFICIENT k W/m2K 1,59
FRONTAL WALL 3
Mortar 0,025 0,870 0,029
Clay block 0,250 0,580 0,431
Lime mortar 0,020 0,810 0,025
T O T A L: 0,30 0,485
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 0,655
HEAT TRANSFER COEFFICIENT k W/m2K 1,53
INTERNAL WALL 1
Lime mortar 0,025 0,810 0,031
Solid brick 0,450 0,740 0,608
Lime mortar 0,025 0,810 0,031
T O T A L: 0,50 0,670
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 0,930
HEAT TRANSFER COEFFICIENT k W/m2K 1,08
INTERNAL WALL 2
Lime mortar 0,025 0,810 0,031
Solid brick 0,300 0,740 0,405
Lime mortar 0,025 0,810 0,031
T O T A L: 0,35 0,467
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 0,727
HEAT TRANSFER COEFFICIENT k W/m2K 1,38
INTERNAL WALL 3
Lime mortar 0,025 0,810 0,031
Solid brick 0,150 0,740 0,203
Lime mortar 0,025 0,810 0,031
T O T A L: 0,20 0,265
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 0,525
HEAT TRANSFER COEFFICIENT k W/m2K 1,91
INTERNAL WALL 4
Lime mortar 0,025 0,810 0,031
Clay block 0,200 0,580 0,345
Lime mortar 0,025 0,810 0,031
T O T A L: 0,25 0,407
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 0,667
HEAT TRANSFER COEFFICIENT k W/m2K 1,50
FLOOR ON THE GROUND 1
Decking floor 0,024 0,140 0,171
Cement layer 0,030 1,400 0,021
Charged concrete 0,150 2,330 0,064
Waterproofing 0,001 0,000
Gravel 0,100 0,000
T O T A L: 0,31 0,256
Thermal resistance from the inside 0,170
Air layer thermal resistance -
Thermal resistance from the outside 0,000
TOTAL THERMAL RESISTANCE: 0,426
HEAT TRANSFER COEFFICIENT k W/m2K 2,35
FLOOR ON THE GROUND 2
Ceramic tiles 0,010 1,050 0,010
Cement layer 0,040 1,400 0,029
Charged concrete 0,150 2,330 0,064
Waterproofing 0,001 0,000
Gravel 0,100 0,000
T O T A L: 0,30 0,103
Thermal resistance from the inside 0,170
Air layer thermal resistance -
Thermal resistance from the outside 0,000
TOTAL THERMAL RESISTANCE: 0,273
HEAT TRANSFER COEFFICIENT k W/m2K 3,66
FLOOR ON THE GROUND 3
Ceramic tiles 0,010 1,050 0,010
Cement layer 0,040 1,400 0,029
Tervol 0,050 0,041 1,220
Charged concrete 0,100 2,330 0,043
Waterproofing 0,001 0,000
Gravel 0,100 0,000
T O T A L: 0,30 1,302
Thermal resistance from the inside 0,170
Air layer thermal resistance -
Thermal resistance from the outside 0,000
TOTAL THERMAL RESISTANCE: 1,472
HEAT TRANSFER COEFFICIENT k W/m2K 0,68
STRUCTURAL FLOORS 1
Decking floor 0,024 0,210 0,114
Slug (buffer) 0,060 0,190 0,316
AB board 0,100 2,040 0,049
Vazduh 0,300 0,000 0,120
Wood (lath) 0,030 0,140 0,214
Reed 0,015 0,093 0,161
Reedy mortar 0,025 0,170 0,118
T O T A L: 0,55 1,092
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 1,352
HEAT TRANSFER COEFFICIENT k W/m2K 0,74
STRUCTURAL FLOORS 2
Parquet 0,024 0,210 0,114
Cement screed 0,040 1,400 0,029
Concrete 0,040 2,040 0,020
TM 3 0,160 0,580 0,276
Lime mortar 0,020 0,810 0,025
T O T A L: 0,28 0,464
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,130
TOTAL THERMAL RESISTANCE: 0,724
HEAT TRANSFER COEFFICIENT k W/m2K 1,38
STRUCTURAL FLOOR TO ATTIC 1
Wooden piles 0,030 0,140 0,214
Attic (mud+straw) 0,080 0,700 0,114
AB board 0,100 2,040 0,049
Air 0,300 0,000 0,120
Wood (lath) 0,030 0,140 0,214
Reed 0,015 0,093 0,161
Reedy mortar 0,020 0,170 0,118
T O T A L: 0,58 0,990
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 1,160
HEAT TRANSFER COEFFICIENT k W/m2K 0,86
STRUCTURAL FLOOR TO ATTIC 2
PVC foil 0,003 0,000 0,000
Tervol 0,050 0,041 1,220
Concrete 0,040 2,040 0,020
TM 3 0,160 0,580 0,276
Lime mortar 0,020 0,810 0,025
T O T A L: 0,27 1,541
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 1,711
HEAT TRANSFER COEFFICIENT k W/m2K 0,58
STRUCTURAL FLOOR TO OPEN PASSAGE
Decking floor 0,024 0,210 0,114
Slug (buffer) 0,060 0,190 0,316
AB board 0,100 2,040 0,049
Air 0,300 0,000 0,120
Wood (lath) 0,030 0,140 0,214
Reed 0,015 0,093 0,161
Reedy mortar 0,020 0,170 0,118
T O T A L: 0,55 1,092
Thermal resistance from the inside 0,130
Air layer thermal resistance -
Thermal resistance from the outside 0,040
TOTAL THERMAL RESISTANCE: 1,262
HEAT TRANSFER COEFFICIENT k W/m2K 0,79
EXTERNAL WOODEN WINDOW WITH SPACED WINGS
HEAT TRANSFER COEFFICIENT k W/m2K 2,90
EXTERNAL WOODEN DOOR (WITH GLASS)
HEAT TRANSFER COEFFICIENT k W/m2K 3,50
EXTERNAL TERMAL INSULATED METAL DOOR
HEAT TRANSFER COEFFICIENT k W/m2K 4,00
INTERNAL WOODEN DOOR
HEAT TRANSFER COEFFICIENT k W/m2K 2,30
INTERNAL WOODEN WINDOW
HEAT TRANSFER COEFFICIENT k W/m2K 3,40
HEAT LOSS CALCULATION
Heat loss calculation is done according to the formula:
Qg = Qt + Qd
Here is:
Qt - Transmission heat losses W
Transmission heat losses calculation is done according to the formula:
Qt = k x F x (tp - ts)
Here is:
k - Heat transfer coefficient through the barrier W m2K
F - Barrier area m2
tp - Design temperature in the room C
ts - External design temperature in winter mode C
Qd - Heat loss from supplements W
Heat loss from supplements is done according to the formula:
Qd = Qss + Qp + Qv
Here is:
Qss - Supplements to the side of world W
Qp - Supplements to the discontinuation of work W
Qv - Supplement to the outside air blowing through the windows joints [W]
Supplement to the outside air blowing through the windows joints is done
according to the formula:
Qv = * (a1 * l1) + (a2 * l2) * R * H * (tp - ts)
Ovde je:
- Height correction factor
a1 - Permeability through the outer window [m2/mhPa
2/3]a2 - Permeability through the outer door [m2
/mhPa2/3]
l1 - Gap length window [m]
l1 - Length of the neck joints [m]
R - Characteristics of the room
H - Performance of the building
Barr. Orien- Num. of Barrier Heat tr. Room Temp. Temp. Spec. Barrier Barrier Barrier Heat
mark tation peaces thick. coeff. temp. beh.barr. diff. heat flux length height area flux
- - n k tp ts t q L H F Q
- - - m W/m2K
oC
oC K W/m
2 m m m2 W
01 02 03 04 05 06 07 08 09 10 11 12 13
G R O U N D F L O O R
ROOM NAME: WINDSHIELD
ROOM NUMBER: 1
ROOM TEMPERATURE - tp: 15
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 - 1 - 0,74 15 20 -5 -3,70 3,00 2,70 8,10 -30
SZ 1 W 1 0,50 1,20 15 -18 33 39,66 2,70 4,25 11,48 455
PZ 2 - 2 0,35 1,38 15 20 -5 -6,88 3,00 4,25 12,75 -175
PZ 2 - 1 0,35 1,38 15 20 -5 -6,88 2,70 4,25 11,48 -79
SV W 1 - 3,50 15 -18 33 115,50 1,60 2,10 3,36 388
UV - 1 - 2,30 15 20 -5 -11,50 1,60 2,10 3,36 -39
PNT 2 - 1 0,30 3,66 15 3 12 43,96 3,00 2,70 8,10 356
ODB1 W 1 - 1,20 15 -18 33 39,66 1,65 -2,10 -3,47 -137
ODB2 - 1 - 1,38 15 20 -5 -6,88 1,65 -2,10 -3,47 24
TRANSMISSIVE HEAT LOSSES: Qh = 763
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 145
33 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =9,50 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 540
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 685
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1448
ROOM NAME: HALL
ROOM NUMBER: 2
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 E 1 0,50 1,20 20 -18 38 45,67 2,70 4,25 11,48 524
PZ 1 W 1 0,50 1,08 20 18 2 2,15 6,50 4,25 27,63 59
PZ 1 - 1 0,50 1,08 20 18 2 2,15 2,70 4,25 11,48 25
PZ 2 - 1 0,35 1,38 20 15 5 6,88 2,70 4,25 11,48 79
SV E 1 - 3,50 20 -18 38 133,00 1,40 2,10 2,94 391
UV - 1 - 2,30 20 18 2 4,60 0,90 2,10 1,89 9
UV - 1 - 2,30 20 15 5 11,50 1,60 2,10 3,36 39
PNT 2 - 1 0,30 3,66 20 3 17 62,27 1,00 88,24 88,24 5495
ODB1 E 1 0,50 1,20 20 -18 38 45,67 1,40 -2,10 -2,94 -134
ODB2 - 1 0,50 1,08 20 18 2 2,15 0,90 -2,10 -1,89 -4
ODB3 - 1 0,35 1,38 20 15 5 6,88 1,60 -2,10 -3,36 -23
TRANSMISSIVE HEAT LOSSES: Qh = 6459
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 1356
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =9,10 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 596
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1952
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 8411
ROOM NAME: CLASSROOM
ROOM NUMBER: 3
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 6,10 4,25 25,93 1184
SZ 1 N 1 0,50 1,20 20 -18 38 45,67 9,30 4,25 39,53 1805
PZ 1 - 1 0,50 1,08 20 18 2 2,15 6,10 4,25 25,93 56
SP N 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
PNT 1 - 1 0,31 2,35 20 3 17 39,91 6,10 9,30 56,73 2264
ODB1 N 1 - 1,20 20 -18 38 45,67 1,65 -6,30 -10,40 -475
TRANSMISSIVE HEAT LOSSES: Qh = 5980
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 299
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 1375
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 4070
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 10050
ROOM NAME: OFFICE
ROOM NUMBER: 4
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 2,80 4,25 11,90 544
SZ 1 S 1 0,50 1,20 20 -18 38 45,67 1,00 4,25 4,25 194
SP W 1 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 382
PNT 1 - 1 0,31 2,35 20 3 17 39,91 2,80 4,60 12,88 514
ODB1 W 1 0,50 1,20 20 -18 38 45,67 1,65 -2,10 -3,47 -158
TRANSMISSIVE HEAT LOSSES: Qh = 1475
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 310
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 799
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1108
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2584
ROOM NAME: OFFICE
ROOM NUMBER: 5
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 3,00 4,25 12,75 582
PZ 2 - 1 0,35 1,38 20 15 5 6,88 3,00 4,25 12,75 88
SP W 1 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 382
PNT 1 - 1 0,31 2,35 20 3 17 39,91 3,00 3,00 9,00 359
ODB1 W 1 0,50 1,20 20 -18 38 45,67 1,65 -2,10 -3,47 -158
TRANSMISSIVE HEAT LOSSES: Qh = 1253
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 263
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 799
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1062
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2314
ROOM NAME: PRINCIPAL'S OFFICE
ROOM NUMBER: 6
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 2,60 4,25 11,05 505
SZ 1 N 1 0,50 1,20 20 -18 38 45,67 1,00 4,25 4,25 194
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 3,10 4,25 13,18 602
PZ 2 - 1 0,35 1,38 20 15 5 6,88 3,00 4,25 12,75 88
SP W 2 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 764
PNT 1 - 1 0,31 2,35 20 3 17 39,91 1,00 23,26 23,26 928
ODB1 W 1 0,50 1,20 20 -18 38 45,67 1,65 -2,10 -3,47 -158
ODB2 W 1 0,50 1,20 20 -18 38 45,67 1,65 -2,10 -3,47 -158
TRANSMISSIVE HEAT LOSSES: Qh = 2764
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 580
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =24,40 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 1597
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 2178
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 4941
ROOM NAME: CLASSROOM
ROOM NUMBER: 7
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 6,10 4,25 25,93 1184
SZ 1 S 1 0,50 1,20 20 -18 38 45,67 9,30 4,25 39,53 1805
SZ 1 E 1 0,50 1,20 20 -18 38 45,67 6,10 4,25 25,93 1184
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
PNT 1 - 1 0,31 2,35 20 3 17 39,91 6,10 9,30 56,73 2264
ODB1 S 1 0,50 1,20 20 -18 38 45,67 1,65 -6,30 -10,40 -475
TRANSMISSIVE HEAT LOSSES: Qh = 7108
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -355
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 25% Qpr = 1777
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3817
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 10925
ROOM NAME: CLASSROOM
ROOM NUMBER: 8
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 S 1 0,50 1,20 20 -18 38 45,67 9,00 4,25 38,25 1747
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
PNT 1 - 1 0,31 2,35 20 3 17 39,91 9,00 6,00 54,00 2155
ODB1 S 1 0,50 1,20 20 -18 38 45,67 1,65 -6,30 -10,40 -475
TRANSMISSIVE HEAT LOSSES: Qh = 4573
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -229
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 960
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3127
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 7700
ROOM NAME: DINNING ROOM
ROOM NUMBER: 9
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 S 1 0,50 1,20 20 -18 38 45,67 9,30 4,25 39,53 1805
SZ 1 N 1 0,50 1,20 20 -18 38 45,67 12,00 4,25 51,00 2329
PZ 2 - 1 0,35 1,38 20 18 2 2,75 9,30 4,25 39,53 109
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
SP N 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
UV - 1 - 2,30 20 18 2 4,60 1,00 2,10 2,10 10
UP - 1 - 3,40 20 18 2 6,80 0,80 0,80 0,64 4
PNT 2 - 1 0,30 3,66 20 3 17 62,27 1,00 93,24 93,24 5806
ODB1 S 1 0,50 1,20 20 -18 38 45,67 1,65 -6,30 -10,40 -475
ODB2 N 1 0,50 1,20 20 -18 38 45,67 1,65 -6,30 -10,40 -475
ODB3 - 1 0,35 1,38 20 18 2 2,75 1,00 -2,50 -2,50 -7
TRANSMISSIVE HEAT LOSSES: Qh = 11398
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 570
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 25% Qpr = 2850
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 5815
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 17213
ROOM NAME: KITCHEN
ROOM NUMBER: 10
ROOM TEMPERATURE - tp: 18
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 - 1 0,55 0,74 18 20 -2 -1,48 2,90 6,00 17,40 -26
SZ 1 S 1 0,50 1,20 18 -18 36 43,27 2,90 4,25 12,33 533
PZ 2 - 2 0,35 1,38 18 20 -2 -2,75 6,00 4,25 25,50 -140
SP S 1 - 2,90 18 -18 36 104,40 1,65 2,10 3,47 362
UV - 1 - 2,30 18 20 -2 -4,60 1,00 2,10 2,10 -10
PNT 2 - 1 0,30 3,66 18 3 15 54,95 2,90 6,00 17,40 956
ODB1 S 1 0,50 1,20 18 -18 36 43,27 1,65 -2,10 -3,47 -150
ODB2 - 2 0,35 1,38 18 20 -2 -2,75 1,00 -2,10 -2,10 12
TRANSMISSIVE HEAT LOSSES: Qh = 1537
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -77
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 292
36 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 757
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 972
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2509
ROOM NAME: KITCHEN - FOOD ISSUE
ROOM NUMBER: 11
ROOM TEMPERATURE - tp: 18
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 - 1 0,55 0,74 18 20 -2 -1,48 3,00 2,90 8,70 -13
SZ 1 N 1 0,50 1,20 18 -18 36 43,27 3,00 4,25 12,75 552
PZ 2 - 1 0,35 1,38 18 20 -2 -2,75 2,90 4,25 12,33 -34
PZ 3 - 1 0,20 1,91 18 3 15 28,59 2,90 4,25 12,33 352
SP N 1 - 2,90 18 -18 36 104,40 1,65 2,10 3,47 362
UP - 1 - 3,40 18 20 -2 -6,80 0,80 0,80 0,64 -4
UV - 1 - 2,30 18 3 15 34,50 1,00 2,10 2,10 72
PNT 2 - 1 0,30 3,66 18 3 15 54,95 3,00 2,90 8,70 478
ODB1 N 1 0,50 1,20 18 -18 36 43,27 1,65 -2,10 -3,47 -150
ODB2 - 1 0,35 1,38 18 20 -2 -2,75 0,80 -0,80 -0,64 2
ODB3 - 1 0,20 1,91 18 3 15 28,59 0,70 -2,10 -1,47 -42
TRANSMISSIVE HEAT LOSSES: Qh = 1575
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 79
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 331
36 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 757
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1166
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2741
ROOM NAME: SPORTS ROOM
ROOM NUMBER: 13
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 S 1 0,50 1,20 20 -18 38 45,67 15,20 4,25 64,60 2950
SZ 1 E 1 0,50 1,20 20 17 3 3,61 6,00 4,25 25,50 92
PZ 2 - 1 0,35 1,38 20 -18 38 52,29 6,00 4,25 25,50 1333
PZ 2 - 1 0,35 1,38 20 18 2 2,75 3,10 4,25 13,18 36
PZ 2 - 1 0,35 1,38 20 3 17 23,39 5,50 4,25 23,38 547
PZ 2 - 1 0,35 1,38 20 24 -4 -5,50 4,60 4,25 19,55 -108
SP S 4 - 2,90 20 -18 38 110,20 1,10 1,40 1,54 679
SV 1 S 1 - 4,00 20 -18 38 152,00 1,40 2,60 3,64 553
UV - 1 - 2,30 20 24 -4 -9,20 0,90 2,10 1,89 -17
PNT 1 - 1 0,31 2,35 20 3 17 39,91 15,20 6,00 91,20 3639
ODB1 S 1 0,50 1,20 20 -18 38 45,67 1,00 -9,90 -9,90 -452
ODB2 - 1 0,35 1,38 20 3 17 23,39 0,90 -2,10 -1,89 -44
TRANSMISSIVE HEAT LOSSES: Qh = 9209
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -460
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 2118
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =33,40 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2186
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3844
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 13053
ROOM NAME: DRESSING ROOM FOR TEACHERS
ROOM NUMBER: 14
ROOM TEMPERATURE - tp: 24
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 - 1 0,55 0,74 24 20 4 2,96 2,00 2,90 5,80 17
SZ 1 N 1 0,50 1,20 24 -18 42 50,48 2,00 4,50 9,00 454
PZ 2 - 1 0,35 1,38 24 3 21 28,90 2,90 4,50 13,05 377
PZ 2 - 1 0,35 1,38 24 20 4 5,50 2,00 4,50 9,00 50
SP N 1 - 2,90 24 -18 42 121,80 0,80 0,80 0,64 78
UV - 1 - 2,30 24 20 4 9,20 0,90 2,10 1,89 17
PNT 1 - 1 0,31 2,35 24 3 21 49,30 2,00 2,90 5,80 286
ODB1 N 1 0,50 1,20 24 -18 42 50,48 0,80 -0,80 -0,64 -32
ODB2 - 1 0,35 1,38 24 20 4 5,50 0,90 -2,10 -1,89 -10
TRANSMISSIVE HEAT LOSSES: Qh = 1237
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 62
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 284
42 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =3,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 232
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 578
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1814
ROOM NAME: DRESSING ROOM 1
ROOM NUMBER: 16
ROOM TEMPERATURE - tp: 24
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 - 1 0,55 0,74 24 20 4 2,96 2,50 2,90 7,25 21
SZ 1 N 1 0,50 1,20 24 -18 42 50,48 2,50 3,25 8,13 410
SZ 1 E 1 0,50 1,20 24 3 21 25,24 2,90 2,10 6,09 154
PZ 3 - 1 0,20 1,91 24 20 4 7,62 1,40 3,25 4,55 35
UV - 1 - 2,30 24 20 4 9,20 0,80 2,10 1,68 15
PNT 1 - 1 0,31 2,35 24 3 21 49,30 2,50 2,90 7,25 357
ODB1 - 1 0,20 1,91 24 20 4 7,62 0,80 -2,10 -1,68 -13
TRANSMISSIVE HEAT LOSSES: Qh = 980
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 49
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 186
4 a1 =7,00 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =5,80 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 466
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 701
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1682
ROOM NAME: DRESSING ROOM 2
ROOM NUMBER: 17
ROOM TEMPERATURE - tp: 24
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 1 W 1 0,55 0,74 24 20 4 2,96 2,50 2,90 7,25 21
SZ 1 - 1 0,50 1,20 24 3 21 25,24 2,90 2,30 6,67 168
PZ 2 W 1 0,35 1,38 24 20 4 5,50 2,50 2,35 5,88 32
PZ 3 - 1 0,20 1,91 24 20 4 7,62 2,50 2,35 5,88 45
UV - 1 - 2,30 24 20 4 9,20 0,80 2,10 1,68 15
PNT 1 - 1 0,31 2,35 24 3 21 49,30 2,50 2,90 7,25 357
ODB1 - 1 0,20 1,91 24 20 4 7,62 0,80 -2,10 -1,68 -13
TRANSMISSIVE HEAT LOSSES: Qh = 627
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 17% Qpr = 107
4 a1 =7,00 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =5,80 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 466
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 573
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1200
ROOM NAME: HALL
ROOM NUMBER: 18
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 1 W 1 0,50 1,20 20 -18 38 45,67 3,50 4,25 14,88 679
PZ 3 - 1 0,20 1,91 20 24 -4 -7,62 2,90 4,25 12,33 -94
SV W 1 - 3,50 20 -18 38 133,00 0,80 2,10 1,68 223
UV - 2 - 2,30 20 24 -4 -9,20 0,70 2,10 1,47 -27
PNT 1 - 1 0,31 2,35 20 3 17 39,91 2,10 2,90 6,09 243
ODB1 - 1 0,20 1,91 20 24 -4 -7,62 1,40 -2,10 -2,94 22
TRANSMISSIVE HEAT LOSSES: Qh = 1047
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 220
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =5,80 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 380
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 600
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1647
ROOM NAME: MALE TOILET - STUDENTS
ROOM NUMBER: 19
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 3 E 1 0,30 1,53 20 -18 38 58,02 1,80 2,80 5,04 292
SV E 1 - 3,50 20 -18 38 133,00 1,40 2,10 2,94 391
PNT 3 - 1 0,30 0,68 20 3 17 11,55 1,80 6,50 11,70 135
ODB1 E 1 0,30 1,53 20 -18 38 58,02 1,40 -2,10 -2,94 -171
TRANSMISSIVE HEAT LOSSES: Qh = 648
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 123
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =9,10 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 596
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 719
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1367
ROOM NAME: MALE TOILET - TEACHERS
ROOM NUMBER: 20
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKS 2 - 1 0,27 1,38 20 22 -2 -2,76 2,75 3,95 10,86 -30
PZ 4 - 1 0,25 1,50 20 15 5 7,50 2,75 2,80 7,70 58
PNT 3 - 1 0,30 0,68 20 3 17 11,55 2,75 3,95 10,86 125
TRANSMISSIVE HEAT LOSSES: Qh = 153
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 17% Qpr = 26
0 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =0,00 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 0
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 26
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 179
ROOM NAME: FEMALE TOILET
ROOM NUMBER: 21
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 3 E 1 0,30 1,53 20 -18 38 58,02 2,00 2,80 5,60 325
PZ 4 - 1 0,25 1,50 20 15 5 7,50 3,65 2,80 10,22 77
SP E 2 - 2,90 20 -18 38 110,20 0,50 0,50 0,25 55
PNT 3 - 1 0,30 0,68 20 3 17 11,55 1,00 9,90 9,90 114
ODB1 E 1 0,30 1,53 20 -18 38 58,02 0,50 -1,00 -0,50 -29
TRANSMISSIVE HEAT LOSSES: Qh = 542
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 17% Qpr = 92
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =4,00 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 262
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 354
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 896
ROOM NAME: TOILET - HALL
ROOM NUMBER: 22
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 3 E 1 0,30 1,53 20 -18 38 58,02 2,00 2,80 5,60 325
SP E 2 - 2,90 20 -18 38 110,20 0,50 0,50 0,25 55
PNT 3 - 1 0,30 0,68 20 3 17 11,55 2,00 2,50 5,00 58
ODB1 E 1 0,30 1,53 20 -18 38 58,02 0,50 -1,00 -0,50 -29
TRANSMISSIVE HEAT LOSSES: Qh = 409
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 78
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =4,00 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 262
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 339
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 748
ROOM NAME: FEMALE TOILET - STUDENTS
ROOM NUMBER: 23
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
SZ 3 E 1 0,30 1,53 20 -18 38 58,02 1,80 2,80 5,04 292
SV E 1 - 3,50 20 -18 38 133,00 1,40 2,10 2,94 391
PNT 3 - 1 0,30 0,68 20 3 17 11,55 1,80 6,50 11,70 135
ODB1 E 1 0,30 1,53 20 -18 38 58,02 1,40 -2,10 -2,94 -171
TRANSMISSIVE HEAT LOSSES: Qh = 648
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 123
38 a1 =0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =9,10 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 596
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 719
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 1367
FIRST FLOOR
ROOM NAME: HALL
ROOM NUMBER: 1,1
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 2,20 15,70 34,54 953
SZ 2 E 1 0,35 1,59 20 -18 38 60,41 2,70 4,35 11,75 710
SP E 1 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 382
ODB1 E 1 0,35 1,59 20 -18 38 60,41 1,65 -2,10 -3,47 -209
TRANSMISSIVE HEAT LOSSES: Qh = 1835
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 349
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 799
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1147
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2982
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,2
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 6,10 9,30 56,73 1565
SZ 2 W 1 0,35 1,59 20 -18 38 60,41 6,10 4,35 26,54 1603
SZ 2 N 1 0,35 1,59 20 -18 38 60,41 9,30 4,35 40,46 2444
SP - 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
ODB1 W 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 6130
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 306
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 1410
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 4112
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 10242
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,3
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 7,00 6,90 48,30 1332
SZ 2 W 1 0,35 1,59 20 -18 38 60,41 6,90 4,35 30,02 1813
SP W 2 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 764
KOP - 1 0,55 0,79 20 -18 38 30,11 1,00 3,10 3,10 93
ODB1 W 1 0,35 1,59 20 -18 38 60,41 1,65 -4,20 -6,93 -419
TRANSMISSIVE HEAT LOSSES: Qh = 3584
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 753
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =24,40 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 1597
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 2350
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 5934
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,4
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 8,80 6,90 60,72 1675
SZ 2 W 1 0,35 1,59 20 -18 38 60,41 8,80 4,35 38,28 2313
SP W 3 - 2,90 20 -18 38 110,20 1,65 2,20 3,63 1200
KOP - 1 0,55 0,79 20 -18 38 30,11 1,00 3,10 3,10 93
ODB1 W 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 4653
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 977
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3373
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 8026
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,5
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION W
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 6,10 6,90 42,09 1161
SZ 2 W 1 0,35 1,59 20 -18 38 60,41 6,10 4,35 26,54 1603
SZ 2 S 1 0,35 1,59 20 -18 38 60,41 9,30 4,35 40,46 2444
SZ 2 E 1 0,35 1,59 20 -18 38 60,41 6,10 4,35 26,54 1603
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
ODB1 S 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 7329
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 25% Qpr = 1832
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 4228
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 11557
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,6
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 9,00 6,10 54,90 1514
SZ 2 S 1 0,35 1,59 20 -18 38 60,41 9,00 4,35 39,15 2365
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
ODB1 S 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 4397
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -220
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 923
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3099
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 7497
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,7
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 9,50 6,10 57,95 1599
SZ 2 S 1 0,35 1,59 20 -18 38 60,41 9,50 4,35 41,33 2497
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
ODB1 S 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 4613
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -231
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 969
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3134
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 7747
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,8
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 9,50 6,10 57,95 1599
SZ 2 S 1 0,35 1,59 20 -18 38 60,41 9,50 4,35 41,33 2497
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
MKS - 1 0,55 0,74 20 18 2 1,48 2,90 6,00 17,40 26
ODB1 S 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 4638
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -232
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 974
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3138
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 7776
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,9
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION S
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 9,00 6,10 54,90 1514
SZ 2 S 1 0,35 1,59 20 -18 38 60,41 9,00 4,35 39,15 2365
PZ 1 - 1 0,50 1,08 20 15 5 5,38 6,10 4,35 26,54 143
SP S 3 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 1146
ODB1 S 1 0,35 1,59 20 -18 38 60,41 1,65 -6,30 -10,40 -628
TRANSMISSIVE HEAT LOSSES: Qh = 4540
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD -5% Qss = -227
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 21% Qpr = 953
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3122
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 7662
ROOM NAME: LIBRARY
ROOM NUMBER: 1,10
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 2,90 6,10 17,69 488
SZ 2 N 1 0,35 1,59 20 -18 38 60,41 2,90 4,35 12,62 762
PZ 2 - 1 0,35 1,38 20 15 5 6,88 6,10 4,35 26,54 183
SP N 2 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 764
ODB1 N 1 0,35 1,59 20 -18 38 60,41 1,65 -4,20 -6,93 -419
TRANSMISSIVE HEAT LOSSES: Qh = 1778
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 89
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 409
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =24,40 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 1597
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 2095
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 3873
ROOM NAME: HALL
ROOM NUMBER: 1,11
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 2,90 21,80 63,22 1744
SZ 2 N 1 0,35 1,59 20 -18 38 60,41 21,80 4,35 94,83 5729
SP N 7 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 2673
ODB1 N 1 0,35 1,59 20 -18 38 60,41 1,65 -14,70 -24,26 -1465
TRANSMISSIVE HEAT LOSSES: Qh = 8681
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 434
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 31% Qpr = 2691
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =85,40 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 5590
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 8715
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 17396
ROOM NAME: STAIRS
ROOM NUMBER: 1,12
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION N
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 1 - 1 0,58 0,86 20 -12 32 27,59 9,00 2,90 26,10 720
SZ 2 N 1 0,35 1,59 20 -18 38 60,41 3,00 4,35 13,05 788
SP N 1 - 2,90 20 -18 38 110,20 1,65 2,10 3,47 382
ODB1 N 1 0,35 1,59 20 -18 38 60,41 1,65 -2,10 -3,47 -209
TRANSMISSIVE HEAT LOSSES: Qh = 1681
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 5% Qss = 84
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 19% Qpr = 319
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =12,20 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 799
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 1202
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 2883
ROOM NAME: CLASSROOM
ROOM NUMBER: 1,13
ROOM TEMPERATURE - tp: 20
ROOM ORIENTATION E
CALCULATION OF HEAT LOSS THROUGH THE BUILDING STRUCTURE - Qh
MKT 2 - 1 0,28 0,58 20 -12 32 18,70 1,00 54,08 54,08 1011
SZ 3 N 1 0,30 1,53 20 -18 38 58,02 6,50 3,60 23,40 1358
SZ 3 E 1 0,30 1,53 20 -18 38 58,02 9,15 3,60 32,94 1911
SP E 3 - 2,90 20 -18 38 110,20 1,80 1,60 2,88 952
MKS 2 - 1 - 1,38 20 18 2 2,76 2,90 6,00 17,40 48
ODB1 E 1 0,30 1,53 20 -18 38 58,02 1,80 -4,80 -8,64 -501
TRANSMISSIVE HEAT LOSSES: Qh = 4779
TEMPER. PERMEABILITY OF JOINTS ALTITUDE SIDE OF WORLD 0% Qss = 0
DIFFER. WINDOW DOOR CORRECT. DISC. OF WORK 23% Qpr = 1099
38 a1 = 0,60 a2 = 0,00 FACTOR PER. OF BUILD. CHAR. OF ROOM
LEN. OF JOIN. l1 =36,60 l2 = 0,00 = 1,00 H = 3,19 R = 0,90
HEAT LOSSES ON BLOWING (Qv): Qv = *(a1*l1+a2*l2)*R*H* t = 2396
HEAT LOSSES ADDITIONS TOTAL (Qd = Qss + Qpr): Qg = 3495
HEAT LOSSES TOTAL (Qg = Qt + Qd): Qg = 8274
NO. DESCRIPTION OF WORKS UNIT QUAN
TITY
UNIT
PRICE
TOTAL
PRICE
1.06. PRE-MEASUREMENT AND ESTIMATE
1.06.01. THERMOTECHNICS EQUIPMENT
01.06.01.01 Delivery and installation of a hotwater boiler, which uses
wood pellets for heating, made by "EKO PRODUKT" - Novi
Sad.
Q = 300 kW
tw = 90 / 70 oC
A = 2130 mm
L = 920 mm
H = 2100mm com. 1 1.780.500 1.780.500
01.06.01.02 Delivery and installation of a flexible screw conveyor for
pellets, made by "EKO PRODUKT" - Novi Sad.
Q = 70 kg/h
D = 140 mm
N = 35 min-1
L = 3000 mm
Pm = 1,10 kW com. 1
305.500 305.500
01.06.01.03 Delivery and installation of a bin for pellets, made by "EKO
PRODUKT" - Novi Sad.
Q = 60 kg/h
D = 100 mm
N = 25 min-1
L = 2700 mm
Pm = 0,8 kW com. 1 189.000 189.000
01.06.01.04 Delivery and installation of a screw conveyor for ash
transportation to ash container, made by "EKO PRODUKT" -
Novi Sad.
Q = 60 kg/h
D = 100 mm
N = 25 min-1
L = 3000 mm
Pm = 0,8 kW com. 1 210.000 210.000
01.06.01.05 Delivery and installation of ash container
V = 0,81 m3
A = 900 mm
B = 900 mm
H = 1000 mm 1 62.000 62.000
01.06.01.06 Delivery and installation of a container for pellet, made by
"EKO PRODUKT" - Novi Sad. 1
125.000
125.000
V = 1,8 m3
A = 3000 mm
B = 3000 mm
H = 3000 mm kom.
01.06.01.07 Delivery and installation of flue multi-cyclone dust collector
with electric motor driven rotary airlock valve and container
for ashes, made by "EKO PRODUKT" - Novi Sad.
com. 1 290.000 290.000
01.06.01.08 Delivery and installation of centrifugal fan of flue gases, made
by "DYNAIR" – Italy.
Q = 3500 m3/h
Pm = 2,5 kW
n = 2200 min-1
tradno, max = 300 oC
h = 0,71 com. 1 258.000 258.000
01.06.01.09 Delivery of a hand pallet truck with transport capacity 2 t.
com. 1 72.000 72.000
01.06.01.10 Delivery and installation of construction for unloading and
easy handling jumbo bags with pellets. Structural mass 1060
kg.
com.
1 327.000 327.000
01.06.01.11 Delivery and installation of steel flue pipe for chimney,
diameter 500 mm, with mineral wool insulation, thickness
50mm and protection of aluminum sheet, thickness 0,8mm.
com. 1 15.000 15.000
01.06.01.12 Delivery and installation of black seamless pipes according to
DIN 2448.
DN 10 - Ø 16,0x1,8 m
DN 20 - Ø 25,0x2,8 m
DN 80 - Ø 88,9x3,8 m
DN150 - Ø 159,0x4,5 m
DN200 - Ø 219,1x5,9 m
24
30
35
1
1
190
340
1.400
4.120
6.515
4.560
10.200
49.000
4.120
6.515
01.06.01.13 For connecting and sealing material, Hamburg bows, two-
piece pipe clamps, hangers for pipes, metal rosettes, wall
bushings, cement, plaster and other materials needed for
pipeline installation takes 50% of the value of the number 09
in this report.
50%
53.007,5 53.007,5
01.06.01.14 Construction and installation vessel for ventilation installations.
Ø 159,0 x 4,5 / 150,0 com. 8 3.000 24.000
01.06.01.15 Construction and installation of steel collectors made of steel
pipes with the required number of connections:
Split collector: Ø 219,1 x 5,9 / 1600 mm
DN 80 - Connection for boiler pipeline
DN 20 - Connection for sanitary water boiler
DN 80 - Connection for pipeline
DN150 - Side connection for a quick connection
DN 10 - Head-on connection for pressure gauge
DN 20 - Bottom connection for drainage
com. 1 38.250 38.250
01.06.01.16 Split collector: Ø 219,1 x 5,9 / 1600 mm
DN 80 - Connection for boiler return pipeline
DN 20 - Connection for sanitary water boiler (return line)
DN 80 - Connection for pipeline (return line)
DN150 - Side connection for a quick connection
DN 10 - Head-on connection for pressure gauge
DN 20 - Bottom connection for drainage
DN 20 - Bottom connection for water inlet
com.
1 38.250 38.250
01.06.01.17 Delivery and installation of ball valves for NP6, with threaded
connections.
DN 10 com.
DN 20 com.
8
16
440
1.320
3.520
21.120
01.06.01.18 Delivery and installation of ball valves for NP6, with flanges
and counter flanges.
DN 80 com. 11 8.000 88.000
01.06.01.19 Delivery and installation of dirt separators for NP6, with with
threaded connections
DN 20 com. 2 1.150 2.300
01.06.01.20 Delivery and installation of dirt separators for NP6, with
flanges and counter flanges.
DN 80 kom. 4 3.120 12.480
Delivery and installation of three-way valves with electric
motor, made by “AUTER” – Beograd.
01.06.01.21 RV3-50/40/AVC.24
DP = 5600 Pa
Qv = 9,15 m3/h
Kvs = 40,00 m3/h com 1 106.000 106.000
01.06.01.22 Delivery and installation microprocessor controller for
keeping the temperature constant, depending on external
temperature, made by “AUTER” – Beograd
type AMR/202RG com. 1 37.000 37.000
01.06.01.23 Delivery and installation temperature sensor for liquid, made
by “AUTER” – Beograd
Type TSW 01 com. 1 5.700 5.700
01.06.01.24 Delivery and installation temperature sensor for external
influences, made by “AUTER” – Beograd
Type TSS 01 com. 1 4.900 4.900
01.06.01.25 Delivery and installation of unit for manual/automatic control
of regulation valve, made by “AUTER” – Beograd
Type RDV 2 com. 1 35.000 35.000
01.06.01.26 Assembly of automation elements, clamping and
commissioning without the supply and installation of
electrical cables 15.000 15.000
01.06.01.27 Delivery and installation of pipe thermostat for sanitary
water, made by “AUTER” – Beograd
Type AT1W com. 1 12.500 12.500
01.06.01.28 Delivery and installation of electric-command locker for
complete boiler room control. com. 1 48.000 48.000
01.06.01.29 Delivery and installation of pressure regulators with threaded
connectors
DN 20 com. 1 2.000 2.000
01.06.01.30 Delivery and installation of a thermometer, made by "FAR" -
Italy.
Measuring range: 0 - 130°C com. 7 350 2.450
01.06.01.31 Delivery and installation of a pressure gauge, made by "FAR"
– Italy.
Measuring range: 0 - 10 bar com. 2 440 880
01.06.01.32 Delivery and installation of closed expansion vessels, made by
"INFLEKS" - Beograd.
Tip F - 400
Vk = 150 l
H = 1570 mm
D = 600 mm
Hs = 1,50 bar com. 1 35.000 35.000
01.06.01.33 Delivery and installation of safety valves with spring
DN 40 com. 1 33.000 33.000
01.06.01.34 Delivery and installation of circulation pumps, made by
"WILO" – Germany
Type TOP-S 65/13, speed 3, trofazna
Gh = 9,63 m3/h
H = 82.767 Pa
nmin = 3 - 2250 min-1
Nmax = 1449 W
U = 3 x 400 V / 50 Hz com. 1
147.000
147.000
01.06.01.35 Type Star RS-15/2, speed 3, monofazna
Gh = 0,557 m3/h
H = 6903 Pa
nmin = 3 - 1450 min-1
N = 45 W
U = 1 x 230 V / 50 Hz
1 9.300 9.300
01.06.01.36 Type Star RS-15/4, speed 3, monofazna
Gh = 0,475 m3/h
H = 18044 Pa
nmin = 3 - 2350 min-1
N = 48 W
U = 1 x 230 V / 50 Hz 1 18.150 18.150
01.06.01.37 Type TOP-S 50/4, speed 3, trofazna
Gh = 14,50 m3/h
H = 10003 Pa
nmin = 3 - 1700 min-1
N = 330 W
U = 3 x 400 V / 50 Hz kom. 1
85.720
85.720
01.06.01.38 Delivery and installation of magnetic flow water softeners
whose maximum temperature is tw = 40 oC. Representative
and importer is "FEROMAX" – Belgrade
Type AQUA UNIQUE A4 50-385 HW
DN20 com. 1 120.000 120.000
01.06.01.39 Construction and installation of mechanical impurities filter
installed along with magnetic water softener. Representative and importer is "FEROMAX" – Beograde
Type AU 50 MPS
DN20 com. 1 25.000 25.000
01.06.01.40 Construction and installation of boiler for sanitary water, with all necessary connections and following characteristics:
V = 300 l
Q = 11,79 kW
tw = 90 / 70 oC
tw san = 50 / 16 oC
Fizm = 0,50 m2 com.
1 115.000 115.000
01.06.01.41 Cleaning of the pipes, double coating of red lead, construction
of thermo-insulating layer, type PLAMAFLEX or similar,
thickness d = 30 mm
DN 20 kom.
DN 80 kom.
DN150 kom.
DN200 kom.
123
35
1
4
100
1.050
3.000
5.000
12.326
36.782
3.000
20.000
01.06.01.42 Delivery of dry powder fire extinguishers
Type S - 9 com. 1 6.000 6.000
01.06.01.43 Delivery of barrel with sand, a shovel and a pick.
complet 1 5.000 5.000
01.06.01.44 For manipulative expenses, like costs of examining the
installation for cold water pressure, costs of hot testing, costs
of regulating the installation and costs of other preparation-
finishing works, it is calculated at 5% of all stated value
5% 2.082.330 104.116
TOTAL: 5.136.820
01.06.02. EQUIPMENT AND INSTALLATION WORKS FOR INTERNAL HEATING
INSTALLATIONS
01.06.02.01 Delivery and installation of steel panel radiators, made by
„Jugoterm“ Gnjilane:
900 × 400 com.
900 × 600 com.
900 × 800 com.
900 × 1000 com.
900 × 1200 com.
900 × 1400 com.
4
6
27
23
8
3
4.080
6.144
7.630
10.041
10.980
12.540
16.320
36.864
206.031
230.956
87.840
37.620
01.06.02.02 Delivery and installation of radiator lockshield valves, made
by „Celefi“ Italy.
com. 71 336,2 23.870
01.06.02.03 Delivery and installation of thermostatic valves, made by
„Danfos“
com. 71 950 67.450
01.06.02.04 Delivery and installation of equipment to carry panel radiators
(set):
com. 142 169 24.000
01.06.02.05 Manual shut-off valve with flange and counter flange:
DN 80 com. 2 34.498 68.996
01.06.02.06 Delivery and installation of air vents:
DN 15 10 463,8 4.638
01.06.02.07
Delivery and installation of steel welded pipes according to
standard SRPRS C.D5.221 for pipeline installation of central
heating:
DN 15 Ø 21,3 × 2,0 (m)
DN 20 Ø 26,9 × 2,3 (m)
DN 25 Ø 33,7 × 2,6 (m)
DN 32 Ø 42,4 × 2,6 (m)
DN 40 Ø 48,3 × 2,6 (m)
318
96
60
84
42
101,8
149,5
213,1
272,5
312,8
32.369,45
14.352,49
12.787,46
22.890,19
13.137,36
01.06.03. HOT WATER PIPELINE
01.06.03.01 Delivery and installation of pre-insulated pipes, made by
"TERMIZO" - Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
52
83
4.836
1.591,2
251.472
131.098
01.06.03.02 Delivery and installation of pre-insulated pipe bows, made by
"TERMIZO" - Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
8
10
8.029,05
2.885,64
64.232,44
28.856,41
01.06.03.03 Delivery and installation of pre-insulated pipe joints, made by
"TERMIZO" - Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
16
20
4.266,60
2.586,48
68.256,60
51.279,60
01.06.03.04 Delivery and installation of elements for implementing pre-
insulated pipeline through the walls, made by "TERMIZO" -
Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
4
4
3.307,20
1.817,40
13.228,80
7.269,60
01.06.03.05 Delivery and installation of end caps for the transition from
polyurethane to the insulating layer of PLAMAFLEX, made
by "TERMIZO" - Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
4
4
4.243,59
2.411,09
16.974,36
9.644,36
01.06.03.06 Delivery and installation of pre-insulated pipe fixed supports,
made by "TERMIZO" - Novi Sad.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
4
4
11.763,41
4.196,13
47.053,66
16.784,54
DN 50 Ø 60,3 × 2,9 (m)
DN 60 Ø 76,1 × 2,9 (m)
132
60
439,0
559,8
57.944,37
33.590,94
01.06.02.08 For connecting and sealing material, knees and elbows,
oxygen and disugas, clamps for pipes and other supporting
materials necessary for the proper execution of the
installation, taking 50% of the value of the number 07 in this
report.
(50%) - - 56.121,68
01.06.02.09 Drilling holes and breaks through the walls and floor
construction:
- - 30.000
TOTAL: 1.077.780,33
01.06.03.07 Third category soil digging for laying the hot water pipeline
and waste disposal.
(m3) 9 5.500 49.500
01.06.03.08 Making the sand at the bottom of the channel and around pre-
insulated pipeline, layer thickness above pipeline b=20 cm.
(m3) 7 4.100 28.700
01.06.03.09 Backfilling excavated soil over the buried sand and alignment
with the field.
(m3) 8 3.500 28.000
01.06.03.10 Removal of surplus excavated soil to the landfill.
(m3) - 24.500 24.500
01.06.03.11 Fabrication and installation of vessels for installation venting.
ϕ 88,9 × 3,2 (com.)
ϕ 30,0 × 2,6 (com.)
4
4
2.800
1.800
11.200
7.200
01.06.03.12 Drilling walls and floor trusses for the passage of pipe lines
without closing.
DN 80 – ϕ 88,9 × 3,2 (m)
DN 25 – ϕ 30,0 × 2,6 (m)
4
4
1.100
800
4.400
2.400
01.06.03.13 For handling costs, such as installation testing costs on a cold
pressurized water, hot rehearsal costs and other costs of
preparator- final works, taking 3% of value of all listed
shares.
(3%) - - 21.198,31
TOTAL: 926.508,64
01.06.04. CONSTRUCTION OF A BOILER ROOM BUILDING
01.06.04.01 Construction of a prefabricated building with steel supporting
construction, mass 27 kg/m2, plated with thermo-insulating
panels, thickness d=60 mm, with a single entrance door and
and two outer windows. There is a control room and a toilet
facility in the installation. The floor of the boiler room is made
of concrete with industrial coating as a finishing layer. 1 1.583.600
1.583.600
PROJECT DOCUMENTATION (5%) 413.185
R E C A P I T U L A T I O N :
01.06.01. THERMOTECHNICS EQUIPMENT 5.136.820
01.06.02. EQUIPMENT AND INSTALLATION WORKS FOR INTERNAL HEATING
INSTALLATIONS 1.077.780
01.06.03. HOT WATER PIPELINE 926.509
01.06.04. CONSTRUCTION OF A BOILER ROOM BUILDING 1.583.600
01.06.05. PROJECT DOCUMENTATION (5%) 413.185
TOTAL: 9.137.894