best energy practices implementation in seshasayee paper
TRANSCRIPT
1
Best Energy Practices Implementation in
Seshasayee Paper
Knowledge Exchange Platform Workshop
Bureau of Energy Efficiency &
Institute of Industrial Productivity
New Delhi
26th Feb 2015
Dr T.G.Sundara Raman,SPB
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Paper Industry- Emission Mitigation Strategies
• Improving Energy efficiency of the Process
• Energy Conservation
• Cleaner fuels Usage for energy generation
• Efficient high pressure cogeneration with increased cycle efficiency
• In house Biomass generated by the process [BLS,wood dust, bagasse pith etc.] usage
• Conversion of waste (solid, liquid /gaseous) to energy
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SPB: CPP Unit Process Flow
E2
C
BOILER
PSH SSH
ECO
E1
To
Process
To Process
& Deaerator
CT
OUT
IN
CW
0.1 ata
12
ata 5 ata
Steam
SJE/GSC FST
Spray
Deaerator
LP Steam
STG ~G
5
Power Enhancement Concept- First of its kind
• Automation Control Scheme Implemented & in
successful operation ensuring high degree of exhaust
condensing steam wetness related to increased
Power generation; alongside maintaining high degree
of condenser vacuum in 21 MW Extraction
Condensing STG of Captive Power Plant.
7
21 MW CPP-Power Enhancement Scheme–Summary
Section Parameter Impact Result Outcome
Condenser
–Cooling
Water
Circuit
CW Flow
increase
CW outlet temp.
drops increasing
LMTD & possible
lowering of exhaust
Steam temp.
Lowered CW exit
temperature;
Heat transfer
coefficient
increases due to
increased CW
velocity
Minor increase
in condenser
vacuum
Exhaust
Steam
wetness
Highly
desirable
[restricted
to < 15%]
Steam Enthalpy
differential increases
Enhanced Power
Generation through
increased cycle
efficiency
Power increase
: 0.3 to 0.4 MW
[inclusive of
above factor]
Condenser
Vacuum-
High
Advantage-
ous
Ensures higher
steam energy
exchange through
higher DP available
Power
enhancement
marginal
-
Generator PF >0.95
desirable
Generator efficiency
increases
Marginal increase in
Power generation
0.05 -0.1 MW
High
operating
load
Generator efficiency
increases
Increase in Power
generation
-
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Total
Energy
Flow
Heat Release
ISPB : D-E-B / 900
Heat Release Computation
DRUM
PRESSURE
Heat Release is used as measured variable for master
fuel control algorithm
d /dt
Advantages of Heat Release:
• Independent of Fuel measurement system
• Totalizes fuel from all sources internally
• Monitors Change in Fuel quality
Innovative Project –High Pressure AFBC Boiler
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Advances in Instrumentation & Control Automation
• Integrated Direct Energy Balance Automation
Concept in HP Cogen Plant (First of its kind )
• Power consumption reduction : 0.15 MW
• Boiler Steam Pressure Swings minimized ensuring
higher power output.
• Load Sharing Control Scheme with both Cogen
units
• With VFD - ID & PA Fans in place, Power savings
are doubled
10
Boiler #10- LOI redn. in flyash
P.A. pressure reduced from 1400 to 1200 mmWC
• LOI in Flyash reduced from 12% to 6%
• Combustion η increased by : 0.5 to 0.6 %
• Coal saving : 60 to 70 te/month
• GHGE reduction:900 to 1100 tCO2/yr
• Easy disposal of flyash to Cement mill
Waste to Energy Conversion
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Optimization of Operation of Coal fired
Cogeneration Battery
• For deriving maximum mileage from
the high cycle efficiency of CPP , it
had been decided to run the 3 MW
STG sparingly and limit steam
generation to the extent practicable in
the low pressure coal fired boilers.
The shortfall in power requirement had
been made up by grid power import.
• The above scheme coupled with the
high efficient operation of CPP unit,
avoidance of HP steam through
PRDS ( 105 bar) and implementation
of innovative Energy Management
schemes had resulted in significant
specific coal consumption reduction .
1.431.31
1.14
0
0.4
0.8
1.2
1.6
2
2011-12 2012-13 2013-14
Spec.C
oal C
onsn.[
t/t]
13
E2
E1 E1
E2
BLR#10 VHP BLR#11
HP
P2 P1
21 MW
DEC
16 MW
EBP
LP LP
MP
Steam & Power Optimisation with 2 HP Cogen online
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Innovation related to LCE
Maximizing Green Power generation in Recovery Cogeneration Unit through:
• Minimal/No extraction & maximizing Exhaust
LP flow in 16 MW STG
• Maximizing steam inlet temperature through
operating the Recovery Boiler at high SOT &
effecting reduction in steam temperature loss
through highly effective advanced state of
the art insulation of MSL on-line
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Advanced Boiler Main steam
pipeline reinsulation- online ------------------------------------------------------------------------------
Replacing existing insulation with
fresh insulation mattress of higher
thk [210mm] & density [140kg/m3]-
with new cladding pin design
Steam temperature drop redn. from
10/12°C to 5/6 °C.
Radn & convecn heat loss redn.
Enthalpy gain in 16MW STG:
3kcal/kg
Addl. Power genern : 0.3 MW
GHGE Reduction : 2400 tCO2/ yr
Waste to Power
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E1[MP]steam redn:From 8TPH to <1TPH
• Power gen. increase …….…. : 0.4 MW
• Addl. power gen. through
increase in flow of E2 ........... : 0.05 MW
• Addl Green power gen……. : 0.45 MW
• REC ……………… : 300 units/month
• GHGE reduction ……..: 1800 tCO2/yr
16 MW STG : Energy Management Maximizing E2 steam with E1 minimal-
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# Increased BLS firing to over 700 TPD
# Optimization of Combustion air flow
•Increased HP Steam gen. …..………: > 90 TPH
•Increased Green power gen. …..: 10.5-11 MW
•Green steam to process ……..... : 33 to 36 TPH
•GHGE reduction increase: 20,000-25,000 tCO2/yr
•REC ………………… : Over 6000 units /month
Recovery Cogen - Green Energy Management
18 18
Green Power Generation from 16 MW STG integrated
to Recovery Boiler –since inception
6.36.9
7.98.3
9.05 9.39.8
0
2
4
6
8
10
12
2008-
09
2009-
10
2010-
11
2011-
12
2012-
13
2013-
14
Apr-
Dec
2014
Gre
en
Po
we
r [M
W]
19 19
Green Steam to Process
2930
36
25
30
35
40
Jan-Dec 12 Jan-Dec'13 Jan'14 -Dec '14
Steam to Process [tph]
Ste
am
- t
ph
21
Boiler
Steam
Rate
TPH
Efficiency
(Energy
Efficient)%
Efficiency
(Standard
oper. )%
Net Power
Savings%
Daily
Power
Savings
in Units
10 85 70 47 50 5000
11 90 70 50 40 3000
Energy Efficient Pumps – Coal fired & Recovery Boilers
Innovative Project
Power Management - BFP
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Advanced Energy Conservation Scheme BFP for H.P. Steam Generator
Efficiency [%] of BFP in Operation
40
50
60
70
80
70 84 98 112 126 140
LargeBFP EFBFP
Feed Water Flow to Boiler 10 [ TPH]
BF
P E
ffic
iency [
%]
DP across EFBFP Control valves –Boiler 10
0
10
20
30
40
70 82 94 106 117
CV original CV LowDP
Feed Water Flow to Boiler 10 [ TPH]
DP
across B
FP
CV
[b
ar]
Energy Saving : 1000 units/day
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.
ACF MB
ST
FWT
Process Hot /
Condensate Tank
Filter
Polished
Condensate
To Deaerators
PHEs Hot
Fluid
Process Condensate : 90°C to 35°C
DM Water Preheating : from 32°C
Heat Recovery : 4 MWt
CPU+ HRU - Integrated Water &
Energy Management - Boilers
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0.827
0.767
0.681
0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
2011-12 2012-13 2013-14
PAT-Specific Energy Consumption Reduction S
pec
.En
erg
y C
on
su
mp
tio
n [
MT
OE
/t p
rod
uct]
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2.532.73
3.11
0
0.5
1
1.5
2
2.5
3
3.5
2011-12 2012-13 2013-14
GHG Emission Reduction [GtoG] S
pec.C
O2 E
mis
sio
n [
tCO
2/t
pro
du
ct]
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Non Energy Benefits - New Concept [ACEEE]
• SPM in Stack gas : < 50 mg/Nm3
• Water conservation through CPU - PHE in CPP
• Nansulate coating in Dryer section – Scanner
• Water conservation through lowered Dryness
Fraction in 21 MW STG condensation steam
exhaust
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CSR -Social Promotion of GreenCo in SPB
• Treated RO water for Drinking purposes
• Waste Water for Irrigation -Cane
• Green Initiatives Awareness for School students –
Formation of Green Club in SPB High school
• Encouraging Engng College students to do Industrial
projects related to Green Initiatives
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Initiated & On-Going Green Initiatives
• Tree Farming – High Carbon Sequestration at Source
• Landscape –Greening
• Solar Heating system for Hot water for Canteen
• Green Initiative –Solar Lightpipe in Finishing House of
Paper Machine
• In-Plant Training related to GreenCo Initiatives
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Innovative Energy Conservation Schemes
Implemented-Summary Unit Activity SPB to Beneficiaries
Cogeneration Power
Plants
Direct Energy Balance-400 for
marginal increase in Power
generation
Metso Automation
Captive Power Plant Power increase through Exhaust
steam Dryness fraction maintenance
through control automation scheme
All Thermal &
Industrial Power
Plants
HP Cogeneration
Battery
MP to LP steam switch for
maximizing Power generation-STG
All Back pressure
Cogeneration units
HRU -CPU Heat recovery & DM water
conservation
Process Industries
Nansulate - Drying cylinder
ends & Scanner Steam reduction ; scanner made
operational
Nanotech. USA
Energy efficient BFP
integrated with CV
Station Power consumption reduction All Boiler Feed water
Pumps
Advanced thermal
insulation of Main steam
pipeline
Increased Green Power generation All STGs world over