dr. sanjay v. patil head and technical adviser …. sv.patiil.pdf · email:...
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AIDA Technical Seminar www.vsisugar.com Bengaluru, 05-06-Oct-2017
DR. SANJAY V. PATIL
HEAD AND TECHNICAL ADVISER
DEPARTMENT OF ALCOHOL TECHNOLOGY
VASANTDADA SUGAR INSTITUTE, MANJARI, PUNE (INDIA)
Email: [email protected]
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Types of assessments
Norms – SW Treatment/Disposal
Approved ZLD systems
Approach
Fermentation and Distillation
Effluent quantities and Characteristics
Biomethanation
Reverse osmosis
Multiple effect Evaporation
Biocomposting
Slop fired Incineration boiler
BMSW dryer
Condensate Polishing unit
On-line monitoring system and other requirements
Conclusions
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Self Assessment
Third Party Assessment-VSI/NEERI/Distillers’ Association etc
Assessment by regulatory authority-SPCB/CPCB/MoEF
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1. Red category and Zero Liquid Discharge (ZLD).
2. For Bio-composting as a final treatment:
MEE is essential
SW storage max. 30 days on raw SW basis.
Max. 270 days (With covered compost yard-
additional/throught-out the year can be allowed)
Yard has to be impervious as per CREP norms.
Bio-compost has to be bagged in polybags &
compost composition & manufacturers name to be
printed on it.
Compost quality has to be certified by Ministry of
Agriculture.
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2. For Bio-composting as a final treatment (Continued):
For 5 to 12 % solids containing spent wash, the filler
material (PMC) to spent wash ratio prescribed is 1:
2.5 for 45 days cycle and 1:3.5 for 60 days cycle.
For concentrated spent wash (20 to 30 % solids), the
filler material (PMC) to spent wash ratio prescribed is
1: 1.6 for 60 days cycle.
Impervious compost yard area based on material
balance (plus ready compost storage area) should
be made available.
During rainy season, bio-composting process has to
be stopped.
Record of filler material used (PMC) and bio-
compost produced/sold should be maintained.
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3. SW storage- Impervious as per CREP norms.
4. For Incineration route: Storage of 7 days on conc. SW
basis in impervious storage tank.
5. Secondary treatment: Process condensate, permeate,
spent lees, CT & boiler Blowdown, pump gland cooling
water etc. has to be treated (CPU) & recycled back.
6. Online monitoring :
Mass flowmeters before & after concentration of
SW.
Camera: 30 days SW storage tank & bio-compost
yard.
Stack Monitoring System (PM <150 mg/NM3 or 50
mg/NM3).
To be installed & connected to SPCB/CPCB server.
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Biomethanation MEE Bio-composting
Biomethanation RO MEE Bio-composting
Biomethanation MEE DRYER
Biomethanation RO MEE
MEE Incineration
1
2
3
4
5
DRYER
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1. Holistic Approach: Integrated management
employing Reduce-Recycle-Reuse principle
2. No End of Pipe Treatment.
3. No Discharge
4. Analytical & Necessary measurement facilities
(Water, Steam, Power, Effluents)
5. Fresh water consumption-section wise
6. Environment Management Cell:
(Unit Head + Distillery Manager + ET plant I/c
+ Concerned Officers/Chemists)
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Distillery installed and Licensed capacity. Boiler
capacity. Source of electricity and water.
Distance from river/dam/canal/other water bodies.
Authentic data on alcohol production/molasses
consumed. Per day alcohol production data.
Authentic data on per day SW & SL production, total SW
& SL production.
No. of days of operation in a year.
Alcohol % (v/v) achieved in wash, Fermentations
efficiency, Distillation efficiency, Recovery etc.
Fermentation technology employed.
Distillation technology employed, reboilers used, spent
lees generation (Rectifier, PRC etc).
If sludge is generated, quantity of sludge MT/day & its
method of disposal.
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RAW
SPENT WASH
VALUES
Volume, M3/Day
Volume, L/L
pH
COD, mg/L
BOD, mg/L
TDS, mg/L
TSS, mg/L
Volatile acids,
mg/L
SPENT LEES VALUES
Total SL, M3/Day
Volume, L/L
SL Recycled,
M3/Day
SL for treatment
M3/Day
pH
COD, mg/L
BOD, mg/L
TDS, mg/L
TSS, mg/L
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Setting cum cooling tank capacity = M3 (if any)
Setting cum cooling tank RT = days
Digester design basis= Hydraulic Retention Time = ----days(15-24 days)
= Organic Loading Rate = ------- kg/M3 /Day
= Volume = ----- M3
Type of Technology = CSTR/UASB/ Thermophilic/ Hybrid
Biomethanation Plant Performance (based on 1 month data)Parameters Minimum Performance parameters Actual Values
Feed rate, M3 /Day
0Brix, (Inlet/Outlet)
pH, (Inlet/Outlet)
COD, mg/L (Inlet/Outlet)
BOD, mg/L (Inlet/Outlet)
COD reduction % 60
BOD reduction % 85
Biogas generation, NM3 /Kg of COD
consumed0.5
Biogas generation, M3 /Day -
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No. of days of operation of digesters (days/annum).
Restabilization method and period required.
How digester is maintained during ideal days?
Year of establishment of digester.
How temp of digester is maintained?
Total biogas generated (M3/annum) and baggase/coal
saved.
Whether digester has been revamped? If yes, how
many times & for what purpose?
Sludge generation from digester and how the sludge is
disposed off?
Log Book records supporting biogas plant performance.
Present Bottle-necks/problems
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Particulars Raw spent wash (Feed)
Treated effluent (Outlet)
Quantity, M3/day
Colour
PH
Temperature, degree C
Conductivity, ms
BOD, ppm
COD, ppm
Total solids, %
Total dissolved solids, %
Total suspended solids, %
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Setting tank capacity before RO = M3 (if any)
Year of installation/establishment & commissioning of
RO plant
Type of technology of membrane filtration.
Number of membranes per module & number of
modules.
Designed feed capacity of R.O. (M3/day).
Acceptable level of suspended solids, dissolved
solids & other membrane affecting components in
the feed.
No of days of operations.
Log Book supporting RO plant performance.
Further treatment/disposal of Permeate/Reject
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Particulars Inlet (Feed)
Reject Permeate Rinsing
back
wash
Chem
Cleaning
Quantity, M3/day
Recovery, %
Colour
pH
Conductivity, ms
BOD, ppm
COD, ppm
Total solids, %
Total dissolved
solids, %
Total suspended
solids, %
Based on at least 1 month data
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Setting tank capacity before MEE = M3 (if any)
Year of installation/establishment & commissioning of
MEE plant
Type of technology of MEE.
Number of Effects with their HTA and MOC. Number of
stand-by bodies and degasser provided.
Designed feed capacity and evaporation duty of MEE
(M3/day).
Acceptable level of suspended solids, dissolved solids
etc in the feed.
No of days of operations.
What is the frequency and duration of cleaning. Log Book supporting MEE plant performance.
Further treatment/disposal of Condensate/Concentrate
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Particulars Unit Values
Feed rate @ Sp. Gr. (Approximate) Kg/hr
Solid content in feed/brix %/ degree
Water evaporation rate (Minimum) Kg/hr
Concentrate output Kg/hr
Solid content in concentrate/brix %/degree
Steam required for water evaporation Kg/hr
Cooling water circulation rate M3/hr
Power consumption for Evaporation KWH
Feed temperature 0C
Steam pressure / temperature Kg/cm2 /0C
Steam Economy, (Kg water /kg steam) Kg
Operation hour Hr / day- or week or month
Frequency of CIP Hr/ day or week or month
Quantity of CIP effluent M3/hr
Quantity of process condensate M3/hr
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Particulars Conc. spent wash
Process Condensate
Quantity, M3/day
Colour
PH
Temperature, degree C
BOD, ppm
COD, ppm
Total solids, %
Total dissolved solids, %
Total suspended solids, %
Ammonical Nitrogen (as N), ppm NA 270
Based on at least 1 month data
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30 days holding tank capacity with dimensions and
construction details.
Biocompost yard details- Impervious biocompost yard
(PCC- 1:3:6 or RCC- 1:2:4 or brick on edge) with
construction details.
Area of impervious biocompost yard (uncovered and
covered) with biocompost storage area.
Number & type of turning & mixing machine.
Number of Bore well around compost yard.
Number of Pizometers around the compost.
Spentwash available for biocomposting (M3/Annum)
and spentwash characteristics.
Log Book supporting biocompost plant operations.
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Biocompost filler material availability (Press mud/Yeast
sludge/Boiler ash) (MT/day or MT/annum).
Record of Press mud produced or purchased from out
side.
Average Press mud to spentwash mixing ratio.
Windrows size (Length x width x height)
Biocompost cycle (45 days or 60 days) and number of
cycle per annum.
Biocompost analysis report.
Material balance for biocompost.
Record of biocompost produced and sold with selling
price of biocompost (Rs./MT).
Biocompost sold in loose or bag packing.
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Date of installation
Design basis : Slop and subsidiary fuel ratio, calorific values
and feed rates considered to finalise capacity and other
details
Boiler/Technology Supplier details and type of boiler
Boiler capacity, pressure, temperature and other details
Boiler performance details: Including slop and subsidiary fuel
actual ratio achieved, no of working days, shut down days-
cleaning period required, steam generation (MT/hr), steam
pressure & temperature etc.
Emission control system installed, its details, analysis report.
Problems faced in operation and maintenance of Boiler.
Quantity of ash generated (MT/day), its characteristics and
method of disposal etc.
Log Book records supporting incineration boiler performance.
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Date of installation.
Design basis : BMSW feed rates considered to finalise
capacity and other details.
Dryer/Technology Supplier details and type of dryer.
Dryer capacity and other details.
Dryer performance details: Including BMSW feed rate,
steam/biogas used/hr, no of working days, shut down days-
cleaning period required, powder produced (MT/hr) and
other details.
Emission control system installed and its details.
Problems faced in operation and maintenance of dryer.
Characteristics of powder produced and storage method.
Quantity of condensate generated (M3/day), its
characteristics and method of treatment/disposal etc.
Log Book records supporting dryer performance.
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Date of installation of CPU unit.
Name of plant/technology supplier.
Type of technology of CPU plant: Conventional /RO/
Striper / Photo-oxidation /In house technology etc).
Design capacity of CPU unit (M3/day) and feed
characteristics considered.
Low strength effluents treated though CPU & their
quantities (Process condensate, permeate, spent lees,
etc).
Recovery (%) and characteristics of treated water and
its further utilization details.
Is there any reject generated and how it is disposed?
Total fresh water consumption after reuse of treated low
strength effluents. Log Book records supporting CPU performance.
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Particulars Mixed Influent Treated effluent
Quantity, M3/day
Colour
PH
Temperature, degree C
BOD, ppm
COD, ppm
Total solids, %
Total dissolved solids, %
Total suspended solids, %
Volatile acids
Total Alkalinity
Based on at least 1 month data
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Number and location of mass flow meters installed (minimum
two) with photographs.
Number and location of cameras installed (minimum two)
with photographs.
Details of on-line emission (stack) monitoring system for
boiler.
Date on which the online monitoring system was
commissioned/connected to the server.
Name and contact details of the vendor who has supplied
and commissioned the on-line monitoring system.
Problems faced in maintaining the continuity of on-line
monitoring system.
Green belt surrounding biocompost yard (Photographs).
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Identification of recipient drains/ rivulets and their u/s &
d/s locations for monthly monitoring to ensure ZLD.
Material and mass balance of your total distillery plant
operations including ETPs showing ZLD.
Also indicate how your distillery unit is achieving steam
and power balance.
Environment Management Cell- MoMs and necessary
documents.
EC, Consent to Operate, Directions received and
related documents.
Water conservation measures taken report (rain water
harvesting etc).
Prepare your own action plan for achieving ZLD.
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Preparing self assessment report is first step towards
compliance to ZLD norms.
It indicates your concern to save the environment.
It will definitely help you to identify bottle-necks and
further improve your performance.
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