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| Common
Effluent Treatment Plants |
CETP at Vatva, Ahmedabad
Name of Project :
The Green Environment Co-op. Soc. Ltd.,
Plot No.244 to 251, Phase-II
GIDC Estate, Vatva, Ahmedabad-382445
Phone: 079-5892283, 5832449
Fax : 079-5893614
No. of Contributing Members : 437
Area of CETP Site : 20,000 sq.mt.
Designed Capacity of CETP : 16,000 m3/d
Present Flow being Recd. : 10,000 m3/d
Cost of Project :
About Rs.300 million(including cost of conveyance,
treatment and disposal)
Commencement of CETP : April,1998
Treatment Units :
Equalization tank 1 no
Panic/surge tank for excessive shockload 1 no.
Flash mixer 1 no.
Floccualater 1 no.
Dissolved air floataation unit 1 no.
Combined aeration tank/clarifier Unit
with diffused aeration tank 1 no
Plate & frame type filter press for dewatering of sludge 3 nos.
Other
details
CETP at Odhav, Ahmedabad
Name of the Project :
Odhav Enviro Projects Limited
Plot No.25, GIDC Estate , Odhav, Ahmedabad-382415
Phone : 079-2891277
No. of Contributing Members : 57
Area of CETP Site : 6,015 sq.mt.
Designed Capacity of CETP : 1,200 m3/d
Present Flow being Recd. : 720 m3/d
Cost of the Project : Rs. 41.5 million (including cost of conveyance, treatment and disposal)
Commencement of CETP : January,1998
Treatment Units :
Collection sump 2 no.
Equalization tank 1 no.
Flash mixer
Calrifloculater
First stagte aaeration tank
First stage secondary clarifier
Second stage aeration tank
Second stage secondary clarifier
Intermediate storage tanak
Pressure sandfilter
Cetrated curbon colour
Plated frame type filter press for watering of primary stage
Sludge drying beds for secondary sludge.
Other details :
CETP at Vapi, dist : Valsad, Gujarat
Name of the Project :
Vapi Water & Effluent Management Co. Ltd.
Plot No.135, VIA House GIDC Estate, VAPI
Dist : Valsad - 396 195
Phone : 02638 – 29950 ; Telefax : 02638 - 30950
No. of Contributing Members : 1800
Area of CETP Site : 2,86,655 sq.m.
Designed Capacity of CETP : 55,000 m3/d, further expansion is possible upto 90,000 m3/d
Cost of Project :
Rs.204 million (does not include cost conveyance and disposal)
40 % initially contributed by the industries, remaining amount to
be paid in 32 quarterly installments with interest
Commissioning of CETP : January 1997
Treatment units :
a Screen chamber 1 no. g. Aeration tank 2 nos
b. Grit chamber 2 nos h. Secondary settling tank 2 nos.
c. Equalisation tank 1 no. i. Return sludge pumping stn. 1 no.
d. Equalisation pumping stn. 1 no. j. Sludge thickener 2 nos.
e. Primary settling tank 2 nos k. Thickened sludge pumping stn. 1 no.
f. Primary sludge pumping stn. 1 no l. Sludge drying beds
Effluent characteristics ( as on March 2000)
| Sample specification | pH | SS | TDS | BOD | COD | CL- | S2- | Phenol |
| Raw effluent after equalisation | 7.5 | 510 | 88190 | 792 | 2202 | 2763 | - | 1.85 |
| Final treated effluent | 7.3 | 40 | 6020 | 41 | 601 | 3516.2 | 1.17 | 0.33 |
Other details
CETP at Mathura, U.P.
Name
of the Project :
Mathura Industrial Area Pollution Control Co. Ltd.
D-70, Site-A, Industrial Area
Mathura (U.P.)
Phone : 0565-461254
No. of Contributing Members : 30
Area of CETP Site : 16540 sq.m.
Designed Capacity of CETP : 6250 m3/d
Cost of Project : Rs. 18.8 million
Commencement of CETP : Oct. 1997 (Stabilised since June 1998)
Treatment units :
Equalisation tank
Grit chamber
Flash mixer
Clariflocculator
Aeration tank
Secondary clarifier
Sludge Drying Beds
Effluent characteristics ( as on Nov. 1999)
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Other details :
CETP at Naroda, Ahmedabad, Gujarat
Name of the Project :
Naroda Enviro Projects Ltd.,
CETP Division
Plot No. 512-515, Opp. : Naroda Post Office
GIDC Estate, Naroda, Ahmedabad
Phone: 079-2816311, Fax: 079-2823299
No. of Contributing Members
:
229
Area of CETP Site :
16,500 sq.m.
Designed Capacity of CETP : 3,000 m3/d
Present Flow being Received :
Plant has not as yet been commissioned, However it is expected
@ 70% of designed capacity.
Cost of Project :
Rs.79.5 million (including cost of conveyance, treatment and
disposal
Commencement of CETP : July,1999
Treatment units :
Collection sump
Oil and Grease trap
Equalization tank 3 nos.
Flash mixer
Clarifloculater
Aeration basin with diffused aeration 4 nos.
Second clarifier 2 Nos.
Treated water sump 1 No.
Plate and frame type filter press and
sludge beds for de-watering of sludge
Other details :
CETP At Nandesari, dist., Gujarat
Name of the
project :
Pollution Advisory Committee
Nandesari Industries Association
Plot No.135/1, GIDC Estate
Nandesari - 391 340. Distt. : Vadodara
Phone : 0265 - 840390 Fax : 0265 - 840890
No. of Contributing Members :
226
( mostly Organic / inorganic chemical ,
dye / dye intermidiate units)
Area of CETP Site :
6918 sq.m. (Land area)
Designed Capacity of CETP :
11250 m3/d
Cost of Project : Rs 30 million (does not include conveyance & disposal cost)
Commencement of CETP : Nov. 1994
Treatment units :
Collection cell
Grit chamber
Equalization tank
Flash mixer
Flocculation tank
Primary clarifier
Aeration tank with surface aeration
Secondary clarifier
Gravity sand and activated carbon filter
Sludge drying beds.
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Other details :
CETP At Ankleshwar, Gujarat
Name of the project :
M/s Enviro Technology Ltd.
Ankleshwar, Gujarat
No. of Contributing Members :
200
Designed Capacity of CETP :
1000 m3/d
Cost of Project :
Rs 59.90 million
Commencement of CETP :
Dec. 1996
Treatment units :
Equalisation tank
Flash Mixture
Primary Clarifier
Aeration tank
Secondary Clarifier
Chlorination,HyderogenPeroxideTreatment
Sand bed
Granular Activated Carbon Tower
Rotory Vacuum Drum Filter
Effluent characteristics ( as on March 2000)
| Sample specification | pH | SS | TDS | BOD | COD | Cl- | S2- | Phenol |
| Raw effluent after equalisation | 1.97 | 570 | 48910 | 2183.5 | 6940 | 26309 | 19.74 | 8.65 |
| Final treated effluent | 7.72 | 590 | 8070 | 31.5 | 381.5 | 3893 | 0.59 | 1.83 |
Pollution load status ( as on March 2000)as received by CETP Ankleshwar
| Flow | SO4- | SS | TDS | BOD | COD | Cl- | S2- | Phenol |
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Other details :
Jeedemetla CETP, Andhra Pradesh
1. Name of the project : M/s Jeedimetla Effluent Treatment Plant Ltd.
2. Members :
109 medium and small scale units ,
out of which 66 are active members
contributing effluent to CETP
3. Designed capacity :
1500 m3/d, 66% from bulk drugs,
20% from dye & dye inter- Mediate, 14% from others
4. Cost of project : Rs. 25 million
5. Date Commencement : 1989
6. Conveyance system : Through tankers
7. Treatment units :
Neutralisation tank - 2 nos
Equalisation tank - 2 nos
Clariflocculator - 1 nos
Buffer tanks - 3 nos
Distribution
Chamber - 1000 m3
Aeration tank - 3 nos
Sec. Clarifier - 2 nos
Primary SDB - 6 nos
Sec. SDB - 3 nos
8. Measures undertaken at CETP
9. Measures suggested at industry level
11. Pattern of cost sharing
:
On the basis of C.O.D., in addition to this a minimum
charge is levied from all member units irrespective they
are active or not, as the CETP already has built-in
treatment capacity for them
1. Name of the project :
M/s Punjab Small Scale Industries Export Co-operation
(PSIEC), Leather Complex, Kapoorthala Rd.
Jullundhar, Punjab .
2 Members : 29 medium and small scale units pursuing chrome tanning
3. Area of CETP : Approximately 40,000 sq.m
4. Designed capacity :
1500 m3/d, pre-treated tannery waste blended in 9: 1
proportion with sewage.
5. Cost of project : Rs. 9.6 million
6. Operational cost : Rs. 4.03 million / y
7. Date of Commencement : June 1995
8. Conveyance system :
The CETP is established in leather complex, wherein the
member units are also established. The effluent is conveyed
through 2 ft. wide RCC / RBC open channels
9. Treatment units :
Equalisation tank - 1 no.
Reaction channel
Oxidation tank
Primary Clarifier - 1 no.
Main Clarifier - 1 no.
Aeration tank - 1 no.
Polishing pond - 1 no.
Sec. Clarifier - 1 no.
Sludge tank - 2 no.
Sludge beds
10. Pattern of cost sharing :
On the basis of plot size and volume of effluent.
CETP at Unnao, U.P.
Name of the project :
M/s Unnao Tanneries Pollution Control Co. Ltd.(UTPCCL)
A-&, Site-II, Indl. Area, Unnao
Members :
21 medium and small scale units pursuing chrome and
vegetable tanning , out of which 11 are active members
contributing effluent to CETP
Designed capacity : 2150 m3/d
Area of project : 20311 sq.m
Cost of project : Rs. 19.5 million
Operational cost : Rs. 7.03 million
Date of Commencement : 31.01.1996
Conveyance system :
5 km long closed conveyance network made of HDPE / RCC
followed by drains covered with pre-cast slabs.
Treatment units :
Screen chamber - 2 nos.
Equalisation tank - 2 nos
Clariflocculator - 2 no
Aeration Tank - 2 no
Clarifier - 2 no.
Sludge Beds - 20 nos
Effluent characteristics ( as on Dec. 1998)
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Measure(s) undertaken at CETP
Measures at industry level
.Pattern of cost sharing
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On the basis of raw water consumption / standard rate of effluent generation.
CETP at Kanpur, U.P.
Name of the project : 36 MLD, UASB Plant, Jajmau, Kanpur.
Members :
354 tanneries, Out of which 305 are active members
which consist of 167 chrome tanning units, 35 vegetable
tanning, 55 pursuing both type of tanning
and 48 units
engaged in leather splitting. Out of 305 active members
6 are in large scale and remaining 299 in small or medium
scale category.
Designed capacity :
36000 m3/d, consisting of mixture of tannery
waste and sewage blended in 1:3 ratio.
Area of project : 30,000 sq.m
Cost of project :
Conveance system : Rs. 39.08 million
Post treatment :
Rs. 62.99 milion
Conveyance system :
Through 17.57 km long network, wherein majority is closed
and some of the portions are open channel
covered with
pre-cast slabs. Flow is facilitated by 4 pumping
stations
located at appropriate junction in the network
Treatment units :
Screen chamber - 4 nos; Grit channel - 4 nos.
Equalisation tank - 2 nos; UASB reactors - 2 nos
Collection well - 1 no; Diffuser - 1 no
Dosing tank - 1 no; Clariflocculator - 2 no
Sludge thickener - 1 no; Gas holder - 1 no.
Sludge Beds
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Measure(s) undertaken at CETP
2. Designed capacity of Gas generation : 1800 M3/D
3. Designed capacity of Gas dome : 600 M3
4. Nos. and wattage of Gas engines : 3 Nos.180 KW each.
5. Hourly consumption of Gas : 3x75 M3
2. Time required to completely fill
the gas dome(Plant on KESA supply) : 8 hrs.
3. Gas Amount in excess which should
either be utilized or flared. : 1200 M3/d
4. Duration for which the entire plant
can be run exclusively on Gas, once
the Gas dome is completely filled. : 3.8 hrs.
5. Duration for which the entire plant
can be run by completely utilizing
the designed gas production.
(1800 M3/day). :11.61 hrs.
* The CETP at Kanpur has its designed capacity of 36 MLD and receives combined waste constituted by 9 MLD Tannery waste and 27 MLD Sewage. The treatment is through UASB Anaerobic process