|
|
|
 |
|
 |
| |
| NAME
OF THE CUSTOMER |
 |
SAGAR
SUGAR & ALLIED PRODUCTS LIMITED |
......................................................................................................................................... |
| NATURE
OF INDUSTRY |
 |
POWER
PLANT |
......................................................................................................................................... |
| TYPE
OF THE WATER |
 |
BORE
WELL WATER |
......................................................................................................................................... |
| PLANT
PROPOSED |
 |
ULTRAFILTRATION
SYSTEM - 45.0 M3 / HR. REVERSE
OSMOSIS - 30 M3 / HR.
|
......................................................................................................................................... |
|
OBJECTIVE
:
TO DESIGN THE PLANT FOR CAPABLE OF DELIVERING TREATED
WATER TO SUIT BOILER FEED QUALITY.
SCHEME
PROPOSED :
PRETREATMENT -
ULTRAFILTRATION SYSTEM - REVERSE OSMOSIS
SYSTEM - MIXED BED SYSTEM
DESIGN BASIS :
S.
No. |
Parameters |
Units |
Feed
Quality |
Treated
Water
Quality |
1. |
Total Dissolved Solids |
Ppm |
1470 |
Conductivity :
< 0.2 mscm2 |
|
....................................................................................................................................... |
2. |
Colloidal Silica |
Ppm |
14 |
Nil |
|
....................................................................................................................................... |
3. |
Silica |
Ppm |
60 |
< 0.02 ppm |
|
....................................................................................................................................... |
4. |
SDI |
Ppm |
>
5 |
<
2 |
|
|
|
|
|
BENEFITS :
•
The purpose of incorporating Ultrafiltration system
is to remove Coloidal silica, suspended particles &
Bacteria & SDI, thus enabling the RO plant to operate
at a higher flux rate.
•
Providing State-of-art-Ultrafiltration system, by eliminating
conventional system -lime dosing for reduction of Coloidal
Silica to the acceptable limit to RO system.
•
Provision of UF system enhance the life of the RO membranes
and also increase the frequency of chemical cleaning.
•
Membrane based technology gives consistent water quality
even in wide variations of feed water quality
•
Lower foot print
•
No Sludge
•
Lower operating cost
•
Less maintenance Cost
• Less man power
|
| |
 |
| NAME
OF THE CUSTOMER |
 |
TUBE
PRODUCTS INDIA LTD. |
......................................................................................................................................... |
| NATURE
OF INDUSTRY |
 |
STEEL
INDUSTRY |
......................................................................................................................................... |
| PLANT
PROPOSED |
 |
ULTRAFILTRATION
SYSTEM - 11.0 M3 / HR. REVERSE
OSMOSIS - 12.25 M3 / HR.
|
......................................................................................................................................... |
OBJECTIVE
:
TO DESIGN THE PLANT CAPABLE OF DELIVERING TREATED WATER
TO BOILER FEED QUALITY , COOLING TOWER MAKE UP WATER
& PROCESS WATER APPLICATION
SCHEME
PROPOSED :
PRETREATMENT
- ULTRAFILTRATION SYSTEM - REVERSE
OSMOSIS SYSTEM
DESIGN BASIS :
S.
No. |
Parameters |
Units |
Feed
Quality |
Treated
Water
Quality |
| 1. |
TDS |
Ppm |
4000 |
50 |
|
....................................................................................................................................... |
2. |
Silica |
Ppm |
40 |
2 |
|
....................................................................................................................................... |
3. |
pH |
|
8 |
5.5 |
|
|
|
|
|
BENEFITS :
• The
purpose of incorporating Ultrafiltration system is to
remove Colloidal silica, suspended particles & Bacteria
& SDI, thus enabling the RO plant to operate at
a higher flux rate.
•
Providing State-of-art-Ultrafiltration system, by eliminating
conventional system and lime dosing for reduction of
Colloidal Silica to the acceptable limit to RO system.
•
Provision of UF system would enhance the life of the
RO membranes and also increased the frequency of chemical
cleaning.
•
The membrane based technology gives consistent water
quality in wide variations of feed water quality
• Lower foot
print
• Lower operating
cost
• Less maintenance
Cost
• Less man
power
• No Sludge
• Eco-friendly
system
|
| |
 |
| NAME
OF THE CUSTOMER |
 |
BRAKES
INDIA LIMITED |
......................................................................................................................................... |
| NATURE
OF INDUSTRY |
 |
AUTOMOBILE
INDUSTRY |
......................................................................................................................................... |
| TYPE
OF THE WATER |
 |
WASTE
WATER |
......................................................................................................................................... |
| PLANT
PROPOSED |
 |
ULTRAFILTRATION
SYSTEM - 6.25 M3 / HR.
REVERSE
OSMOSIS - STAGE I 4.0 M3 / HR.
REVERSE OSMOSIS - STAGE II 1.0 M3 / HR.
|
......................................................................................................................................... |
OBJECTIVE
:
TO DESIGN THE PLANT FOR CAPABLE OF DELIVERING THE TREATED
EFFLUENT, WHICH WAS DISCHARGED TO THEIR SOLAR EVAPORATION
POND. MTL SUGGESTED BIL THAT THIS QUANTITY OF TREATED
EFFLEUNT CAN BE RECYCLED BACK TO THEIR PROCESS, THUS
ENABLING THEM TO REDUCE THE RAW WATER CONSUMPTION.
SCHEME
PROPOSED :
PRETREATMENT
- ULTRAFILTRATION SYSTEM - REVERSE
OSMOSIS SYSTEM STAGE
I - OSMOSIS
SYSTEM STAGE
II
DESIGN BASIS :
S.
No. |
Parameters |
Units |
Feed
Quality |
Treated
Water
Quality |
| 1. |
Total Dissolved Solids |
Ppm |
5000 |
< 500 [at II Stage] |
|
....................................................................................................................................... |
2. |
TSS |
Ppm |
30 |
BDL |
|
....................................................................................................................................... |
3. |
Silica |
Ppm
|
40
- 50 |
<
2 |
|
|
|
|
|
BENEFITS :
• The
resin based DM Plant discarded from the operation thus
eliminating the regenerant effluent and high maintenance
cost.
•
Consisting quality in treated water quality to their
process
•
Less man power
•
Minimum quantity of Sludge
•
Lower operating cost
•
Eco friendly system
•
The final reject for discharge reduced 8.0 M3 / Day
and hence reduction in area for the reject disposal
•
Providing State-of-art-Ultrafiltration system, by eliminating
conventional system and lime dosing for reduction of
Colloidal Silica & SDI to the acceptable limit to
RO system.
•
Provision of UF system would enhance the life of the
RO membranes and also increased the frequency of chemical
cleaning.
•
Lower foot print
• Eco-friendly
system
|
| |
 |
| NAME
OF THE CUSTOMER |
 |
PERFETTI VANMELLE INDIA
LTD. |
......................................................................................................................................... |
| NATURE
OF INDUSTRY |
 |
CONFECTIONARY & FOOD INDUSTRY |
......................................................................................................................................... |
| TYPE
OF THE WATER |
 |
BORE
WATER |
......................................................................................................................................... |
| PLANT
PROPOSED |
 |
PRETREATMENT
: 20 M3 / HR. REVERSE OSMOSIS
- 15.0 M3 / HR. |
......................................................................................................................................... |
OBJECTIVE
:
TO DESIGN THE PLANT FOR CAPABLE OF DELIVERING THE WATER,
TO THEIR BOILER FEED & COOLING TOWER MAKEUP.
SCHEME
PROPOSED :
PRETREATMENT
- REVERSE OSMOSIS SYSTEM
WITH
PROPRIETORY ANTISILICA RO SYSTEM
DESIGN BASIS :
S.
No. |
Parameters |
Units |
Feed
Quality |
Treated
Water
Quality |
| 1. |
Total Dissolved Solids |
Ppm |
1100 |
150 |
|
....................................................................................................................................... |
2. |
Reactive Silica |
Ppm |
64 |
< 4 |
|
....................................................................................................................................... |
3. |
Total
Hardness |
Ppm
|
<
30 |
628 |
|
|
|
|
|
BENEFITS :
• MTL
provided Proprietory Antisilica RO system, due to the
high silica content in the raw water, thus eliminating
the lime dosing, clarifier for precipitation of Silica
•
Eliminates Sludge
• Lower operating
cost
• Less man
power
•
Less maintenance cost
• Eco friendly
system
|
| |
 |
| NAME
OF THE CUSTOMER |
 |
HINDUSTAN
LEVER LTD, |
......................................................................................................................................... |
| NATURE
OF INDUSTRY |
 |
DETERGENT
DIVISION |
......................................................................................................................................... |
| TYPE
OF THE WATER |
 |
WASTE
WATER |
......................................................................................................................................... |
| PLANT
PROPOSED |
 |
ULTRAFILTRATION
SYSTEM - 10.0 M3 / HR.
REVERSE
OSMOSIS 7.0 M3 / HR
|
......................................................................................................................................... |
OBJECTIVE
:
TO DESIGN THE PLANT FOR CAPABLE OF DELIVERING THE TREATED
EFFLUENT, TO THEIR BOILER FEED.
SCHEME
PROPOSED :
PRETREATMENT
- ULTRAFILTRATION SYSTEM - REVERSE
OSMOSIS SYSTEM STAGE
DESIGN BASIS :
S.
No. |
Parameters |
Units |
Feed
Quality |
Treated
Water
Quality |
| 1. |
Total Dissolved Solids |
Ppm |
836 |
< 100 |
|
....................................................................................................................................... |
2. |
Total Hardness |
Ppm |
330 |
BDL |
|
....................................................................................................................................... |
3. |
COD |
Ppm
|
59 |
<
10 Ppm |
|
|
|
|
|
BENEFITS :
• To
cease procurement of DM water from other vendors and
suppliers
•
Logistics involved in handling the water tankers
•
Become self sufficient, thus eliminating the dependency
on 3rd party for the DM water / raw water
•
No Sludge
•
Lower operating cost
•
The final reject for discharge reduced 8.0 M3 / Day
and hence reduction in area for the reject disposal
•
Providing State-of-art-Ultrafiltration system, by eliminating
conventional system and lime dosing for reduction of
Coloidal Silica & SDI to the acceptable limit to
RO system.
•
Provision of UF system would enhance the life of the
RO membranes and also increased the frequency of chemical
cleaning.
•
Lower foot print
•
Eco-friendly system
|
| |
 |
 |
Copyright © 2004 MEMBRANE TECHNOLOGIES LTD. All rights reserved.
|
|