American Mobile HealthCare Home
- -
American Mobile HealthCare Profile
- -
American Mobile HealthCare Technology
- -
American Mobile HealthCare Services
- -
American Mobile HealthCare Specification
- -
American Mobile HealthCare MTL Innovation
American Mobile HealthCare Desalination
American Mobile HealthCare Projects Executed
American Mobile HealthCare Infrastructure
- -
American Mobile HealthCare Quality
- -
American Mobile HealthCare R & D
American Mobile HealthCare Gallery
- -
American Mobile HealthCare Feedback
- -
American Mobile HealthCare Contact
- -
Travel nursing is the way to go
 
-
America's leader in traveling healthcare professionals

CHENNAI PETROLEUM CORPN LTD (CPCL)

SAGAR SUGARS & ALLIED PRODUCTS

TUBE PRODUCTS INDIA LIMITED

BRAKES INDIA LIMITED

PERFETTI VANMELLE INDIA LTD

HINDUSTAN LEVER LTD. PONDY
















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.