Ultrafiltration Plants
Ultrafiltration Plants
Treatment Plants and identifying synergies between various treatment technologies. Our Membrane division at Kanpur, India has a state-of-the-art Manufacturing facility spread
over 120,000 ft2, integrated from raw aterial
storage till membrane packaging all under 1 roof. The facility is also equipped with a Research & Development center and a QC lab to ensure continuous product improvement as well as consistency of latest specifications. Technorbital is one of the few membrane manufactures with An ISO 9001:2000 certified Quality Management System.
RWS from Technorbital connects our innovations, experience, commitment to offer low cost simple solutions to our global customers and we are blessed that our products have over 4000000 satisfied users.
Welcome to Right Water System, your trusted partner for advanced UF Plant Manufacturer in Delhi. With our commitment to innovation and quality, we specialize in designing and manufacturing UF plants that cater to the diverse water purification needs of industries, communities, and commercial establishments.
Experienced advanced UF plant in Delhi with Right Water System in Delhi. Our UF plant is engineered to deliver exceptional water purification and filtration capabilities, ensuring the removal of suspended solids, bacteria, and other contaminants from water sources. With our commitment to innovation and quality, we offer premium UF plant solutions that provide clean and safe water for various applications.
We specialize in designing and manufacturing UF plant in Delhi tailored to meet the diverse needs of industries, communities, and commercial establishments in Delhi. Our UF plants are built using cutting-edge technology and high-quality materials, ensuring reliable performance, durability, and long-term efficiency.
Advantages of UF over Conventional Media Filtration
Operational Flux | Guidelines | |||||||
---|---|---|---|---|---|---|---|---|
Filtration | Cycle | |||||||
Type of Feed Water | Unit | Cross | - Flow | Backwash | ||||
Dead | End | With | Media Filter | Without | Media Filter | |||
Time , min | Flux , l.m2.h¹ | Time , min | Flux , L.m².h¹ | Time , min | Flux , L.m².h * ¹ | l.m2.h | ||
Bore Water | L.m³.h¹ | 0.5 | 80 | ΝΑ | ΝΑ | ΝΑ | ΝΑ | 160 |
Surface Water | l.m2.h¹ | 0.5 | 50 | 1 | 85 | 0.5 | 70 | 160 |
Treated Sewage | L.m².h¹ | NA | ΝΑ | 1 | 70 | 0.5 | 50 | 160 |
Treated Effluent | L.m².h¹ | ΝΑ | ΝΑ | 0.5 | 60 | 0.5 | 40 | 160 |
Effluent with Solvent * | L.m².h¹ | ΝΑ | ΝΑ | 0.5 | 50 | 0.5 | 40 | 160 |
Sea Water | l.m².h | ΝΑ | ΝΑ | 0.5 | 40 | 0.5 | 30 | 160 |
Process Engineering
Ultrafiltration Module | Unit | All Model |
---|---|---|
Mode of Operation | Out - In | |
Maximum Applied Feed Pressure | kg.cm² | 2 |
Maximum Trans - membrane Pressure | kg.cm² | < 1.5 |
Backwash Duration | S | 30-60 |
Backwash Frequency | min | 15-60 |
Backwash Flux | L.m².h¹ | 160 |
Typical Clean water Flux Range | L.m².h¹ | 200-250 |
Minimum Operating Temperature | ° C | 5 |
Maximum Operating Temperature | ° C | 40 |
Operating pH Range | 3.5-10.5 | |
Cleaning pH Range | 2-12 | |
Instantaneous Chlorine Tolerance | mg.l¹1 | 200 |
Maximum Instantaneous Feed Turbidity | NTU | 100-300 |
Maximum shell inlet pressure | kg.cm² | 3.5 |
Continuous FRC | mg.l | 0.2 |
Process Cycle | Process Backwash | |
Chemical Cleaning Method | CIP |
Physical Properties
Ultrafiltration Module | Unit | All Model |
---|---|---|
Configuration | Cross - flow / Dead End | |
Membrane Type | Hollow Fibers | |
Membrane Material | PolyNorbit | |
Housing Material | UPVC | |
Fiber Dimensions OD | ID | mm | 1.210.8 |
Pore Size | micron ( p ) | 0.02 |
MWCO ( Nominal ) | kDa | 75 |
System Integration | Modular Rack | |
Chemical Compatibility
Ultrafiltration Module | All Model |
---|---|
Disinfection Chemicals | NaOCI / H₂O₂ |
Cleaning Chemicals | Citric Acid |
Cleaning Chemicals | Na₂CO3 |
Performance Guarantee
Ultrafiltration Module | Unit | All Model |
---|---|---|
Filtrate Turbidity | NTU | < 0.5 |
Bacteria Removal | log reduction | 6 |
Virus Removal | log reduction | 4 |
Total Suspended Solids | mg . Activate | Window |
Silt Density Index SDI₁5 | Go to | Setting to activa |
Performance Guarantee
Ultrafiltration Module | Specification | RWS 4040 | RWS 6040 | RWS 8040 | RWS 8060 |
---|---|---|---|---|---|
Module Diameter | mm ( inch ) | 100 ( 4 ) | 175 ( 7 ) | 215 ( 8.5 ) | 215 ( 8.5 ) |
Module Length | mm ( inch ) | 1146 ( 45 ) | 1290 ( 51 ) | 1300 ( 51 ) | 1524 ( 60 ) |
Weight | kg | 7 | 18 | 28 | 38 |
Nominal Membrane Area | m² | 9 | 26 | 37 | 55 |
Ultrafiltration Module | Specification | RWS 4040 | RWS 6040 | RWS 8040 | RWS 8060 |
---|---|---|---|---|---|
Module Diameter | mm ( inch ) | 100 ( 4 ) | 175 ( 7 ) | 215 ( 8.5 ) | 215 ( 8.5 ) |
Module Length | mm ( inch ) | 1146 ( 45 ) | 1290 ( 51 ) | 1300 ( 51 ) | 1524 ( 60 ) |
Weight | kg | 7 | 18 | 28 | 38 |
Nominal Membrane Area | m² | 9 | 26 | 37 | 55 |
Chemical | Preparation | Guideline | ||||
---|---|---|---|---|---|---|
Sr. No. | Names | IS . NO . | Concentration | Application | Cleaning Time | Attention ! |
1 | Citric Acid | IS 13186 : 1991 | 2.00 % | Inorganic CaCO3 | 1-3 Hours | If pH increases by 0.5 while recycling the solution then , restore the pH using HCl . |
2 | Oxalic Acid | IS 501 : 1976 | 2.00 % | Inorganic Metal Ion + CaCO3 | 1-3 Hours | |
3 | Sodium Carbonate | IS 251 : 1998 | 0.20 % | Organic , Oil | 1-3 Hours | If pH decreases by 0.5 while recycling the solution , then restore the pH using NaOH . |
4 | Sodium Hypochlorite | IS 11673 : 1992 | 0.20 % | Biological | 1-3 Hours | |
5 | Sodium Hydroxide | IS 252 : 1991 | 0.10 % | Organic , Oil | 1-3 Hours | Before use take Prior approval by Technorbital Advanced Materials Pvt . Ltd. |
6 | Sodium Dodecyl Sulfate | IS 4956 : 2002 | 0.10 % | Organic , Oil | 1-3 Hours | |
7 | Sodium Benzoate | IS 4447 : 1994 | 0.10 % | Only Membrane Preservation | ΝΑ | This chemical to be used only during Prolong storage membranes . Follow Procedure |
Step | UF System Operation Logic | |||||||||||||||
Description | ||||||||||||||||
UF System | ||||||||||||||||
Start Mode | (P1) | (P2) | (P3) | (V1) | (V2) | (V3) | (V4) | (V5) | (V6) | (V7) | (V8) | (IV1) | (IV2) | |||
Filtration Cycle | ||||||||||||||||
Filtration Service | 1 | 29 min | --- | ON | OFF | OFF | ON | ON | OFF | OFF | OFF | ON | OFF | OFF | ON | ON |
Backwash | 2 | 1 min | --- | OFF | ON | OFF | OFF | OFF | ON | ON | OFF | ON | OFF | OFF | ON | ON |
Draining | 3 | NA | --- | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | OFF | OFF | ON | ON |
Membrane Performance Restoration | 1 | NA | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | OFF | OFF | ON | ON | |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Draining | --- | |||||||||||||||
Clean In Place | 2 | 30 min | --- | OFF | OFF | ON | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | ON | ON |
Soaking | 3 | 60 min | NA | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON |
Draining | 4 | NA | --- | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | OFF | OFF | ON | ON |
Backwash | 5 | 1 min | --- | OFF | ON | OFF | OFF | OFF | ON | ON | OFF | ON | OFF | OFF | ON | ON |
Flushing | 6 | 1 min | --- | ON | OFF | OFF | OFF | OFF | OFF | ON | OFF | OFF | ON | ON | ||
Filtration Service | 7 | 29 min | --- | ON | OFF | OFF | ON | ON | OFF | OFF | OFF | ON | OFF | OFF | ON | ON |
Membrane Storage Procedure | 1 | NA | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | OFF | OFF | ON | ON | |
Draining | --- | |||||||||||||||
Clean In Place | 2 | 30 Min | --- | OFF | OFF | ON | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | ON | ON |
Soaking | 3 | 60 Min | NA | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON |
Draining | 4 | NA | --- | OFF | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | OFF | OFF | ON | ON |
Backwash | 5 | 1 Min | --- | OFF | ON | OFF | OFF | OFF | ON | ON | OFF | ON | OFF | OFF | ON | ON |
Flushing | 6 | 1 Min | --- | ON | OFF | OFF | OFF | OFF | OFF | ON | OFF | OFF | ON | ON | ||
Preservative | 7 | 2 Min | - | OFF | OFF | ON | OFF | OFF | OFF | OFF | OFF | OFF | ON | ON | ON | ON |
Injection |