OSE-MBR STP are Membrane Bio Reactor based Sewage treatment and recycling plants. It is indigenously developed for meeting stringent treated water norms for sewage water and various other ETP's. It works on principle of biological digestion followed by specially designed submerged hollow fiber membrane filtration. Hollow fiber membranes have pore size of 0.1 –0.06 micron which ensures removal of pathogens and bacteria in treated water. OSE-MBR STP is a combination of membranes, pumps and other electrical equipment's which makes itself unique in operation and having hassle free maintenance.
A membrane bioreactor connects membrane filtration to a biological active sludge system. The membranes thus replace the sedimentation basin in classic biological purification and help to separate the sludge from the effluent. This helps to ensure that all floating matter is retained, whereby sedimentation is no longer a restrictive factor for sludge concentration. A membrane reactor is thus able to process significantly higher sludge concentrations and lower reactor volumes, compared to conventional systems.
The membrane can either be placed next to the biological basin (= external or separate system), or in the basin (= internal or submerged). External systems involve continuous cross-flow circulation along the membranes. Both tubular and flat plate membranes are used to realise this. An internal system involves the effluent being extracted from the active sludge using under-pressure. This normally involves the use of hollow fibres or flat plate membranes.
PARAMETER | DESCRIPTION |
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MOC OF FIBER | REINFORCED PVDF |
SQM AVAILABLE ( SQM / MODULE ) | 10/20/30 SQM– AS PER REQUIREMENT |
FILTRATION MODE | OUT TO IN |
PH RANGE | 2 – 12 |
TEMPERATURE RESISTANCE | Upto 40 deg C |
APPLICATIONS | STP / ETP / CLEAN WATER / FILTRATION |
BACKWASHABLE | YES |
CIP | POSSIBLE WITH HYPO, CITRIC, HCL – As per recommendation of supplier |
MLSS handling capacity | 4000 – 10000 ppm |
Diameter of fibers | 0.9 /2.1 – ID / OD |
Description | Activated Sludge Process | MBBR Moving Bed Bioreactor | OSE-BIOZAP-MBR |
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Process Type | Suspended Growth | Attached Growth | Biological + Filtration |
Area Footprint | Maximum | Moderate | Minimal |
Treatment Efficiency(COD, BOD, TSS) | 80- 90 % Reduction | 90-95 % Reduction | 97-99 % Reduction |
Water quality & Consistency | Low quality & Consistency | Moderate quality & consistency | Excellent quality with Highconsistency |
Required Level Of Manual Intervention | Medium | High | Low |
Maintenance | Difficult | Difficult | Easy |
Water Recovery | 80-90% | > 90% | > 95% |
Enhancement of Treatment capacity | Low Chances | Enhances by 5-10% | Enhances by > 3 X |
Sludge handling | Require Periodic Sludge Wasting Intern Frequent Sludge Handling Equipment Usage | Require Periodic Sludge Wasting Intern Frequent Sludge Handling Equipment Usage | Highly Stabilized Sludge Reduces Sludge Handling Equipment Footprint |
Electrical Consumption | Medium | Medium | Moderate |
Parameter | OSE ‒ Membrane Bio Reactor (MBR) | Conventional Attached Growth Bioflim Process (MBBR/FRB/SAFF etc.) |
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Output water quality |
• For reuse application, the MBR-based treatment approach gives better results (lower COD/BOD) because solid-liquid separation is based on a fine pore submicron membrane. • Nutrient removal is also better or at par in the MBR reactor due to higher MLSS. |
• For reuse application, the MBBR-based approach gives limited results as the final solid-liquid separation is based on gravity. • If MBR-equivalent output is required, then the conventional process would require extensive tertiary treatment and even Ultra Filtration of the treated water. |
Nutrient removal |
• MBR systems due to their higher MLSS operation create a unique ecosystem which is very efficient in removal of nutrients likes nitrogen and phosphorus present in sewage water. |
• If good nutrient removal is desired in conventional technology then special design is required as these technology are very in- efficient in nutrient removal. • The advantage of MBR over conventional technology in nutrient removal has been verified by several studies. |
Treatment stages |
• MBR based approach is only single composite treatment stage. • Single treatment stage makes plant operation easier. |
• There are generally three treatment stage: Primary, Secondary and Tertiary. • Three stages of treatment complicates plant operation. |
Foot print |
• MBR plant have smallest foot print. • Because the treatment stages are composite in nature the plants are compact and their design highly flexible. • Small foot print plant makes design of package plant very easy. |
• Conventional plant occupy nearly double the space that of MBR. • The plant design is in flexible in nature. • Design of package plant is difficult due to bulky nature of plant. |
Sludge quantity |
• As MBR operate on higher MLSS content, the sludge generation is lower than conventional plants. • Higher MLSS operation creates unique environment wherein the plants can be if desired operated in net zero sludge mode. • Lower plant foot print helps plan sludge management well |
• These technologies operate on a limited MLSS values which is ½ to 2/3 less than MBR. • Lower MLSS leads to higher sludge generation. As the plant foot print is higher, there is limited space available for sludge handling. |
Ease of Startup |
• Membrane based system haver lower startup and stabilization time because go nearly 100% retention of bacterial mass within the bioreactor. |
• Conventional Biofilms based process required longer duration for startup. They also require very close monitoring of the process and regular intervention. |
Ease of operation |
• OSE MBR system are by default fully automatic system requiring minimal manual intervention. • Pump operations, Membrane backwashing, air purging, sludge wasting and in-situ CIP happen in auto mode. |
• Manufacturers of conventional plant generally charge extra for a fully automatic plant. |
Scope of Future expansion |
• Treatment capacity of OSE MBR plants can be increased to accommodate increased flow of wastewater. • Higher MLSS based operation gives good results at even lower HRT (Hydraulic Residence Time) |
• Plants based on these technologies cannot be expanded as the HRT are higher and thus it cannot be increased easily. |
Capital cost |
• Capital cost of MBR plants were higher in past due to higher membrane cost. But with reduction in membrane price during past few years, capital cost of packaged MBR plants have come at par with conventional systems |
• Conventional plant has perceived advantage of lower cost, but when complete cost of plant ownership which includes civil and mechanical equipment cost is compared with MBR plant than its at par with MBR based system. |