The textile wastewater by MBR

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The textile wastewater by MBR

The textile wastewater by MBR

The textile wastewater by MBR

The textile wastewater by MBR

The textile wastewater by MBR

The textile wastewater by MBR

Hi Friends

The goal of our company is to recycle #textile #wastewater by #MBR#RO method.
The input #COD of MBR is 1000 ppm and permeate MBR is 100 ppm. While the standard input COD to RO is below 10 ppm.
Can I reduce the COD to 10 ppm?
Thanks for all.

Pictures of the project site

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8 Answers

Mechanical Vapor Compression ...

Mechanical Vapor Compression based Low temperature evaporators are successfully employed in many textile mills in India.  Fully automated, plug and play type.  With your requirement details contact jayakumar.thakur@gmail.com  or whatsapp +91 9443220246

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Tried your email and it was rejected. Questions on your systems: (gallons or m3)

How big can these units be made (million gallons per day)?

Cost to build? per 1000 gallons

Cost to operate? per 1000 gallons

Maximum salt level that can be handled?

Form of salts obtained?

 

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You may add UF as per diagram ...

You may add UF as per diagram attached.

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Could you please share with ...

Could you please share with me the quality of influent in terms of BOD, COD, TSS, pH etc. then I can guide properly because I have done a turnkey project in Carpet Industry. Please forward details on my mail mamta.tomar@gmail.com 

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You can try activated carbon ...

You can try activated carbon filter upwards RO. Regards

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What is the MWCO of the ...

What is the MWCO of the membrane being used. You may need to add a UF or NF prefilter to the RO. That is common.

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Hi Arsalan, Ozonation prior ...

Hi Arsalan,

Ozonation prior to MBR would reduce COD and increase biodegradability of wastewater and filtration, such as sand filtration of MBR effluent should be able to reduce COD to the desired level.

Good luck

Ali Amiri (a.amiri@cogeco.ca) 

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Hi May be if you eliminate ...

Hi

May be if you eliminate the pigments and additives by ferric chloride at pH=7 to 8 and then start your MBR process it reduces your process time and the resulted COD as well. More over, you can ozonate the treated waste water in presense of a UV module with proper debi. I suggest that some amount of the concentrate of the RO  system shoulbe conducted to the entrance of the MBR process to reduce the contimination load and put more water in recycle sequence.

Good luck

Published by alireza Reyhan, Eng

Please go for Forward ...

Please go for Forward Osmosis which will handle the COD of 100 ppm

 

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