Factory Supply Uf Filter Membrane - MCR Membrane Module Reinforced PVDF BM-SLMCR-30 Replacing Project – Bangmo

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Factory Supply Uf Filter Membrane - MCR Membrane Module Reinforced PVDF BM-SLMCR-30 Replacing Project – Bangmo Detail:

Applications

● Purification of surface water.
● Reuse of heavy metal waste water.
● Pretreatment of RO.

Filtration Performance

Below filtration effects are proved according to the use of modified PVDF hollow fiber ultrafiltration membrane in different types of water:

No.	Item	Water Output Index
1	TSS	≤1mg/L
2	Turbidity	≤ 1

Specifications

Size

product-description1

Chart 1 MBR Size

Technical Parameters

Filtering Direction	Outside-in
Membrane Material	Reinforced Modified PVDF
Precision	0.03 micron
Membrane Area	30m2
Membrane ID/OD	1.0mm/ 2.2mm
Size	1250mm×2000mm×30mm
Joint Size	Φ24.5mm

Component Material

Component	Material
Hollow Fiber Membrane	Reinforced Modified PVDF
Sealing Compound	Epoxy Resins + Polyurethane (PU)
Housing	ABS

Using Conditions

Proper pretreatments must be set when raw water contains a lot of impurities/coarse particles or large proportion of grease. Defoamer must be used to remove foams in membrane tank when necessary, please use alcoholic defoamer which is not easy to scale.

Item	Limit	Remark
PH Range	5-9 (2- 12 when washing)	Neutral PH is better for bacterial culture
Particle Diameter	<2mm	Prevent sharp particles to scratch membrane
Oil & Grease	≤2mg/L	Prevent membrane fouling/sharp flux decrease
Hardness	≤150mg/L	Prevent membrane scaling

Application Parameters

Designed Flux	15~40L/m2.h
Backwashing Flux	Twice the designed flux
Operating Temperature	5~45°C
Maximum Operating Pressure	-50KPa
Suggested Operating Pressure	≤-35KPa
Maximum backwashing Pressure	100KPa
Operating Mode	Continuous opeartion, intermittent backwashing air flushing
Blowing Mode	Continuous Aeration
Aeration Rate	4m3/h.piece
Washing Period	Clean water backwashing every 1~2h; CEB every 1~2 days;Offline washing every 6~12 months (Above information is for reference only, please adjust according to actual differential pressure change rule)

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Membrane Design