Highly-antifouling PVDF membrane products have entered the international market and are being used normally worldwide.
For more information, please see the product page, PVDF Ultrafiltration Membrane.
Through the transformation of technology industrialization and products performance improvement, the large-scale and continuous production of highly-antifouling PVDF hollow fiber membranes has been realized. The ultrafiltration membrane has fully reached the standard and officially launched to the market in batches. And its productivity is up to 1.2 million square meters every year.
Performances comparison under the same conditions | Highly-antifouling PVDF membranes | Normal PVDF membranes |
Water flux, LMH | 40 – 45 | < 25 |
TMP, bar | ~0.5 | 1.0 – 1.5 |
Performances comparison under the same conditions | Highly-antifouling PVDF membranes | Normal PVDF membranes |
Water flux, LMH | >55 | <22 |
TMP, bar | ~0.5 | 1.0 – 1.5 |
Performances comparison under the same conditions | Highly-antifouling PVDF membranes | Normal PVDF membranes |
Water flux, LMH | 50 - 64 | <26 |
TMP, bar | 0.5 – 1.0 | 1.5 – 2.0 |
Performances comparison under the same conditions | Highly-antifouling PVDF membranes | Normal PVDF membranes |
Water flux, LMH | >60 | <30 |
TMP, bar | 0.5 – 1.0 | 1.5 – 2.0 |
Performances comparison under the same conditions | Highly-antifouling PVDF membranes | Normal PVDF membranes |
Water flux, LMH | ~60 | <30 |
TMP, bar | 0.5 – 1.0 | 1.5 – 2.0 |
Parameters | Feed Water | Produced Water |
COD (mg/L) | 200-400 | ≤50 |
BOD (mg/L) | ≤200 | ≤10 |
TN(mg/L) | ≤50 | ≤15 |
pH | 6-9 | 6-9 |
SS | ≤200 | ≤5 |
NH3-N | ≤30 | ≤5(Summer); ≤50(Winter) |
TP | ≤3 | ≤0.5 |
Turbidity | ≤0.5 |
Parameters | Feed Water | Produced Water |
COD(mg/L) | 100~120 | ≤30 |
pH | 6-9 | 6-9 |
SS | ≤30 | ≤5 |
NH3-N | ≤30 | ≤5 |
TP | ≤3 | ≤0.5 |
Turbidity | ≤0.1 |
Parameters | Feed Water | Produced Water |
COD (mg/L) | 200-400 | ≤30 |
BOD (mg/L) | ≤200 | ≤10 |
TN (mg/L) | ≤50 | ≤15 |
pH | 6-9 | 6-9 |
SS | ≤200 | ≤5 |
NH3-N | ≤30 | ≤5 (Summer); ≤8 (Winter) |
TP | ≤3 | ≤0.5 |
Turbidity | ≤0.1 |
Parameters | Unit | Limit |
COD(mg/L) | mg/L | ≤500 |
BOD(mg/L) | mg/L | ≤300 |
TSS | mg/L | ≤150 |
NH3-N | mg/L | ≤50 |
Animal and vegetable oils | mg/L | ≤30 |
Mineral oil | mg/L | ≤3 |
PH | 6-9 |
No | Project name | Construction scale | Main process | Operation time |
1 | Municipal Wastewater Recycling | 50000 t/d | Pretreatment + UF + RO | 2019 |
2 | Steel Wastewater Reuse | 50000 t/d | Pretreatment + UF + RO + EDI | 2018 |
3 | Metallurgical Wastewater Reuse | 3500 m3/d | Pretreatment + UF + RO + ED + MVR | 2017 |
4 | Papermaking Wastewater Treatment | 25000 m3/d | Pretreatment + UF+ RO | 2016 |
5 | Desalination Water Treatment | 8000 m3/d | Pretreatment + UF + RO | 2016 |
6 | Chemical Wastewater Reuse | 4500 m3/d | O₃ + UF + RO | 2016 |
7 | Power Plant Wastewater Reuse | 14400 m3/d | Pretreatment + UF + RO + Mixed bed | 2016 |
8 | Papermaking Wastewater Reuse | 22800 m3/d | O₃ + UF + RO | 2016 |
9 | Pharmaceutical Wastewater Reuse | 20000 m3/d | O₃ + UF + RO | 2015 |
10 | Wastewater Reuse | 4400 m3/d | Pretreatment + UF + RO | 2014 |
11 | High-Concentrated Chemical Wastewater Reuse | 500 m3/d | Pretreatment + UF + RO | 2014 |
12 | Demonstration Project of Wastewater Reuse | 40000 m3/d | Membranes Integrated Systems | 2013 |
13 | Power Plant Wastewater Reuse | 12000 m3/d | Pretreatment + UF + RO + Mixed bed | 2013 |
14 | Highly Polluted Surface Water Purification | 12000 m3/d | Pretreatment + UF | 2013 |
15 | Pharmaceutical Wastewater Reuse | 18000 m3/d | Pretreatment + UF + RO + Mixed bed | 2012 |
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