Audited Supplier
| Type | Hollow fiber | |||
| Film making process | NIPS(wet process) | |||
| Membrane material | PVDF | |||
| nominal bore | 0.03um | |||
| Membrane inner/outer diameter | 0.7/1.3mm | |||
| Component specifications | ||||
| Housing material | UPVC | |||
| Pouring materials | epoxy resin | |||
| Connection port standard | DN50 | |||
| Effective membrane area | 77 squre meters | |||
| Full water weight | 105KG | |||
| Transport weight | 65KG | |||
| Package size | 180X35X36CM | |||
Product Name: Industrial PVDF film material Hollow fiber UF membrane 1060
| Pre-filter | 50-150um | ||||
| Operation mode | External pressure operation (dead end filtration or cross flow filtration) | ||||
| Operation pressure | 0.02~0.2MPa | ||||
| Max inlet pressure | 0.3MPa | ||||
| Maximum transmembrane pressure difference | 0.15MPa | ||||
| Continuous operation pH range | 2~11 | ||||
| operating temperature range | 1ºC~60ºC | ||||
| Influent turbidity | ≤50NTU | ||||
| Backwash frequency | 15-60min/time | ||||
| Backwash pressure | ≤0.2MPa | ||||
| Backwash flow rate | 100~150L/H.m² | ||||
| Air washing aeration pressure | 0.1MPa | ||||
| Air washing aeration time | 30~60 seconds | ||||
| Aeration flow rate(Nm³/h) | 8~12 | ||||
| Component design flux | 2.0~5.0m³/h.pcs | ||||
| Turbidity of produced water | <0.1NTU | ||||
| Water pollution density index (SDI15) | <1 | ||||
| Removing Escherichia coli | 99.99% remove | ||||
| Total number of water producing colonies | <3(CFU/mL) | ||||
High filtration accuracy, good effluent quality (turbidity less than 0.1NTU)
Strong hydrophilicity (contact angle as low as 47 °, less prone to fouling and flux recovery)
Membrane silk has high strength and good toughness (membrane silk elongation exceeds 50%)
Low pressure and high flux (can meet the design flux at a very low transmembrane pressure difference)
Good chemical stability (the performance of the membrane module remains unchanged after 50 acid and alkali chemical cleaning)
Strong anti pollution ability (cleaning cycle extended by 30% compared to peers, and membrane flux recovery effect is good)
Externally pressurized use, with strong pollution capacity and wider inlet water quality.
