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Preparation method of micro-wave-shaped hollow fiber nanofiltration membrane

A technology of nanofiltration membrane and microwave wave, which is applied in the field of filtration membrane, can solve the problems of limited effective area of ​​straight membrane, small flux of filter element assembly, high degree of freedom of membrane, etc., achieve low degree of freedom, increase flux of filter element, increase effective area Effect

Inactive Publication Date: 2021-06-08
NINGBO FOTILE KITCHEN WARE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The current hollow fiber nanofiltration membranes are all straight and cylindrical. In the structure of the filter element assembly, the gap between the membrane filaments is relatively large. During the flow of water, the membrane has a high degree of freedom and is easy to break; in addition The effective area of ​​the straight membrane is limited, so the flux of the assembled filter element assembly is small

Method used

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  • Preparation method of micro-wave-shaped hollow fiber nanofiltration membrane
  • Preparation method of micro-wave-shaped hollow fiber nanofiltration membrane
  • Preparation method of micro-wave-shaped hollow fiber nanofiltration membrane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] 1) Polysulfone (PSf) polymer (molecular weight 70,000), N,N-dimethylacetamide (DMAc), pore size regulator polyvinylpyrrolidone (PVP) (molecular weight 10,000) and pure water according to mass percentage Prepare casting solution by mixing 25%, 47%, 20%, and 8% in turn; prepare core solution by mixing 50% and 50% of N, N-dimethylacetamide and pure water according to mass percentage; mix casting solution The core liquid and the core liquid are respectively injected into a spinneret through the casting liquid channel and the core liquid channel through the gear pump, and the hollow tubular liquid film is extruded through the casting liquid port and the core liquid port of the spinneret. The inner and outer diameters of the membrane filaments are 0.2 / 0.4mm, casting fluid pressure is 2bar, temperature is 45°C, flow rate is 15g / min, core fluid pressure is 0.5bar, temperature is 45°C, flow rate is 1g / min, spinneret temperature is 45°C.

[0028] 2) The liquid film enters the ge...

Embodiment 2

[0031]1) Polysulfone (PSf) polymer (molecular weight 90,000), N,N-dimethylacetamide (DMAc), pore size regulator polyvinylpyrrolidone (PVP) (molecular weight 20,000) and pure water according to mass percentage 18%, 74%, 5%, and 3% were mixed successively to prepare the casting solution; N, N-dimethylacetamide and pure water were mixed according to the mass percentage of 60% and 40% respectively to prepare the core solution; the casting film The liquid and the core liquid are respectively injected into a spinneret through the casting liquid channel and the core liquid channel through the gear pump, and the hollow tubular liquid film is extruded through the casting liquid port and the core liquid port of the spinneret. 0.4 / 0.6mm, the casting fluid pressure is 1bar, the temperature is 45°C, the flow rate is 5g / min, the core fluid pressure is 0.5bar, the temperature is 45°C, the flow rate is 1g / min, and the spinneret temperature is 45°C.

[0032] 2) The liquid film enters the gel t...

Embodiment 3

[0035] 1) Polyethersulfone (PES) polymer (molecular weight: 90,000), dimethyl sulfoxide (DMSO), pore size regulator polyethylene glycol (PEG) (molecular weight: 2000) and pure water are 18% by mass. %, 74%, 5%, and 3% were mixed to prepare the casting solution; the core solution was prepared by mixing dimethyl sulfoxide and pure water according to the mass percentage of 75% and 25% respectively; the casting solution and the core solution were respectively passed through the gear The pump is injected into a spinneret through the casting liquid channel and the core liquid channel, and the hollow tubular liquid film is extruded through the casting liquid port and the core liquid port of the spinneret. The membrane liquid pressure is 1 bar, the temperature is 50°C, the flow rate is 10g / min, the core liquid pressure is 0.3 bar, the temperature is 55°C, the flow rate is 0.7g / min, and the spinneret temperature is 45°C.

[0036] 2) The liquid film enters the gel tank (gel device) afte...

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Abstract

The invention discloses a preparation method of a micro-wave-shaped hollow fiber nanofiltration membrane, which is characterized by comprising the following steps: 1) a membrane casting solution and a core solution are respectively extruded from a membrane casting solution opening and a core solution opening of a spinning nozzle to form a hollow tubular liquid membrane; and 2) the liquid membrane passes through the air gap and then enters a gelation device to form a gel-state primary membrane filament, a filament winding fence is arranged in the gelation device, the primary membrane filament passes through the filament winding fence to form a micro-wave-shaped membrane filament, and the micro-wave-shaped membrane filament is washed and cured after going out of the gelation device to obtain the micro-wave-shaped hollow fiber ultrafiltration base membrane. The micro-wave-shaped membrane filaments can be tightly arranged, the degree of freedom is low, impact of water flow on some positions is reduced, and the filament breaking condition is well avoided; the effective area of a nanofiltration membrane in the filter element is increased, and the filter element flux is improved; and the preparation method is simple, small in investment and convenient for industrialization.

Description

technical field [0001] The invention belongs to the technical field of filter membranes, and in particular relates to a preparation method of a microwave-shaped hollow fiber nanofiltration membrane. Background technique [0002] Nanofiltration membrane is a new type of membrane separation technology that has developed rapidly in recent years. Hollow fiber nanofiltration membrane combines many advantages of hollow fiber and composite nanofiltration membrane. It has a self-supporting structure. The operating pressure of the membrane module is low, the membrane packing density is relatively high, and the pretreatment and maintenance are simpler than roll-type membranes. It can be widely used It is a hot spot in the field of nanofiltration membrane research in recent years when it is used in softened water, desalination of brackish water, food processing and electronics industry. The current hollow fiber nanofiltration membranes are all straight and cylindrical. In the structur...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D67/00B01D69/08
CPCB01D67/0002B01D67/0006B01D67/0009B01D69/08
Inventor 李诗文毕春莹卜凡敏
Owner NINGBO FOTILE KITCHEN WARE CO LTD