Unlock instant, AI-driven research and patent intelligence for your innovation.

Composite porous hollow fiber membrane, composite porous hollow fiber membrane module and operating method thereof

An operating method and fiber membrane technology, applied in chemical instruments and methods, membranes, membrane technology, etc., can solve the problems of rising filtration pressure, difficulty in maintaining filtration volume, etc., and achieve the effect of inhibiting occlusion and excellent chemical durability.

Active Publication Date: 2021-06-04
TORAY IND INC
View PDF11 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

If the occlusion progresses, the filtration pressure increases, so it becomes difficult to maintain the filtration capacity

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Composite porous hollow fiber membrane, composite porous hollow fiber membrane module and operating method thereof
  • Composite porous hollow fiber membrane, composite porous hollow fiber membrane module and operating method thereof
  • Composite porous hollow fiber membrane, composite porous hollow fiber membrane module and operating method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0365] 36% by weight of 1,1-vinylidene fluoride homopolymer (KF1300 manufactured by KLEHA Co., Ltd., weight average molecular weight: 417,000, number average molecular weight: 221,000) and 64% by weight of γ-butyrolactone were dissolved at 150°C. The crystallization temperature Tc of this 1,1-vinylidene fluoride homopolymer solution was 48°C.

[0366] For the pressurization and discharge of the film-forming stock solution, an apparatus including a double pipe die, a pipe connected to the die, and two gear pumps arranged on the pipe was used.

[0367] The membrane-forming stock solution was kept at 99 to 101° C. for 20 seconds while pressurizing it to 2.0 MPa in the piping between the gear pumps. Then, while discharging an 85% by weight aqueous solution of γ-butyrolactone from the inner tube of the double-tube die, the film-forming stock solution was discharged from the outer tube. The film-forming stock solution discharged in this way was allowed to stay in a cooling bath at ...

Embodiment 2

[0378] 36% by weight of 1,1-vinylidene fluoride homopolymer (KF1300 manufactured by KLEHA Co., Ltd., weight average molecular weight: 417,000, number average molecular weight: 221,000) and 64% by weight of γ-butyrolactone were dissolved at 150°C. The Tc of this 1,1-vinylidene fluoride homopolymer solution was 48°C.

[0379] Using the same apparatus as in Example 1, the film-forming stock solution was pressurized to 2.0 MPa and allowed to stay at 99 to 101° C. for 20 seconds. Then, while discharging an 85% by weight aqueous solution of γ-butyrolactone from the inner tube of the double tube die, the film-forming stock solution was discharged from the outer tube of the double tube die. Make the discharged film-forming stock solution stay in the first cooling bath at a temperature of 5° C. consisting of an 85% by weight aqueous solution of γ-butyrolactone for 10 seconds, and then place it in a temperature of 25° C. Solidification was carried out by staying in the second cooling b...

Embodiment 3

[0387] 38% by weight of 1,1-vinylidene fluoride homopolymer (KF1300 manufactured by KLEHA Co., Ltd., weight average molecular weight: 417,000, number average molecular weight: 221,000) and 62% by weight of γ-butyrolactone were dissolved at 150°C. The Tc of this 1,1-vinylidene fluoride homopolymer solution was 51°C.

[0388] Using the same apparatus as in Example 1, the film-forming stock solution was pressurized to 2.0 MPa and allowed to stay at 99 to 101° C. for 20 seconds. Then, while discharging an 85% by weight aqueous solution of γ-butyrolactone from the inner tube of the double-tube die, the film-forming stock solution was discharged from the outer tube. The discharged film-forming stock solution was allowed to stay in the first cooling bath at a temperature of 5°C consisting of an 85% by weight aqueous solution of γ-butyrolactone for 10 seconds, and then placed in a temperature of 35°C consisting of an 85% by weight aqueous solution of γ-butyrolactone. Solidified by st...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
lengthaaaaaaaaaa
pore sizeaaaaaaaaaa
breaking strengthaaaaaaaaaa
Login to View More

Abstract

The present invention relates to a composite porous hollow fiber membrane comprising at least a first layer and a second layer containing a fluororesin-based polymer, wherein a part of the molecular chain of the fluororesin-based polymer is along the The composite porous hollow fiber membrane is oriented in the longitudinal direction, and the degree of orientation π calculated based on a specific formula is 0.4 or more and less than 1.0, the first layer has a columnar structure oriented in the longitudinal direction of the composite porous hollow fiber membrane, and the second layer is The layer has a three-dimensional network structure, and the average pore diameter of the surface is 5.0 nm or more and 5.0 μm or less.

Description

technical field [0001] The present invention relates to a composite porous hollow fiber membrane, a composite porous hollow fiber membrane module, and a method for operating the composite porous hollow fiber membrane module, which can be used in water treatment, food or chemical production, or medical treatment. Background technique [0002] Separation membranes (also called porous membranes) are used for filtration in various fields such as water treatment fields such as water purification and waste water treatment, medical applications such as blood purification, and food industry fields. [0003] When filtration is performed, the pores of the separation membrane are blocked. If the clogging progresses, the filtration pressure will increase, so it will gradually become difficult to maintain the filtration amount. Therefore, a method of washing a separation membrane after performing a filtration operation for a certain period of time is disclosed. As the cleaning of the s...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01D71/32B01D63/02B01D65/02B01D69/00B01D69/02B01D69/08B01D69/12B01D71/34C02F1/44
CPCB01D69/02B01D69/08B01D69/12B01D71/34B01D69/087B01D67/0027B01D67/0088B01D2325/30B01D2325/28C02F1/444B01D2325/52B01D67/00113B01D63/031B01D65/02B01D65/08C02F1/44B01D69/1213B01D2325/20B01D2325/02
Inventor 志村俊花川正行岩井健太北出有木村将弘
Owner TORAY IND INC