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Method for manufacturing asymmetric polyvinlylidenefluoride hollow fiber membrane and hollow fiber membrane manufactured therefrom

A fiber membrane, asymmetric technology, used in fiber processing, rayon manufacturing, hollow filament manufacturing, etc., can solve problems such as low compatibility, achieve high porosity, high water permeability, and easy to prepare parameters.

Active Publication Date: 2016-05-04
爱科利态株式会社
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The disadvantages of PVDF hollow fiber membranes prepared according to the prior art are that they are symmetrical hollow fiber membranes with the same pore size and distribution inside and outside the hollow fibers, and long kneading zones when extruders are used for homogeneous mixing The device should be used to ensure sufficient stirring time in order to overcome the low compatibility between PVDF and diluent, and the reliability of kneading of PVDF and diluent should be ensured by, for example, dosing raw materials to the extruder
In addition, it is disadvantageous in that extraction must be performed by adding inorganic fine powder such as hydrophobic silica for effective mixing of diluents, and that stretching and shrinkage are necessary

Method used

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  • Method for manufacturing asymmetric polyvinlylidenefluoride hollow fiber membrane and hollow fiber membrane manufactured therefrom
  • Method for manufacturing asymmetric polyvinlylidenefluoride hollow fiber membrane and hollow fiber membrane manufactured therefrom
  • Method for manufacturing asymmetric polyvinlylidenefluoride hollow fiber membrane and hollow fiber membrane manufactured therefrom

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0085] Manufacturing of PVDF hollow fiber membrane

[0086] use for figure 2 The device shown in to prepare PVDF hollow fiber membrane precursors. The prepared PVDF hollow fiber membrane precursor is wound around a rectangular parallelepiped bobbin. Then, the wound PVDF hollow fiber membrane precursor is cut at the edge portion of the rectangular parallelepiped bobbin, and then the diluent is extracted from the cut PVDF hollow fiber membrane precursor by a solvent extraction method using ethanol as an extractant. After drying at 50°C for 2 hours, the PVDF hollow fiber membrane precursor passes through Figure 5 (a) The intermittent clamp drafting method shown draws 125%. Therefore, if necessary, the obtained PVDF hollow fiber membrane is heat-treated under tension. The details of the relevant equipment, operating conditions and composition of the raw materials are described in Table 1 and Table 2.

[0087] Table 1

[0088] Device

Operating conditions

Batch reactor

Mix at...

Embodiment 2

[0101] Evaluation Example 2: Surface evaluation of PVDF hollow fiber membrane

[0102] Scanning electron micrographs (SAERON, AIS2100) of the outer surface and inner surface of the PVDF hollow fiber membrane prepared from the PVDF hollow fiber membrane precursor prepared in Example 1 through diluent extraction and drafting Picture 12 Means in. in Picture 12 In the middle, the SEM image on the left is an image of the outer surface and the SEM image on the right is an image of the inner surface. From Picture 12 It can be seen that the outer surface of the PVDF hollow fiber membrane manufactured in Example 1 has a porous structure with small pores and low porosity, while the inner surface has a porous structure with large pores and high porosity. Therefore, it was confirmed that the PVDF hollow fiber membrane manufactured in Example 1 had an asymmetric structure.

Embodiment 3

[0103] Evaluation Example 3: Evaluation of physical properties of PVDF hollow fiber membranes

[0104] The tensile strength, average pore size, porosity, and water permeability of PVDF hollow fiber membranes manufactured in Example 1 and Comparative Example 1 were measured as described below. The results are shown in Table 3.

[0105] (Measurement of tensile strength)

[0106] The tensile strength is measured according to ASTM D2256.

[0107] (Measurement of average pore size and porosity)

[0108] The average pore size and porosity are measured as follows. After using a scanning electron microscope (FE-SEM, CarlZeissSupra55) to obtain an SEM image of the surface of the PVDF hollow fiber membrane, use an image analyzer (Image-ProPlus) to measure the average length of the long axis and the short axis of the hole from the SEM image to determine Average pore size. In addition, the porosity was determined by measuring the ratio of the apparent area of ​​the surface of the PVDF hollow fi...

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Abstract

The present invention relates to a method for manufacturing an asymmetric polyvinlylidenefluoride (PVDF) hollow fiber membrane, which enables effective mixing of PVDF and a diluent without using separate inorganic fine powder, such as silica; in which a PVDF hollow fiber membrane is manufactured using a thermally induced phase separation method having an advantage of allowing easy obtaining of a separation membrane of consistent quality due to a key factor in controlling the phase separation in the two-substance mixture system of the polymer and the diluent being temperature, which is a manufacturing variable that is relatively simple and easy to control; in which a technique is applied for producing a temperature difference between the outer and the inner surfaces of a PVDF hollow fiber, and therefore, finally an asymmetric structure is expressed in which the inner surface side and the outer surface side of the PVDF hollow fiber have mutually different pore sizes and distributions; and which, even when an extraction process and a drawing process are applied, achieves a higher tensile strength and a larger average pore size, and thus higher porosity and water permeability than conventional hollow fiber membranes, since inorganic fine powder is not included. The asymmetric PVDF hollow fiber membrane has a pore symmetry index, defined as the ratio between the pore area on the outer surface and the pore area on the inner surface, of 0.1-0.8 and has superior water permeability and tensile strength unlike a PVDF separation membrane manufactured by the existing method.

Description

Technical field [0001] This application claims priority for Korean Patent Application No. 10-2013-0064164 filed in the Republic of Korea on June 4, 2013, the disclosure of which is incorporated herein by reference. [0002] The present disclosure relates to an effective method of manufacturing asymmetric polyvinylidene fluoride (PVDF) hollow fiber membranes, thereby preparing particles of PVDF and diluents to enable PVDF to be made without additional use of inorganic fine powders such as silica. It is effectively mixed with the diluent, and the phase separation of PVDF and the diluent is thermally induced by providing a temperature difference between the inner surface and the outer surface of the hollow fiber during spinning, thereby realizing the inner surface side and the outer surface side of the hollow fiber Asymmetric structure with different pore size and distribution. The present disclosure also relates to an asymmetric PVDF hollow fiber membrane, which has a pore symmetry...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D69/08B01D71/34D01D5/24D01F1/08B29C48/05B29C48/10
CPCD01D5/247D01F1/08D01F6/12B01D69/08B01D69/087B01D71/34B01D2323/08B29B7/005B29B7/12B29B7/26B29B9/06B29B9/16B29C48/001B29C48/05B29C48/10B29C48/0018B29C48/0022B01D67/0018B29B9/12B29K2027/16B29K2105/04B29K2995/0068B29K2995/0077B29L2023/00B29L2031/755D01D5/24B01D2323/28B01D2325/022
Inventor 朴珉守金镇浩
Owner 爱科利态株式会社
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