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Manufacture of a filtration membrane

a filtration membrane and hollow fiber technology, applied in the field of membrane filtration, can solve the problems of major defects in the outer surface of the fiber, the formation of major defects in the inner and outer surfaces of the membrane, and the complex process of the membrane to manufacture, etc., to achieve the effect of easy production, good reproducibility and easy production

Inactive Publication Date: 2019-09-05
ABC MEMBRANES
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The patent describes a method for making a filtration membrane that is cost-effective and reproducible. The membrane made using this method is strong and efficient. This invention solves the problems of previous methods for making filtration membranes.

Problems solved by technology

But in reality, it is a complex process to manufacture a membrane because it is possible to obtain membranes that perform very differently, from a same formulation (collodion).
When producing a hollow fiber through an extrusion spinneret, the surface state of the centering needle and, more importantly, the surface state of the extrusion orifice can cause the formation of major defects in its inner and outer surface.
In contrast, it has been noted that an even slightly degraded surface of the extrusion orifice can cause major defects in the outer surface of the fiber.
The presence of the slightest defect on the inner perimeter of the extrusion orifice of a spinneret can therefore significantly impact the quality of the surface of the nascent fiber.
In fact, the swelling which occurs in the nascent fiber increases the impact of existing defects on the perimeter of the extrusion orifice.
It is difficult to change the manufacturing conditions to minimize the impact of the surface state of the spinneret on the defects formed on the outer surface of the fiber.
Generally, the extrusion spinneret must be changed, which considerably increases the manufacturing cost of the membranes.
The outer surface of a hollow fiber or the active surface of a flat membrane is often damaged by the presence of scratches or burrs on the face of the advancement means which come into contact with them.
The membranes so produced have a semicrystalline structure, which can accelerate their aging and thereby limit their attraction.
Depending on the surface state of the rollers and on the draw conditions imposed, the fiber may suffer damage which can be very significant.
Observations made by scanning electron microscopy have shown that the outer surface of a fiber or the active surface of a flat membrane is very often damaged: indentations, marks, and tears are present on a regular basis.
These major defects affect the retention performance of membranes produced in this manner.
Experience has shown that these defects are the cause of accelerated chemical, mechanical, or thermal aging of membranes.
However, the presence of this dual filtration barrier results in poor hydraulic performance.
In addition, as previously indicated, the presence of numerous advancement means creates surface defects that can degrade the separation performance of the outer skin of the membrane.
This then results in the formation of hollow fibers which have attractive water permeabilities but poor selectivity performance.
Often these collodions also contain microgels which are the cause of many defects affecting selectivity and accelerating the chemical, thermal, and mechanical aging of the membranes so produced.
However, the spinning speeds are limited with such collodions.
To maintain production capacity, we must therefore increase the number of fibers produced in parallel, which intensifies spinning difficulties and gives rise to additional problems.
In addition, flat and hollow fiber membranes produced with an identical formulation did not provide the same hydraulic performance.

Method used

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  • Manufacture of a filtration membrane
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  • Manufacture of a filtration membrane

Examples

Experimental program
Comparison scheme
Effect test

example 1

Based on Polyethersulfone (PES)

[0057]A spin assembly as shown in FIG. 1 can be used for the production of conventional filtration membranes by extrusion. Such an assembly comprises a tank of collodion 1 and a tank of internal liquid 2, both connected to an extrusion spinneret 3 that allows forming a nascent fiber. This nascent fiber falls into a precipitation bath 4 and, by means of take-up rollers 4b is, is guided toward a rinsing bay 5 and a bundling machine 6 which is used to roll it. For experimental spinning, the bundling machine 6 is not used and the nascent fiber falls directly into a basin of water extending to the exit from the large roller of the rinsing bay 5, which advances it forward.

[0058]To manufacture conventional membranes based on polyethersulphone (PES), collodion can be prepared from a polymer mixture containing 16% Veradel 3100P polyethersulfone in the presence of 6% polyvinylpyrrolidone K30 in N-methylpyrrolidone, while stirring and at a temperature maintained ...

example 2

Based on Polyacrylonitrile (PAN)

[0085]To manufacture conventional membranes based on polyacrylonitrile (PAN), a polymer (collodion) mixture is prepared containing 18% polyacrylonitrile in the presence of 2% lithium chloride in N-methylpyrrolidone, while stirring at a temperature maintained at 70° C.

[0086]The collodion is then filtered through a wire mesh (5 micron filtration rating) and transferred to a storage tank where it is vacuum-degassed and then stored at a temperature of 40° C.

[0087]The precipitation liquid is water, degassed by ultrasound and then stored prior to use in a tank maintained at 40° C.

[0088]The hollow fiber is produced with the collodion and internal fluid at a temperature of 40° C. A specific extrusion spinneret is used to produce a fiber having an inner diameter of 0.90 mm and an outer diameter of 1.62 mm.

[0089]The spinning speed used is 18 m / min.

[0090]The external rinsing bath is filled with water maintained at 40° C. The fiber exiting the bath is advanced by...

example 3

n Modules

[0107]The table below gives the filtration areas that can be provided by a filtration module manufactured according to the invention, having an inner diameter of 300 mm and an effective filtration length equal to 1,200 mm. Three configurations of membranes of the invention are considered:

[0108]1—A membrane 15 as illustrated inFIG. 6, having a single series of thirty-three channels 16 (Series 1) placed between two layers of support film 17 measuring 1.5 mm in total thickness, which is a bonding area of 1.5×40 mm. This membrane is suitable for all potential cut-offs, from microfiltration to nanofiltration.

[0109]2—A membrane 15 as illustrated in FIG. 7, having two series of thirty channels 16 (Series 2) placed between two layers of support film 17 measuring 2.7 mm in total thickness, which is a bonding area equal to 2.7×40 mm. This membrane is more suitable for high ultrafiltration, ultrafiltration, or nanofiltration applications.

[0110]3-. A membrane 15 as illustrated in FIG. ...

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Abstract

A filtration membrane made by a method that includes: a) selecting and preparing an organic polymer, such as a collodion; b) injecting a collodion into at least one channel of an extrusion die that also comprises an extrusion die core and at least one outlet; c) injecting an internal liquid into a hollow centering pin, the hollow centering pin comprising a channel positioned on the core of the extrusion die and also positioned at an axis of the outlet of the extrusion die; d) applying a holding film to the outlet of the extrusion die; e) unrolling the holding film onto a surface of at least one hollow fiber emerging from the outlet of the extrusion die; f) immersing the hollow fiber with the first holding film in a rinsing solution so as to obtain a flat hollow fiber filtration membrane; and ending the rinsing of the filtration membrane.

Description

TECHNICAL FIELD[0001]The present invention relates to the field of membrane filtration and more particularly to the manufacture of a hollow fiber filtration membrane associated with a support film.TECHNICAL BACKGROUND[0002]An important aspect of the manufacture of this type of membrane is related to the quality of the inner and outer surfaces of the hollow fibers and the fragility of the resulting membranes. Therefore, a method is usually used that includes particularly delicate steps in order to avoid mechanical stress and physical damage to the membranes.PRIOR ART[0003]The manufacture of organic membranes is based on the principles of phase separation (dry, wet, thermal) or foaming, and even irradiation followed by appropriate chemical treatment(s). The steps in manufacturing a membrane produced according to the principle of liquid-liquid phase separation are seemingly simple. But in reality, it is a complex process to manufacture a membrane because it is possible to obtain membra...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01D69/08B01D69/10B01D71/42B01D71/68B01D63/02
CPCB01D69/087B01D69/10B01D71/42B01D71/68B01D63/021B01D2323/08B01D69/081B01D69/02B01D2325/28B01D2325/04B01D63/02B01D69/0871B01D69/1071B01D71/421B01D63/0233
Inventor ABIDINE, NOUHAD
Owner ABC MEMBRANES
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