Preparation method of asymmetric hollow fiber membrane

A fiber membrane, asymmetric technology, applied in the field of membrane materials, can solve the problems of high cost of extraction time, long extraction time, and reduced economic benefits, and achieve the effect of large industrial practical value, shortened extraction time, and guaranteed economic benefits

Pending Publication Date: 2022-07-12
杭州费尔新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Most of the hollow fiber membranes currently used in oxygenators are asymmetric membranes, which include a separation layer and a support layer, wherein the support layer is located on the side of the hollow fiber membrane close to the inner cavity, and the separation layer is located on the side of the hollow fiber membrane away from the inner cavity ; The support layer has a high porosity, thereby ensuring that oxygen and carbon dioxide can pass through the hollow fiber membrane relatively freely, that is, the CO of the hollow fiber membrane 2 Mass transfer rate and O 2 The mass transfer rate is high; and the separation layer is a dense layer, that is, there are no holes on the surface and inside of the separation layer, which ensures that the hollow fiber membrane has a long plasma permeation time and a long service life; but in the preparation of the above hollow fiber membrane In the process, in order to remove the solvent system in the quenched membrane filament as much as possible, the R&D personnel often take a long extraction time, generally 12-24 hours, and the extraction time cost is too large, thus reducing the economic benefit; how to shorten the extraction time time, but also to ensure the quality of the extraction, so that the extract can completely remove the solvent system from the membrane filaments in a short period of time; Fibrous Membrane Development

Method used

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  • Preparation method of asymmetric hollow fiber membrane
  • Preparation method of asymmetric hollow fiber membrane
  • Preparation method of asymmetric hollow fiber membrane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] A preparation method of asymmetric hollow fiber membrane, comprising the following steps:

[0058] Step 1: Add the solvent system consisting of 41wt% compound A and 14wt% compound B and 45wt% poly(4-methyl-1-pentene) into a twin-screw extruder and stir and knead at 240°C to obtain a homogenous solution. Phase casting liquid; wherein compound A is dimethyl phthalate, and compound B is rapeseed oil;

[0059] Step 2: extruding the casting liquid from a die head with a temperature of 220°C to obtain a molded product with an inner surface and an outer surface;

[0060] Step 3: The molded product is immersed in a cooling liquid for phase separation and solidification, wherein the cooling liquid is the solvent system (solvent system composed of 41wt% dimethyl phthalate and 14wt% rapeseed oil) used in preparing the casting liquid, cooling The liquid temperature is 36°C, and the phase separation curing time is 55ms;

[0061] Step 4: then use the solvent system (solvent system ...

Embodiment 2

[0065] A preparation method of asymmetric hollow fiber membrane, comprising the following steps:

[0066] Step 1: Add a solvent system consisting of 30wt% compound A and 15wt% compound B and 55wt% poly(4-methyl-1-pentene) into a twin-screw extruder and stir and knead at 250°C to obtain a uniform solution. Phase casting liquid; wherein compound A is dehydrated castor oil fatty acid, and compound B is palm oil;

[0067] Step 2: extruding the casting liquid from a die head with a temperature of 225°C to obtain a molded product with an inner surface and an outer surface;

[0068] Step 3: Immerse the molded product in a cooling liquid for phase separation solidification, wherein the cooling liquid is compound A dehydrated castor oil fatty acid, the cooling liquid temperature is 41°C, and the phase separation solidification time is 66ms;

[0069] Step 4: Then use compound A dehydrated castor oil fatty acid as a quenching liquid to quench the molded product, the quenching temperatur...

Embodiment 3

[0073] A preparation method of asymmetric hollow fiber membrane, comprising the following steps:

[0074] Step 1: Add a solvent system consisting of 48wt% compound A and 12wt% compound B and 40wt% polypropylene into a twin-screw extruder and stir and knead at 235°C to obtain a homogeneous casting liquid; wherein compound A is Methyl-12-hydroxystearic acid, compound B is castor oil;

[0075] Step 2: extruding the casting liquid from a die head with a temperature of 220°C to obtain a molded product with an inner surface and an outer surface;

[0076] Step 3: the molded product is immersed in a cooling liquid for phase-separation solidification, wherein the cooling liquid is a solvent system (solvent system composed of 48wt% methyl-12-hydroxystearic acid and 12wt% castor oil) used when preparing the casting liquid, The coolant temperature is 29°C, and the phase-separated curing time is 47ms;

[0077] Step 4: Then use the solvent system (solvent system composed of 48wt% methyl-1...

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Abstract

The invention provides a preparation method of an asymmetric hollow fiber membrane, which comprises the following steps: preparing a membrane casting solution, and extruding the membrane casting solution into a molded product through a die head, performing split-phase curing on the molded product, and performing quenching treatment to obtain a green film; then extracting a solvent system in the green film by using an extracting solution at the extraction temperature of 40-80 DEG C and the concentration of the extracting solution in the extraction process is not lower than 90%, so that the solvent system can be removed from the green film only by 1-4 hours; performing low-temperature drying and high-temperature shaping on the original membrane to obtain a hollow fiber membrane; according to the method, in the process of preparing the hollow fiber membrane, the extraction time can be shortened, and the extraction quality can be ensured, so that a solvent system can be completely removed from membrane filaments by the extract liquor within a relatively short time, and the economic benefit is ensured; meanwhile, it can be guaranteed that the finally prepared hollow fiber membrane has long plasma permeation time, and the plasma permeation time is at least 48 h; and the membrane also has high gas mass transfer rate and large mechanical properties, and is especially suitable for being used as a blood oxygenation membrane.

Description

technical field [0001] The invention relates to the technical field of membrane materials, in particular to a preparation method of an asymmetric hollow fiber membrane. Background technique [0002] In many applications in the fields of chemistry, biochemistry or medicine, there is the problem of separating gaseous components from liquids or adding these components to liquids. For these gas exchange processes, membranes are increasingly used as separation membranes between various liquids and fluids that adsorb or release gaseous components from which gaseous components are separated or added. The fluid here can be a gas or a liquid containing or adsorbing the gas components to be exchanged. Using such membranes, an exchange surface can be provided for gas exchange and, if necessary, direct contact between liquid and fluid can be avoided. [0003] An important application of membrane-based gas exchange methods in the medical field is oxygenators, also called artificial lun...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D67/00B01D69/02B01D69/08B01D69/10
CPCB01D67/0011B01D67/0083B01D67/0093B01D69/02B01D69/08B01D69/10B01D2325/022Y02C20/40
Inventor 贾建东陈梦泽潘哲
Owner 杭州费尔新材料有限公司
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