CN87106024A - The preparation method of reclaimed cellulosic porous membrane - Google Patents
The preparation method of reclaimed cellulosic porous membrane Download PDFInfo
- Publication number
- CN87106024A CN87106024A CN87106024.8A CN87106024A CN87106024A CN 87106024 A CN87106024 A CN 87106024A CN 87106024 A CN87106024 A CN 87106024A CN 87106024 A CN87106024 A CN 87106024A
- Authority
- CN
- China
- Prior art keywords
- peptizer
- film
- water
- porous membrane
- cellulose solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Manufacture Of Macromolecular Shaped Articles (AREA)
- External Artificial Organs (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
The invention discloses the several method of preparation reclaimed cellulosic porous membrane.Adopt cotton, Mierocrystalline cellulose, sulphate cellulose (M η=0.77~20 * 10
4) cadmium ethylenediamine, cupri ethylene diamine, cuprammonium or Paraformaldehyde 96/dimethyl sulphoxide solution, prepared the Hydrophilized porous membrane of a series of mean pore sizes with casting method from 20-400 , but these film organic solvent-resistants, obdurability is better.The semi-permeable membranes that is used as membrane osmometer has selects perviousness preferably, can reach osmotic equilibrium rapidly.It is better to be used for the different sized molecules effects of polymers soln ultra-filtration and separation.They also can be used as dialysis tubing, the separation under low temperature or room temperature of various polymkeric substance or microbial solution, concentrate, medical macromolecular materials such as purification film and artificial kidney, pancreas.
Description
Reclaimed cellulosic porous membrane belongs to a kind of important novel material-functional membrane in the field of fine chemical, is typical hydrophilic film.
Since the seventies, the functional membrane development is very rapid, and principal item has soluble cotton, cellulose acetate, mixed cellulose ester, polymeric amide, tetrafluoroethylene, polyvinyl chloride, regenerated cellulose etc.In recent years, various countries are more to the research of good comprehensive properties regenerated cellulose film, Soviet Union certificate of invention Su, 1047 928(1983), the clear 56-24008(1981 of day disclosure special permission communique), clear 58-89625(1983), West Germany's monograph 3002438(1980) mention respectively with copper ammon solution and prepare regenerated cellulose film or artificial silk.French Patent N
08106153(1981), day clear 60-187307(1985 of disclosure special permission communique) all mention with organic solvent such as LiCl/N-methyl-2-pyrrolidone, LiCl/ N,N-DIMETHYLACETAMIDE, formulations prepared from solutions regenerated cellulose films such as Paraformaldehyde 96/dimethyl sulfoxide (DMSO).Soviet Union magazine Ж П Х 41(10) 1968 mention with cadmium ethylenediamine formulations prepared from solutions regenerated cellulose film, industrial of famous Japanese Asahi Chemical Industry fiber research adopts the copper ammon solution that contains other positively charged ion and solvent to prepare various regenerated cellulose films.It is substantial different that the present invention and above-mentioned prior art have, and proposed the novel method of preparation reclaimed cellulosic porous membrane.
Main points of the present invention are that Mierocrystalline cellulose can be dissolved in some metal ion complex solvent with complex form, also can be dissolved in to contain N
2O
4, LiCl or Paraformaldehyde 96 several organic solvent systems.In Paraformaldehyde 96/dimethyl sulfoxide solvent, the primary hydroxyl methylolation on 6 of the Mierocrystalline celluloses, thus dissolving forms cellulose solution.
According to membrane formation mechanism, as cellulosic solvent, more be poor solvent, can promote crystallite to form more, so key problem in technology is to solidify the preceding solubleness that reduces cellulose solution.Comparatively freezing film helps its regularity under the demulcent condition, peptizer should be able to dissolve each other with cellulosic solvent and don't make cellulose dissolution, select the mixed solvent of organic solvent or organic solvent to make peptizer, the cellulose complex compound structure can not only be destroyed effectively and process of setting relatively relaxes, simultaneously, organic solvent is easy to reclaim by distillation.
Mierocrystalline cellulose cadmium ethylenediamine solution is more stable than copper ammon solution, and the content of its solvability and CdO and quadrol has substantial connection.As CdO: quadrol: water=7.4: 27: in the time of the 65.6(weight ratio), it have very strong dissolving power to fiber, and reduces with temperature and to increase.This solvent is placed certain hour in air after, owing to the quadrol volatilization causes that change of component becomes poor solvent.This cellulose solution is the alkali salt complex compound, so diluted acid, and organic acid, organic solvent and mixes with small amount of water solvent or alcohol can be used as peptizer.Behind the film coagulation forming, can improve its transparency carrying out drying treatment below 70 ℃; But the mean pore size of film can reduce 6-7 doubly.
Paraformaldehyde 96 in fibrination polyoxymethylene/dimethyl sulphoxide solution need be removed with high temperature (more than 100 ℃) gasification,, all will heat-treat before and after solidifying for this reason.Alcohols, organic solvents such as tetrahydrofuran (THF) can be used as peptizer.When making peptizer with alcohol, the film mean pore size increases with pure carbon atom number.Table 1 illustrates with the different influences to permeability with its peptizer under the filming condition of a kind of prescription.In addition, this film is better to solvent adaptability, when they use as the semi-permeable membranes of permeameter, converts toluene solvant to from dimethyl formamide, adapts to after 2 hours, with dynamic osmometry mensuration polystyrene standards (M
n=41.56 * 10
4, Japanese Japan Cao Da) number-average molecular weight, measurement result M
n=42.2 * 10
4Coincide with set-point, and osmotic pressure discrepancy in elevation H is fine to the linear relationship of volumetric flow rate (dv)/(dt) mapping.They also have higher low molecular retention rate than the similar film RC52 of the U.S..
Cuprammonium or cupri ethylene diamine solvent be dissolving cellulos comparatively fast, because their easy oxidative degradation, so must add antioxygen such as Na
2SO
3, sucrose.When adopting the 10%NaOH aqueous solution to make peptizer, film shrinks terrible, is generally about 60%, adopts organic solvent then can obviously reduce shrinking percentage as peptizer, in 5%.Using 87% dimethyl formamide/11% water, 2% quadrol to make peptizer, to obtain shrinkability little, the film that obdurability is good.
Table 1
Peptizer methanol Virahol n-Octanol
Perviousness is in the dimethyl formamide 0.87 2.66 4.88 29.7
G×10
13/cm
3sg
-1
Porosity/% 53 50 56 50
With method for preparing the aperture from 20
To 400
Various apertures reclaimed cellulosic porous membrane.The strong Firmware of these films, organic solvent such as ability tetrahydrofuran (THF), toluene, ketone, alcohols, dimethyl methyl methane amide and diluted acid, dilute alkaline aqueous solution.They have selective permeation speed preferably.Separate as semi-permeable membranes in the membrane osmometer and polymkeric substance, spissated ultra-filtration membrane all obtains effect preferably.They also can be used as dialysis tubing, various polymkeric substance or microbial solution low temperature, room temperature condition separate down, concentrated, purification film, medical macromolecular materials such as artificial kidney or pancreas, use cheap timber, agricultural-product (bagasse, Pericarppium arachidis hypogaeae) is made broad-spectrum functional membrane and is had higher economic worth.
One of embodiments of the invention are, the 110ml quadrol is dissolved in the 240ml water, add 27g Cdo and stirred 1 hour under 0 ℃ of condition, obtain water white transparency cadmium ethylenediamine solution, store standby down at 0 °-5 ℃.
1g Mierocrystalline cellulose (M
η=16.6 * 10
4) and 1g cotton (M
η=20 * 10
4) be dissolved in the 60ml cadmium ethylenediamine solution, stir under 0-5 ℃ and became transparent thick liquid in 30 minutes, after filtration, after the degassing, with two ends is Glass tubing knifing on sheet glass that copper wire (diameter 0.3mm) is arranged, and places 1 hour under 30 ℃ of conditions in Fume Hoods, puts in the peptizer then, film is peeled off from sheet glass naturally about 1 hour, successively at 4% sulfuric acid, plasticising in 20% glycerine is kept in 20% Virahol/2% formalin at last after the water flushing.After oven dry under 70 ℃ of conditions, the film mean pore size is by 140
Reduce to 20
As having of above-mentioned peptizer: 10% acetic acid, 80% dimethyl formamide/18% water/2% quadrol, 90% ethanol or methyl alcohol.
Two of embodiments of the invention are: 6g sulphate cellulose (M
η=1.9 * 10
4Be dissolved in the 220ml dimethyl sulfoxide (DMSO), with the 3g cotton at N
2110 ℃ were heated 3 hours in the gas, add the 28g Paraformaldehyde 96 again, continue stirring down at 115 ℃ and made dissolving in 2 hours, after filtration, carry out knifing (thickness 1mm) after the degassing, again successively at 100 ℃ of hot air driers, placed respectively in the room temperature Fume Hoods 20 minutes, put into then in the peptizer more than 2 hours, take out the back on 60 ℃ of flat boards dry 3 hours, plasticising and boil film is peeled off in 20% aqueous glycerin solution at last has organic solvents such as methyl alcohol, ethanol, Virahol, n-Octanol as above-mentioned peptizer.
Three of embodiments of the invention are, 2g Mierocrystalline cellulose and 2g cotton be dissolved in the 50g cupri ethylene diamine (mol ratio is a copper: quadrol: water=1.2: 2.3: 45) and the 50g cuprammonium (mol ratio is a copper: ammonia: in mixed solvent water=0.4: 4.5: 45), add 0.8g Na
2SO
3Cellulose solution after filtration, the degassing after, knifing on sheet glass (thickness 0.25mm), in Fume Hoods, placed 1 hour under 30 ℃ of conditions again, put into then in the solidification liquid to blue decoloration, again successively at 10% acetic acid, placed respectively in 4% aqueous sulfuric acid 10 minutes, and washed back plasticising 1 hour in 20% aqueous glycerin solution, be kept in 20% Virahol/2% formalin.As above-mentioned peptizer 87% dimethyl formamide/11% water/2% quadrol, 95% ethanol etc. are arranged.
Claims (3)
1, a kind of preparation method of reclaimed cellulosic porous membrane is characterized in that:
1.1 in weight ratio is CdO: quadrol: dissolving cellulos in the cadmium ethylenediamine solvent of water=7.4: 27: 65.6;
1.2 above-mentioned cellulose solution is delayed at dull and stereotyped upper reaches under 30 ℃ of ventilation conditions and placed 1 hour, puts into and carries out coagulation forming in the peptizer, said peptizer is 10% acetic acid, 80% dimethyl formamide/18% water/2% quadrol, 95% ethanol or methyl alcohol;
2, a kind of preparation method of reclaimed cellulosic porous membrane is characterized in that:
2.1 dissolving cellulos in 12.7g Paraformaldehyde 96 and 100ml dimethyl sulfoxide (DMSO) mixed solvent;
2.2 above-mentioned cellulose solution is delayed at dull and stereotyped upper reaches, place 100 ℃ of hot air driers successively, placed respectively in the room temperature Fume Hoods 20 minutes, put into and carry out freezing film in the peptizer, said peptizer is a methyl alcohol, ethanol, Virahol or n-Octanol, to with a kind of prescription, the carbon atom number of alcohol reduces to 1 from 8, and the film mean pore size reduces to 20 from 122
;
2.3 behind the cellulose solution freezing film, under 60-70 ℃ of condition, put in 20% glycerine plasticising after the aftertreatment again and boil film is peeled off.
3, a kind of preparation method of reclaimed cellulosic porous membrane is characterized in that:
3.1 cupri ethylene diamine (mol ratio is a copper: quadrol: water=1.2: 2.2: 45) and cuprammonium (mol ratio is a copper: ammonia: dissolving cellulos in the mixed solvent (1: 1) water=0.4: 4.5: 45);
3.2 above-mentioned cellulose solution is delayed at dull and stereotyped upper reaches, places 1 hour under 30 ℃ of ventilation conditions, puts into peptizer then and carries out coagulation forming, said peptizer is 87% dimethyl formamide/11% water/2% quadrol;
3.3 behind the cellulose solution freezing film, successively in 10% acetic acid, placed 15 minutes in 4% aqueous sulfuric acid, water is rinsed well then, is kept in 20% Virahol/2% formalin.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN87106024.8A CN1004050B (en) | 1987-08-28 | 1987-08-28 | Method for preparing reclaimed cellulosic porous membrane |
CN 88103036 CN1009901B (en) | 1987-08-28 | 1987-08-28 | Prepn. of reganerated cellulose porous membrane by copper amonia method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN87106024.8A CN1004050B (en) | 1987-08-28 | 1987-08-28 | Method for preparing reclaimed cellulosic porous membrane |
Related Child Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 88103036 Division CN1009901B (en) | 1987-08-28 | 1987-08-28 | Prepn. of reganerated cellulose porous membrane by copper amonia method |
CN 88103035 Division CN1037842A (en) | 1988-05-20 | 1988-05-20 | Organic solvent method for preparing regenerated cellulose porous membrane |
Publications (2)
Publication Number | Publication Date |
---|---|
CN87106024A true CN87106024A (en) | 1988-04-06 |
CN1004050B CN1004050B (en) | 1989-05-03 |
Family
ID=4815548
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN87106024.8A Expired CN1004050B (en) | 1987-08-28 | 1987-08-28 | Method for preparing reclaimed cellulosic porous membrane |
CN 88103036 Expired CN1009901B (en) | 1987-08-28 | 1987-08-28 | Prepn. of reganerated cellulose porous membrane by copper amonia method |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 88103036 Expired CN1009901B (en) | 1987-08-28 | 1987-08-28 | Prepn. of reganerated cellulose porous membrane by copper amonia method |
Country Status (1)
Country | Link |
---|---|
CN (2) | CN1004050B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105597551A (en) * | 2015-10-16 | 2016-05-25 | 福建农林大学 | Production method of regenerated cellulose nanofiltration membrane |
CN108602026A (en) * | 2016-03-31 | 2018-09-28 | 旭化成医疗株式会社 | Remove the manufacturing method of the film of virus and the film of removal virus |
CN113600146A (en) * | 2021-07-26 | 2021-11-05 | 武汉大学 | Iron-manganese composite membrane adsorbent, preparation method thereof and application thereof in adsorbing arsenic and cadmium in water and soil |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4980789B2 (en) * | 2006-06-05 | 2012-07-18 | レンゴー株式会社 | Total heat exchanger seat |
-
1987
- 1987-08-28 CN CN87106024.8A patent/CN1004050B/en not_active Expired
- 1987-08-28 CN CN 88103036 patent/CN1009901B/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105597551A (en) * | 2015-10-16 | 2016-05-25 | 福建农林大学 | Production method of regenerated cellulose nanofiltration membrane |
CN105597551B (en) * | 2015-10-16 | 2019-05-10 | 福建农林大学 | A kind of preparation method of regenerated cellulose nanofiltration membrane |
CN108602026A (en) * | 2016-03-31 | 2018-09-28 | 旭化成医疗株式会社 | Remove the manufacturing method of the film of virus and the film of removal virus |
CN108602026B (en) * | 2016-03-31 | 2021-12-28 | 旭化成医疗株式会社 | Virus-removing film and method for producing virus-removing film |
CN113600146A (en) * | 2021-07-26 | 2021-11-05 | 武汉大学 | Iron-manganese composite membrane adsorbent, preparation method thereof and application thereof in adsorbing arsenic and cadmium in water and soil |
CN113600146B (en) * | 2021-07-26 | 2022-07-29 | 武汉大学 | Iron-manganese composite membrane adsorbent, preparation method thereof and application thereof in adsorbing arsenic and cadmium in water and soil |
Also Published As
Publication number | Publication date |
---|---|
CN1009901B (en) | 1990-10-10 |
CN1037843A (en) | 1989-12-13 |
CN1004050B (en) | 1989-05-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103143269A (en) | Chitosan/cellulose composite separation membrane and preparation method thereof | |
CN103028331A (en) | Preparation method of hydroxyethyl cellulose-silicon dioxide pervaporation hybrid membrane | |
KR20110074201A (en) | Acetylated methyl cellulose, membrane for water treatment using that and preparing method thereof | |
CN105521715A (en) | Blend polyvinylidene fluoride hollow fiber film and making method thereof | |
EP0066408A2 (en) | Porous membrane | |
CN101721927B (en) | Ultrafiltration membrane copoly(phthalazinone aryl ether sulfone) and preparation method thereof | |
CN87106024A (en) | The preparation method of reclaimed cellulosic porous membrane | |
JPH03174231A (en) | Polyether ketone semi- permeable membrane | |
JPS6238205A (en) | Semi-permeable membrane for separation | |
CN103007783A (en) | Preparation method of cellulose ether-ethyl orthosilicate pervaporation hybrid membrane | |
JPS59103671A (en) | Membrane and production thereof | |
CN111495214A (en) | Method for improving performance of porous membrane through crosslinking | |
JPH0317532B2 (en) | ||
EP0146655A1 (en) | A process for separating mixtures of water and an organic compoundand a water-selective permeation membrane | |
CA1209764A (en) | Reverse osmosis membrane quenching | |
JPS62168503A (en) | Separation membrane | |
CN1037842A (en) | Organic solvent method for preparing regenerated cellulose porous membrane | |
CN108607372A (en) | A kind of preparation method and cellulose gas separation membrane of the cellulose gas separation membrane of ion doping | |
JPS6151928B2 (en) | ||
CN102861518A (en) | Preparation method of high polymerization degree polyvinyl chloride hollow fiber ultrafiltration membrane | |
JPS6139061B2 (en) | ||
CN116207314A (en) | Preparation method of polymer electrolyte membrane based on polymer solution modulation | |
KR870000757B1 (en) | Anionic polysaccaride separation membranes | |
JPH07121346B2 (en) | Selective permeable membrane | |
CA1255061A (en) | Separation membranes |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C13 | Decision | ||
GR02 | Examined patent application | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |