CN1635002A - Process for preparing high hydroscopicity resin from polyacrylonitrile powder - Google Patents
Process for preparing high hydroscopicity resin from polyacrylonitrile powder Download PDFInfo
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Abstract
A process for producing high water absorption resin using polyacrylonitrile powder is provided. In the process, polyacrylonitrile powder, water, alcohols compound and hydrolytic reagent are heated up to a temperature under stirring action and dispersive hydrolytic reaction is carried out. After the hydrolytic reaction, the resin product is filtered out and dried, and the powdered or granular product is obtained. The water absorbing multiple and salt tolerance of the product can be improved greatly.
Description
Technical field
The present invention relates to field of polymer technology, particularly relate to and a kind ofly prepare the processing method of super absorbent resin with the polyacrylonitrile powder, the super absorbent resin for preparing is applicable to every field such as physiological hygiene, agricultural gardening, petrochemical complex, Oil extraction, building, papermaking, weaving, printing and dyeing and water-proof material.
Background technology
Super absorbent resin is a kind of functional high molecule material that has wide range of applications, and can be used for many fields such as oil, chemical industry, building, oil field, physiology, medical treatment and agricultural gardening.Just preparation method's classification of super absorbent resin mainly comprises natural polymer graft type (as starch-grafted vinyl cyanide) and monomer synthesis type two big classes, and wherein the synthesis type super absorbent resin occupies dominant position owing to characteristics such as having anti-enzyme.The polymerization single polymerization monomer that adopts in the synthesis type super absorbent resin is generally vinylformic acid (sometimes with the acrylamide copolymerization).In general, this super absorbent resin has cross-linked structure owing to add difunctionality (or polyfunctionality) linking agent in polymerization process, thereby has high suction multiple.Also can adopt acrylonitrile monemer to aggregate into polyacrylonitrile in addition, reaction then is hydrolyzed, hydrophobic groups such as the itrile group in the molecular chain are hydrolyzed into hydrophilic carboxyl (or carboxylate salt) and amide group etc., also can obtain cross-linked structure and have higher water absorbing properties when linking agent exists.These products all reach the suction purpose by having the space cross-linked structure.The crosslinking sodium polyacrylate super absorbent resin can absorb self tens, the water (being generally deionized water) of hundreds of even several thousand times, and have only when absorbing saline media such as physiological saline its suction multiple 1/10th in addition lower, this illustrates that its salt tolerance is relatively poor, and most application scenarios are saline medias, and this just makes its application be subjected to certain limitation.
U.S. Pat 5496890 discloses a kind of super absorbent resin preparation method, the high-molecular weight polyacrylonitrile that letex polymerization is obtained carries out partial hydrolysis, under the situation that does not add linking agent, obtain the product of high-hydroscopicity energy by the effect of hydrophobic grouping and hydrophilic radical, the highest suction multiple of this super absorbent resin can reach 1000 times, inhales the physiological saline multiple and can reach 90 times.This preparation technology requires to adopt the high molecular weight polypropylene nitrile of emulsion polymerization prepared, the product that adopts suspension method (aqueous phase precipitation method) preparation in the general acrylic fibers industry then since molecular weight be dissolved in water behind the low in hydrolysis very much and do not have water absorbing properties.
Summary of the invention
Technical problem to be solved by this invention mainly provides a kind of method of utilizing the super absorbent resin of polyacrylonitrile powder preparation suction multiple height, good salt tolerance.The present invention also aims to fully utilize the super absorbent resin product of waste acrylic dry powder production high added value.
The present invention produces the method for super absorbent resin with the polyacrylonitrile powder, it is characterized in that polyacrylonitrile powder, water, alcohol compound, hydrolytic reagent are warmed up to certain temperature carries out dispersed hydrolysis reaction under stirring action, hydrolysis reaction finishes after-filtration and goes out rosin products, drying obtains powder or granular product, described alcohol compound is to contain a monohydroxy-alcohol to eight carbon atoms, hydrolytic reagent is a strongly alkaline compound, hydrolysis temperature is the azeotropic point temperature of the complex reaction medium formed of alcohol compound and water, or is higher than 50 ℃ and is lower than the azeotropic point temperature.
The present invention carries out controlled partial hydrolysis reaction to the polyacrylonitrile powder in the specific reaction medium that alcohol and water is formed, obtain containing the multipolymer of multiple hydrophilic radicals such as amide group, carboxyl, ester group, the synergy of above-mentioned group makes the suction multiple of product improve greatly, especially the existence of the amide group of non-ionic type, ester group makes the salt tolerance of super absorbent resin improve greatly, can satisfy the needs of multiple Application Areas.Moreover, adopt common acid system or alkali process to carry out the hydrolysis reaction of polyacrylonitrile, owing to reaction viscosity greatly, is easily reeled off raw silk from cocoons and is not easy to handle and dry the energy consumption for drying height.Carry out dispersed hydrolysis reaction and adopt among the present invention at specific reaction medium, because solid materials all is not dissolved in reaction medium before and after the hydrolysis, thereby solid phase and liquid phase are easily separated, obtain a kind of even-grained product at last, and the particle diameter of product can be regulated, handle with dry convenient, energy consumption for drying reduces greatly, also satisfies the demand of different application field to product form simultaneously easily.
Below describe method of the present invention and optimized technical scheme in detail:
Synthesizing of polyacrylonitrile powder: the present invention adopts acrylonitrile polymerization to become the polyacrylonitrile powder to make the reaction raw materials of dispersed hydrolysis, it can be the acrylonitrile homopolymer that emulsion method or suspension polymerization become, can be that high molecular weight products also can be lower or even the product of molecular weight distribution broad such as the useless dry powder of acrylic fibers of dry acrylic fiber device product of molecular weight, also can be vinyl cyanide and other monomers such as methyl acrylate, ethyl propenoate, butyl acrylate, methyl methacrylate, Jia Jibingxisuanyizhi, butyl methacrylate, the multipolymer of acrylate co-monomers such as vinyl-acetic ester.The Mn that the molecular weight ranges of polymkeric substance can be about 30,000 from the number-average molecular weight Mn of dry acrylic fiber handicraft product, the Mn of wet spinning acrylic fiber handicraft product is about 100,000 high molecular weight products that obtain to emulsion polymerization is up to hundreds of thousands of even higher, be included in the dry acrylic fiber technology from the molecular weight of the fallen portion of hot degraded of dryer be lower than 30,000 and also the useless dry powder of molecular weight distribution broad also meet the demands.The particle diameter of powder can be from about hundreds of nm of emulsion method product to the suspension method product tens μ m.Emulsion polymerization synthetic macromolecule weight polyacrylonitrile powder adopts ordinary emulsion polymerization techniques such as peroxide initiator and Sulfonates anionic emulsifier to obtain.
Especially it is emphasized that the present invention can adopt the acrylic fibers device, especially the waste acrylic dry powder of dry acrylic fiber device generation is made the feedstock production super absorbent resin, and this obviously is to adopt the method for common hydrolysis process and don't adding linking agent to realize.As everyone knows, the dry acrylic fiber production technique is in the drying process of polymkeric substance, and powder unavoidably is scattered from the transport tape of loft drier, generally wants periodic cleaning in case the generation of electrostatic accident.The useless dry powder of the polymkeric substance that cleaning produces generally no longer is used as the raw material of spinning owing to long high temperature drying may cause reasons such as molecular degradation.These waste materials can not be hot-forming because can not natural degradation, can not be used as fuel, and environment protection is caused totally unfavorable influence.Adopt waste acrylic to produce super absorbent resin, can fully utilize waste acrylic on the one hand, turn waste into wealth, three-waste free discharge in the production process is a kind of environmentally friendly green chemistry process; On the other hand, greatly reduce the production cost of super absorbent resin again, can be described as a processing method that makes the best of both worlds.The raw material (mainly being vinyl cyanide) of producing acrylic fibers is from subterranean oil, after human processing, utilizing, consume, after adopting this art breading to obtain super absorbent resin, get back to underground promotion agricultural development if be used for water-loss reducer of soil recirculation, we can say real realized resource circulation utilization and Sustainable development.Therefore, utilize the super absorbent resin of waste acrylic production high added value, coproduction super absorbent resin on the acrylic fibers device has so just significantly reduced plant investment and energy consumption, material consumption etc., has good economic benefit and remarkable social benefit.
Dispersed hydrolysis reaction: polyacrylonitrile powder, water, alcohol compound, hydrolytic reagent adding are equipped with in the reactor of stirring rake, reflux exchanger and thermometer, under stirring action, are warmed up to certain temperature and carry out dispersed hydrolysis reaction.Above-mentioned alcohol compound is to contain a monohydroxy-alcohol to eight carbon atoms, as methyl alcohol, ethanol, n-propyl alcohol, Virahol, propyl carbinol, isopropylcarbinol, sec-butyl alcohol, Pentyl alcohol, primary isoamyl alcohol, tertiary amyl alcohol, neopentyl alcohol, n-hexyl alcohol, n-Heptyl alcohol, n-Octanol etc., can be a kind of in the above-mentioned alcohol compound, two or more is shared.Hydrolytic reagent is a strongly alkaline compound, comprise alkali metal hydroxide, alkali metal alcohol compound, basic metal ammoniate, as sodium hydroxide, potassium hydroxide, sodium ethylate, potassium ethylate and ammonia sodium etc., can be a kind of in the above-mentioned alcohol compound, two or more is shared.Hydrolysis temperature generally adopts the azeotropic point temperature of the complex reaction medium of alcohol compound and water composition, also can adopt to be higher than 50 ℃ of temperature of reaction that are lower than the azeotropic point temperature.Hydrolysis time is 0.5-24 hour, preferred 1-12 hour.Water is 1-40 with the volume ratio of alcohol: 100, and preferred 5-25: 100; The weight ratio of hydrolytic reagent and polyacrylonitrile powder is 1-100: 100, and preferred 5-50: 100; The liquid reaction medium weight ratio that polyacrylonitrile solid powder and alcohol and water are formed is 1-100: 100, and preferred 10-60: 100.
Hydrolysis reaction filters out rosin products after finishing, and drying obtains powder or granular product, and the reaction medium that filters out can reuse.
Preferably under agitation carry out in the hydrolytic process among the present invention, reaction system is mixed, prevent the solid materials precipitation, can not make mixing speed too fast again, solids are smashed.
The super absorbent resin product of producing according to method of the present invention is faint yellow or white powder or particle, suction multiple (deionized water) 100～3000 times, inhale physiological saline (the 0.9%NaCl aqueous solution) 10～180 times, this resin rate of water absorption is fast, the suction multiple has higher intensity less than the hydrogel of 800 times resin suction back formation, water retention property is good, good salt tolerance.The super absorbent resin uniform particles that the inventive method obtains.Method raw material of the present invention is cheap and easy to get, technology is simple, environmental, easy to utilize.
Super absorbent resin suction multiple is meant the weight of a gram deionized water that super absorbent resin absorbs among the present invention, inhales the weight that the physiological saline multiple generally is meant the gram 0.9%NaCl aqueous solution that super absorbent resin absorbed.Measuring method adopts filtration method, at room temperature accurately weighing 0.100-1.000g super absorbent resin adds in the beaker, add weighing 100-500ml deionized water (10～100ml physiological saline) then, stir with glass stick, placed 24 hours, slowly add in the stainless (steel) wire then hydrogel, normal pressure filters out unabsorbed free water, leave standstill for some time after the filtration, weighing absorbs the quality of surplus water (physiological saline), calculates suction multiple (inhaling the physiological saline multiple).
Embodiment
The present invention is described by the following examples, but does not limit the present invention.
Embodiment 1
Add polyacrylonitrile powder (dry acrylic fiber handicraft product at the 500ml four-hole boiling flask that agitator, reflux exchanger and thermometer are housed, Mn is about 30,000) 40g, solid sodium hydroxide 20g, deionized water 20ml, isopropylcarbinol 200ml, start and stir, beginning slowly heats up, and is warmed up to about 95 ℃, and material comes to life.Hydrolysis reaction is 6 hours under boiling state, the cooling stopped reaction.Filter out solid materials, obtain evengranular colourless or faint yellow granulated product after the drying, granularity is about 200-300 μ m.The suction multiple of product is 2400 times, and inhaling the physiological saline multiple is 160 times.
Comparative Examples 1
Working method is with embodiment 1, and difference is that the deionized water that adds is 220ml, does not add isopropylcarbinol.Hydrolysis reaction obtained light yellow viscous liquid after 6 hours, can't filter, and in deionized water and the physiological saline, suction multiple and suction salt solution multiple are 0 times behind the product drying.
Comparative Examples 2
Working method is with embodiment 1, and difference is that the isopropylcarbinol that adds is 220ml, does not add deionized water.The product that obtains is yellow fine powder, meets water and does not dissolve insoluble expanding.Suction multiple and suction salt solution multiple are 0 times.
Embodiment 2-4
Working method is with embodiment 1, and difference is the high molecular weight polypropylene nitrile homopolymer oven dry dry powder that useless dry powder, wet spinning acrylic fiber device oven dry dry powder, emulsion polymerization that the hydrolysis material that adopts is respectively the dry acrylic fiber device and produces obtain.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 2300 times, 2500 times and 3000 times.
Embodiment 5-10
Working method is with embodiment 1, and difference is that the alcohol compound that adds is respectively methyl alcohol, ethanol, Virahol, n-propyl alcohol, tertiary amyl alcohol and n-Octanol, and hydrolysis temperature is the boiling temperature of reaction medium.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 350 times, 620 times, 1500 times, 1850,2600,1800, inhales the salt solution multiple and is respectively 35 times, 60 times, 100 times, 120 times, 190 times, 125 times.
Embodiment 11-12
Working method is with embodiment 1, and difference is that the hydrolytic reagent that adds is potassium hydroxide and sodium ethylate.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 2500 times and 2200 times.
Embodiment 13-16
Working method is with embodiment 1, and difference is that the dosage of deionized water is respectively 5ml, 10ml, 30ml and 40ml.Obtain evengranular colourless or faint yellow granulated product, the particle diameter of product increases successively, be about 100 μ m, 200 μ m, 500 μ m, 800 μ m respectively, its suction multiple is respectively 700 times, 1500 times, 2550 times and 2800 times, inhales the salt solution multiple and is respectively 180 times, 190 times, 180 times and 160 times.
Embodiment 17-20
Working method is with embodiment 1, and difference is that the dosage of hydrolytic reagent is respectively 5g, 10g, 30g and 40g.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 650 times, 1200 times, 2600 times and 2250, inhales the salt solution multiple and is respectively 150 times, 160 times, 170 times and 180 times.
Embodiment 21-23
Working method is with embodiment 1, and difference is that hydrolysising reacting temperature is respectively 50 ℃, 60 ℃, 80 ℃ and 90 ℃.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 300 times, 500 times, 1500 times and 2100 times, inhales the salt solution multiple and is respectively 70 times, 80 times, 110 times and 150 times.
Embodiment 24-29
Working method is with embodiment 1, and difference is that hydrolysis time was respectively 1 hour, 3 hours, 8 hours, 12 hours and 24 hours.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 500 times, 1500 times, 2450 times, 2500 and 1800, inhales the salt solution multiple and is respectively 120 times, 140 times, 150,135 and 110 times.
Embodiment 30-32
Working method is with embodiment 1, and difference is that the liquid reaction medium weight ratio that polyacrylonitrile solid powder and alcohol and water are formed is 10: 100,30: 100,60: 100.Obtain evengranular colourless or faint yellow granulated product, the suction multiple of product is respectively 2500 times, 2100 times and 1650 times, inhales the salt solution multiple and is respectively 180 times, 175 times and 150 times.
Claims (10)
1, a kind of method of producing super absorbent resin with the polyacrylonitrile powder, it is characterized in that polyacrylonitrile powder, water, alcohol compound, hydrolytic reagent are warmed up to certain temperature carries out dispersed hydrolysis reaction under stirring action, hydrolysis reaction finishes after-filtration and goes out rosin products, drying obtains powder or granular product, described alcohol compound is to contain a monohydroxy-alcohol to eight carbon atoms, hydrolytic reagent is a strongly alkaline compound, hydrolysis temperature is the azeotropic point temperature of the complex reaction medium formed of alcohol compound and water, or is higher than 50 ℃ and is lower than the azeotropic point temperature.
2, method according to claim 1 is characterized in that hydrolysis time is 0.5-24 hour.
3, method according to claim 2 is characterized in that hydrolysis time is 1-12 hour.
4, method according to claim 1, the volume ratio that it is characterized in that water and alcohol compound is 1-40: 100, the weight ratio of hydrolytic reagent and polyacrylonitrile powder is 1-100: 100, and the liquid reaction medium weight ratio that polyacrylonitrile solid powder and alcohol and water are formed is 1-100: 100.
5, method according to claim 4, the volume ratio that it is characterized in that water and alcohol compound is 5-25: 100, the weight ratio of hydrolytic reagent and polyacrylonitrile powder is 5-50: 100, and the liquid reaction medium weight ratio that polyacrylonitrile solid powder and alcohol and water are formed is 10-60: 100.
6, method according to claim 1, it is characterized in that described alcohol compound select for use methyl alcohol, ethanol, n-propyl alcohol, Virahol, propyl carbinol, isopropylcarbinol, sec-butyl alcohol, Pentyl alcohol, primary isoamyl alcohol, tertiary amyl alcohol, neopentyl alcohol, n-hexyl alcohol, n-Heptyl alcohol, n-Octanol wherein a kind of, two or more.
7, method according to claim 1, it is characterized in that described hydrolytic reagent comprises alkali metal hydroxide, alkali metal alcohol compound, basic metal ammoniate, as sodium hydroxide, potassium hydroxide, sodium ethylate, potassium ethylate and ammonia sodium wherein a kind of, two or more.
8, method according to claim 1 is characterized in that described polyacrylonitrile powder is emulsion method or the acrylonitrile homopolymer of suspension polymerization one-tenth or the multipolymer of vinyl cyanide and acrylate.
9, method according to claim 8, the molecular weight ranges that it is characterized in that the polyacrylonitrile powder from the number-average molecular weight Mn of dry acrylic fiber handicraft product be about 30,000, the Mn of wet spinning acrylic fiber handicraft product is about the Mn of 100,000 high molecular weight products that obtain to emulsion polymerization up to hundreds of thousands of even higher, be included in the dry acrylic fiber technology from the molecular weight of the fallen portion of hot degraded of dryer and be lower than 30,000 and the useless dry powder of molecular weight distribution broad, the tens μ ms of the particle diameter of powder from about hundreds of nm of emulsion method product to the suspension method product.
10, method according to claim 8 is characterized in that the comonomer acrylate in the multipolymer of described vinyl cyanide and acrylate is selected from methyl acrylate, ethyl propenoate, butyl acrylate, methyl methacrylate, Jia Jibingxisuanyizhi, butyl methacrylate or vinyl-acetic ester.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295729A (en) * | 2010-06-25 | 2011-12-28 | 中国石油化工集团公司 | Preparation method of absorbent resin plugging agent |
| CN102335557A (en) * | 2011-09-13 | 2012-02-01 | 浙江大学 | Method for preparing polyelectrolyte complex/polyacrylonitrile hollow fiber composite pervaporation membrane |
| CN104059192A (en) * | 2014-07-04 | 2014-09-24 | 青岛科技大学 | Non-blending type ACM water swelling rubber and mass polymeriatio preparing method thereof |
| CN104086699A (en) * | 2014-07-04 | 2014-10-08 | 青岛科技大学 | Non-blending type high-stability polyacrylate water absorption swelling rubber and preparation method thereof |
| CN105255458A (en) * | 2015-11-30 | 2016-01-20 | 齐鲁工业大学 | Preparation method of efficient temperature-resisting and salinity-resisting filtrate reducer for drilling fluid |
| CN114606579A (en) * | 2020-12-03 | 2022-06-10 | 吉林碳谷碳纤维股份有限公司 | Ammonification method and device for polyacrylonitrile spinning solution |
-
2003
- 2003-12-26 CN CN 200310114564 patent/CN1264877C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102295729A (en) * | 2010-06-25 | 2011-12-28 | 中国石油化工集团公司 | Preparation method of absorbent resin plugging agent |
| CN102295729B (en) * | 2010-06-25 | 2013-07-31 | 中国石油化工集团公司 | Preparation method of absorbent resin plugging agent |
| CN102335557A (en) * | 2011-09-13 | 2012-02-01 | 浙江大学 | Method for preparing polyelectrolyte complex/polyacrylonitrile hollow fiber composite pervaporation membrane |
| CN102335557B (en) * | 2011-09-13 | 2013-06-12 | 浙江大学 | Method for preparing polyelectrolyte complex/polyacrylonitrile hollow fiber composite pervaporation membrane |
| CN104059192A (en) * | 2014-07-04 | 2014-09-24 | 青岛科技大学 | Non-blending type ACM water swelling rubber and mass polymeriatio preparing method thereof |
| CN104086699A (en) * | 2014-07-04 | 2014-10-08 | 青岛科技大学 | Non-blending type high-stability polyacrylate water absorption swelling rubber and preparation method thereof |
| CN105255458A (en) * | 2015-11-30 | 2016-01-20 | 齐鲁工业大学 | Preparation method of efficient temperature-resisting and salinity-resisting filtrate reducer for drilling fluid |
| CN105255458B (en) * | 2015-11-30 | 2018-12-04 | 齐鲁工业大学 | A kind of preparation method of high-efficient drilling fluid heat and salinity tolerance fluid loss additive |
| CN114606579A (en) * | 2020-12-03 | 2022-06-10 | 吉林碳谷碳纤维股份有限公司 | Ammonification method and device for polyacrylonitrile spinning solution |
| CN114606579B (en) * | 2020-12-03 | 2023-08-01 | 吉林碳谷碳纤维股份有限公司 | Ammoniation method and device for polyacrylonitrile spinning solution |
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