CN1401675A - Method for preparing polyacrylonitrile based carbon fibre spinning solution - Google Patents
Method for preparing polyacrylonitrile based carbon fibre spinning solution Download PDFInfo
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- CN1401675A CN1401675A CN 02130023 CN02130023A CN1401675A CN 1401675 A CN1401675 A CN 1401675A CN 02130023 CN02130023 CN 02130023 CN 02130023 A CN02130023 A CN 02130023A CN 1401675 A CN1401675 A CN 1401675A
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- vinyl cyanide
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Abstract
A polyacrylnitrile-base carbon fibre spinning liquid is prepared from acrylnitrile, dimethyl formamide, distilled water, azodiisobutylnitrile and chain transfer agent through homopolymerization, introducing ammonia gas to stop reaction, and regulating pH value by ammonia gas. Its advantages are uniform distribution of function groups on macro-molecular chain, simple process and easy control.
Description
Affiliated field:
The invention belongs to a kind of preparation method of carbon fiber spinning solution, relate to a kind of preparation method of polyacrylonitrile based carbon fibre spinning solution specifically.
Background technology:
Cyclisation is an important step in the charcoal fiber production process, the introducing of comonomer can make the free radical type cyclization of homopolymer change ionic cyclization course into, reduce the activation energy of cyclization, thereby reduced the starting temperature of exothermic peak, suppressed heat release speed.Simultaneously, the introducing of comonomer can be played the supramolecular structure effect of regulating polyacrylonitrile (PAN), can increase the kindliness of polymer molecule segment, thereby reaches the purpose that improves the polymkeric substance spinning property, and helps the draw orientation in the spinning process.Usually the comonomer of introducing has: vinylformic acid, methacrylic acid, methylene-succinic acid, methyl methacrylate, acrylamide etc.Adopt solution polymerization process that vinyl cyanide/methylene-succinic acid/acrylamide is carried out terpolymer as viscose yarn company of Mitsubishi and obtain charcoal fiber PAN resin.Dong Li company carries out binary copolymerization with the dimethyl sulphoxide solution polymerization with vinyl cyanide/methylene-succinic acid, preparation high-performance carbon fibre resin.Domestic adopt with acrylonitrile/methyl acrylate/methylene-succinic acid/ternary altogether or vinyl cyanide/methylene-succinic acid carry out binary copolymerization, thereby obtain the charcoal fibre resin.Because monomer chemical structure difference, both activities is also variant, in polymerization process, monomer concentration constantly changes in polymerization process, successively the multipolymer that generates is formed reasons such as also inconsistent, can cause copolymerization units skewness on macromolecular chain, produce molecular defect, thereby influence the performance of charcoal fiber.
In addition, each polymer macromolecule all has two end groups, and end group also is the important chemical constitution factor that influences the spinning solution quality.The end group of macromolecular chain depends on initiation and the termination in the polymerization process, end group may derive from monomer, initiator, solvent, molecular weight regulator or other impurity, therefore the chemical property of end group is often different with main chain, and its behavior also is different from the PAN structural unit in preoxidation and carbonization process, thereby influence the performance of charcoal fiber, therefore control the chemical structure of polyacrylonitrile macromole end group, make its preoxidation carbonization process that helps the charcoal fiber, the performance that improves the charcoal fiber is very important.And yet there are no report about this respect document.
Summary of the invention:
The purpose of this invention is to provide a kind of copolymerization units and on macromolecular chain, be evenly distributed, the preparation method of the controllable polyacrylonitrile based carbon fibre spinning solution of end group
The present invention adopts dimethyl formamide, water, chain-transfer agent, vinyl cyanide to carry out the solution homopolymerization, acrylonitrile homopolymer solution being carried out ammonification handles again, add an amount of chain-transfer agent simultaneously, thereby obtain the PAN-based carbon fiber presoma spinning solution that carboxyl and amide group occupy the position of quite a few end group.Concrete preparation method of the present invention comprises the step following steps: mix vinyl cyanide, dimethyl formamide, distilled water, Diisopropyl azodicarboxylate and chain-transfer agent by weight ratio (1): dimethyl formamide is (10-1000) with the water ratio: 1, vinyl cyanide is (100-400) with the Diisopropyl azodicarboxylate ratio: 1, dimethyl formamide is 10 with the ratio of vinyl cyanide: (1-5), dimethyl formamide is (50-500) with the chain-transfer agent ratio: 1,50-70 ℃ of reaction 1-15 hour; (2) in system, feed ammonia and make PH to 8-9, stop polyreaction; (3) regulating PH with ammonia is 9-14, and temperature 80-100 ℃, list, deaeration are taken off in hydrolysis 5 minutes to 2 hours, make spinning solution.Aforesaid chain-transfer agent is formic acid, acetate, methane amide or ethanamide
The invention has the advantages that: 1. the functional group that produces of homogeneous hydrolysis is evenly distributed on macromolecular chain, do not exist functional group in chain, the ununiformity of interchain distribution.2. technology is simple, easy control of reaction conditions.3. the water in the mixed solvent influences the reactive force between resin and solvent molecule, reduces polymer solution viscosity, perhaps can obtain the more spinning solution of high solids content under identical viscosity.4. polymer terminal group is controlled, and making polypropylene segment nitrile end group is ester group.5. chain-transfer agent can impel Diisopropyl azodicarboxylate residual in the polymerization system to decompose, and reduces residual initiators content in the polymkeric substance, improves PAN purity.
Specific implementation method:
Embodiment 1:(1) take by weighing the purified vinyl cyanide of 600 grams, 6000 restrain dimethyl formamides, 6 gram water, and acetate 12 grams add 3 gram Diisopropyl azodicarboxylates, react 1 hour in 70 ℃ under nitrogen protection.(2) logical ammonia makes PH=9 in the system, stops polyreaction.(3) continue logical ammonia and regulate PH to 11, system temperature is risen to 95 ℃, list, deaeration are taken off in hydrolysis 40 minutes, make spinning solution.
Embodiment 2:(1) take by weighing the purified vinyl cyanide of 400 grams, 800 restrain dimethyl formamides, 40 gram water, and formic acid 2 grams, the Diisopropyl azodicarboxylate of adding 1 gram reacted 15 hours in 50 ℃ under nitrogen protection.(2) feed ammonia in the system and make PH=8, stop polyreaction.(3) continue logical ammonia and regulate PH to 14, system temperature is risen to 100 ℃, list, deaeration are taken off in hydrolysis 5 minutes, make spinning solution.
Embodiment 3:(1) take by weighing the purified vinyl cyanide of 1000 grams, 3600 restrain dimethyl formamides, 20 gram water, and methane amide 20 grams, the Diisopropyl azodicarboxylate of adding 5 grams reacted 8 hours in 60 ℃ under nitrogen protection.(2) feed ammonia in the system and make PH=9, polyreaction stops.(3) keeping PH is 9, and system temperature is risen to 80 ℃, and list, deaeration are taken off in hydrolysis 2 hours, make spinning solution.
Embodiment 4:(1) take by weighing the purified vinyl cyanide of 1000 grams, 4500 restrain dimethyl formamides, 30 gram water, and acetate 10 grams, the Diisopropyl azodicarboxylate of adding 10 grams reacted 7 hours in 60 ℃ under nitrogen protection.(2) feed ammonia in the system and make PH=9, polyreaction stops.(3) regulate PH to 12 with ammonia, system temperature is risen to 90 ℃, list, deaeration are taken off in hydrolysis 30 minutes, make spinning solution.
Embodiment 5:(4) take by weighing the purified vinyl cyanide of 800 grams, 3200 restrain dimethyl formamides, 260 gram water, and ethanamide 10 grams, the Diisopropyl azodicarboxylate of adding 5 grams reacted 5 hours in 65 ℃ under nitrogen protection.(5) feed ammonia in the system and make PH=8.7, polyreaction stops.(6) regulate PH to 11.5 with ammonia, system temperature is risen to 90 ℃, list, deaeration are taken off in hydrolysis 45 minutes, make spinning solution.
Embodiment 6:(1) take by weighing the purified vinyl cyanide of 1200 grams, 4000 restrain dimethyl formamides, 80 gram water, and acetate 8 grams, the Diisopropyl azodicarboxylate of adding 6 grams reacted 6 hours in 62 ℃ under nitrogen protection.(2) feed ammonia in the system and make PH=9, polyreaction stops.(3) regulate PH to 10.6 with ammonia, system temperature is risen to 90 ℃, list, deaeration are taken off in hydrolysis 50 minutes, make spinning solution.
Embodiment 7:(1) take by weighing the purified vinyl cyanide of 900 grams, 3600 restrain dimethyl formamides, 100 gram water, and acetate 9 grams, the Diisopropyl azodicarboxylate of adding 8 grams reacted 9 hours in 58 ℃ under nitrogen protection.(2) feed ammonia in the system and make PH=8.9, polyreaction stops.(3) regulate PH to 12.3 with ammonia, system temperature is risen to 96 ℃, list, deaeration are taken off in hydrolysis 45 minutes, make spinning solution.
Claims (2)
1. the preparation method of a polyacrylonitrile based carbon fibre spinning solution, tool is characterised in that and comprises the steps: that (1) mix vinyl cyanide, dimethyl formamide, distilled water, Diisopropyl azodicarboxylate and chain-transfer agent by weight ratio: dimethyl formamide and water are than being (10-1000): 1, vinyl cyanide is (100-400) with the Diisopropyl azodicarboxylate ratio: 1, dimethyl formamide is 10 with the ratio of vinyl cyanide: (1-5), dimethyl formamide is (50-500) with the chain-transfer agent ratio: 1,50-70 ℃ of reaction 1-15 hour; (2) feed ammonia in the system and make PH to 8-9, stop polyreaction; (3) ammonia adjusting PH is 9-14, and temperature 80-100 ℃, list, deaeration are taken off in hydrolysis 5 minutes to 2 hours, make spinning solution.
2. the preparation method of a kind of polyacrylonitrile based carbon fibre spinning solution as claimed in claim 1 is characterized in that described chain-transfer agent is formic acid, acetate, methane amide or ethanamide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021300232A CN1171918C (en) | 2002-08-13 | 2002-08-13 | Method for preparing polyacrylonitrile based carbon fibre spinning solution |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021300232A CN1171918C (en) | 2002-08-13 | 2002-08-13 | Method for preparing polyacrylonitrile based carbon fibre spinning solution |
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| Publication Number | Publication Date |
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| CN1401675A true CN1401675A (en) | 2003-03-12 |
| CN1171918C CN1171918C (en) | 2004-10-20 |
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| CNB021300232A Expired - Lifetime CN1171918C (en) | 2002-08-13 | 2002-08-13 | Method for preparing polyacrylonitrile based carbon fibre spinning solution |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100365178C (en) * | 2005-08-03 | 2008-01-30 | 厦门大学 | Preparation method of polyacrylonitrile-based carbon core |
| CN102060372A (en) * | 2010-11-24 | 2011-05-18 | 同济大学 | Porous filler with large specific surface area for wastewater denitrification and preparation method thereof |
| CN102586921A (en) * | 2011-01-06 | 2012-07-18 | 北京腾化技术有限责任公司 | Method for producing polyacrylonitrile-based carbon fiber precursor |
| CN105088422A (en) * | 2015-08-21 | 2015-11-25 | 威海拓展纤维有限公司 | Method for filling ammonia in preparation of polyacrylonitrile spinning solution |
| CN106353306A (en) * | 2016-08-17 | 2017-01-25 | 中简科技股份有限公司 | Method for testing residual acrylonitrile monomer content in spinning solution during carbon fiber production |
| CN111647956A (en) * | 2020-05-21 | 2020-09-11 | 中复神鹰碳纤维有限责任公司 | Method for preparing dry-jet wet-spun polyacrylonitrile nascent fiber by using annular spinneret plate |
-
2002
- 2002-08-13 CN CNB021300232A patent/CN1171918C/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100365178C (en) * | 2005-08-03 | 2008-01-30 | 厦门大学 | Preparation method of polyacrylonitrile-based carbon core |
| CN102060372A (en) * | 2010-11-24 | 2011-05-18 | 同济大学 | Porous filler with large specific surface area for wastewater denitrification and preparation method thereof |
| CN102060372B (en) * | 2010-11-24 | 2012-06-06 | 同济大学 | Porous filler with large specific surface area for wastewater denitrification and preparation method thereof |
| CN102586921A (en) * | 2011-01-06 | 2012-07-18 | 北京腾化技术有限责任公司 | Method for producing polyacrylonitrile-based carbon fiber precursor |
| CN105088422A (en) * | 2015-08-21 | 2015-11-25 | 威海拓展纤维有限公司 | Method for filling ammonia in preparation of polyacrylonitrile spinning solution |
| CN106353306A (en) * | 2016-08-17 | 2017-01-25 | 中简科技股份有限公司 | Method for testing residual acrylonitrile monomer content in spinning solution during carbon fiber production |
| CN106353306B (en) * | 2016-08-17 | 2019-10-25 | 中简科技股份有限公司 | The test method of spinning solution remaining propylene nitrile monomer content in a kind of carbon fiber production process |
| CN111647956A (en) * | 2020-05-21 | 2020-09-11 | 中复神鹰碳纤维有限责任公司 | Method for preparing dry-jet wet-spun polyacrylonitrile nascent fiber by using annular spinneret plate |
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| Publication number | Publication date |
|---|---|
| CN1171918C (en) | 2004-10-20 |
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Owner name: ZHONGJIAN TECHNOLOGY DEVELOPMENT CO., LTD. Free format text: FORMER OWNER: SHANXI INST. OF COAL CHEMISTRY, CHINESE ACADEMY OF SCIENCES Effective date: 20090828 |
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Effective date of registration: 20090828 Address after: Jiangsu Province, Changzhou City, North Industrial Park Patentee after: ZHONGJIAN SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Address before: 165 mailbox, Taiyuan City, Shanxi Province Patentee before: INSTITUTE OF COAL CHEMISTRY, CHINESE ACADEMY OF SCIENCES |
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Address after: 213127 Jiangsu province Changzhou Xingfeng Road New District No. 6 Patentee after: SINOFIBERS TECHNOLOGY Co.,Ltd. Address before: 213022 Jiangsu province Changzhou City North Industrial Park Patentee before: ZHONGJIAN SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. |
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