CN1328303C - Tech., for polymerizing fibre grade polyphenyl sulfoether resin - Google Patents

Tech., for polymerizing fibre grade polyphenyl sulfoether resin Download PDF

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Publication number
CN1328303C
CN1328303C CNB2005100224376A CN200510022437A CN1328303C CN 1328303 C CN1328303 C CN 1328303C CN B2005100224376 A CNB2005100224376 A CN B2005100224376A CN 200510022437 A CN200510022437 A CN 200510022437A CN 1328303 C CN1328303 C CN 1328303C
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China
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added
polyphenylene sulfide
resin
temperature
dichlorobenzene
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CN1793202A (en
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李勇
李炎
代晓徽
张勇
严永刚
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Sichuan Deyang Engineering Plastic Development Co., Ltd.
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SICHUAN DEYANG TECHNOLOGY Co Ltd
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Abstract

The present invention discloses a polymerization technology of fibre-grade polyphenylene sulfide resin. A polyphenylene sulfide (PPS) monomer is produced by adopting sodium sulfide and p-dichlorobenzene (P-DCB) as raw materials under the action of an alkali metal catalyst through polycondensation. The spinnability of obtained resin slices is improved by adopting the following technological conditions: in the dewatering treatment stage of the sodium sulfide, an auxiliary agent is added, the temperature of the sodium sulfide during stirring is slowly raised to 200DEG C in 2 to 6 hours, and the sodium sulfide is dewatered; in a polycondensation stage after dichlorobenzene is added, a regulating agent is added to raise the temperature to 200 to 275DEG C to carry out a polymerization reaction for 6 to 8 hours; a regulating agent is added at the temperature of 155 to 180DEG C to raise the temperature to 210 to 275DEG C, and the stirring is continued for 0.5 hour. An obtained mixture is filtered and washed more than once, and a synergistic agent is added in the process; the polyphenylene sulfide resin having good spinnability is obtained after rewashing with deionized water and drying treatment.

Description

Fiber-grade polyphenyl thioether resin polymerization technology
Affiliated technical field
The invention belongs to the macromolecule resin production field.
Background technology
High-performance polyphenylene sulfide has the thermostability under excellent chemical proofing and the high temperature, and has fire-retardant, insulation, radiation hardness and favorable mechanical performance.For enlarging the use range of this material, the investigators of various countries make it the novel method that fibrosis is used in searching always.
Chinese patent CN91107114 discloses a kind of potassium titanate fiber and the compound processing method of making matrix material of polyphenylene sulfide, in polycondensation vessel, at first use six polyamine dispersant (the synthetic solvent of using of double as polyphenylene sulfide) under heating and agitation condition, potassium titanate fiber to be disperseed, adding sodium sulphite and santochlor (P-DCB) then is raw material, (sodium sulphite and santochlor (P-DCB) are raw material to polycondensation production polyphenylene sulfide, and the fibre composite of polyphenylene sulfide (PPS) and potassium titanate fiber is produced in polycondensation under the base metal catalysts effect under the base metal catalysts effect.But this method makes the shortcoming that has the fibre breakage intensity difference.U.S. Pat 5401799 discloses a kind of polyphenylene sulfide based thermoplastic glass conjugated fibre with high-wearing feature, and composition of raw materials is provided.
With regard to the situation of prior art, the mode of matrix material is generally adopted in the manufacturing of polyphenylene sulfide fibre, though there is report U.S. Phillipsd company that the fiber-grade polyphenyl thioether production of resins is arranged, does not see the introduction of concrete technology.
The objective of the invention is to study a kind of fiber-grade polyphenyl thioether resin polymerization technology, improve the spinning property of resin, make the fiber manufacturing in later stage obtain the better properties index then by choose reasonable technic index, auxiliary agent, conditioning agent, synergistic agent.
Summary of the invention
The objective of the invention is to realize by following means.
Fiber-grade polyphenyl thioether resin polymerization technology, adopting sodium sulphite and santochlor (P-DCB) is raw material, polycondensation is produced in the monomeric technological process of polyphenylene sulfide (PPS) under the base metal catalysts effect, adopts following processing condition to improve the spinning property of the resin slicer of gained:
1) the sodium sulphite processed stage adds the auxiliary agent sodium borohydride, stirs slow intensification 2-6 hour down, is warming up to 200 ℃ of dehydrations;
2) add polycondensation phase behind the dichlorobenzene, add the nitro dichlorobenzene or to Histol, if be warming up to 200-275 ℃, polyreaction 6-8 hour;
3) through 1) 2) mixture that obtains of step, add the conditioning agent hexanodioic acids down at 155 ~ 185 ℃, be warmed up to 210 ℃ again and continue to stir 0.5 hour.
4) through 1), 2), 3) mixture that obtains of step, after 100 ~ 200 ℃ of filtrations, the filtration-washing repetitive process operation more than once again, and add synergistic agent quadrol tetrem disodium in stirring is washed through deionized water again.
1) through 1), 2), 3), 4) polyphenylene sulfide that obtains having better spinning property after the step resulting polymers drying treatment.
After adopting means as above, the crystallization of the resin of acquisition is more good, and spinning property improves, the breaking tenacity of the fiber that makes, and use temperature and oxygen index are improved.
Description of drawings:
Fig. 1 is the fibre resin index synopsis 1 of the Ryton of the resin that obtains of the present invention and Phillipsd company.
Fig. 2 is the fibre resin index synopsis 2 of the Ryton of the resin that obtains of the present invention and Phillipsd company.
Embodiment
Below in conjunction with embodiment technology of the present invention is described in further detail.
Embodiment 1
In autoclave, add N-methyl-2 pyrrolidone (NMP) 12 kilograms, sodium sulphite (Na 2S.3H 20) 44 kilogram, 0.01 kilogram of sodium borohydride (auxiliary agent), under the 0.01Mpa nitrogen gas pressure, stir on one side, heat up on one side, rise to 200 ℃ of dehydrations with 2 hours times, add 4.15 kilograms of santochlor again, the NMP2 kilogram, the nitro dichlorobenzene is warming up to 200 ℃ for 0.15 kilogram, 8 hours postcooling of polyreaction.185 ℃ add and are warmed up to 250 ℃ of processing after 0.1 kilogram of hexanodioic acid carries out, and mixture is after 140 ℃ of filtrations.With 40 liters of branches of deionized water 8 times the polymkeric substance that makes is carried out repetitive scrubbing, filtration, first and second time washing adds ammonium chloride 0 respectively.1 kilogram, the 4th washing adds 0.05 kilogram of synergistic agent quadrol tetrem disodium, dry under 100 ℃ then, obtain 2.05 kilograms of polyphenylene sulfides, flow rate 172g/10min (ASTM-1238-70), 283.5 ℃ of fusing points, ash 0.27%, volatile matter 0.28% (150 ℃), Mw52589, polydispersity coefficient PD2.19.
Embodiment 2
In autoclave, add N-methyl-2 pyrrolidone (NMP) 12 kilograms, sodium sulphite (Na 2S.3H 2O) 4 kilograms, 0.01 kilogram of sodium borohydride, under the 0.01MPa nitrogen gas pressure, stir on one side, heat up on one side, rise to 200 ℃ of dehydrations with 2 hours times, add 4.10 kilograms of santochlor again, the NMP2 kilogram is warming up to 275 ℃ to 0.17 kilogram of Histol, 6 hours postcooling of polyreaction.185 ℃ add and are warmed up to 250 ℃ of processing after 0.1 kilogram of hexanodioic acid carries out, mixture carries out repetitive scrubbing, filtration with 40 liters of branches of deionized water 8 times to the polymkeric substance that makes after 140 ℃ of filtrations, first and second time washing adds 0.1 kilogram of ammonium chloride respectively, adds 0.05 kilogram of quadrol tetrem disodium the 4th time.Dry under 100 ℃ then, obtain 2.1 kilograms of polyphenylene sulfides. flow rate 168g/10min (ASTM-1238-70), 283.0 ℃ of fusing points, ash 0.25%, volatile matter 0.27% (150 ℃), Mw47685, polydispersity coefficient PD2.4.
The resin of this explained hereafter is linear right-polyphenylene sulfide, and spinning property is superior, and the key technical indexes of the polyphenylene sulfide fibre that makes is good.
The fibre resin index of the fibre-grade PPS resin of its acquisition and the Ryton of Phillipsd company is relatively as table 1, by finding out in the table 1, the product sample 20021209 that the inventive method makes and 20021104 flow rate, ash and volatile matter index are all than the Ryton of Phillipsd company TWE2481 is low, therefore has more better spinnability energy.
The fiber of being made by resin of the present invention is by the detection to index of correlation of Sichuan Province examination of fibers office and national fire-proof construction material quality surveillance inspection center, the Ryton fiber of measurement result and Phillipsd company more as shown in Table 2,
As above contrast as seen, the product that the present invention obtains has better spinnability, and the fiber decapacitation that makes keeps the characteristic of PPS itself such as the chemical resistant properties of excellence, thermotolerance, outside the flame retardant resistance etc., also have more favorable mechanical performance, and its corresponding index all can reach international like product index.
In addition, in actual production, auxiliary agent can be a kind of of following material or several:
The material of the strong reducing power of tool: as formaldehyde, acetaldehyde, sodium borohydride, POTASSIUM BOROHYDRIDE, Thiovanic acid, hydrazine hydrate, phenylhydrazine, pyrodin, phosphorous acid ester, Sodium Nitrite, boron nitride, 4, the two sulfonyl hydrazides of 4-oxo etc.
Conditioning agent can be a kind of of following material or several:
Organic acid or mineral acid: as palmitinic acid, citric acid, lauric acid, hexanodioic acid, butyric acid, n-nonanoic acid,, Sorbic Acid, stearic acid, toxilic acid, pentanedioic acid, mineral acid such as sulfuric acid, hydrochloric acid, etc.
Synergistic agent can be a kind of of following material or several:
The carboxylate salt of alkali or alkaline-earth metal or strong acid weak base salt, sulfonate: as ammonium sulfate, magnesium chloride, ammonium chloride, ammonium sulphite, zinc sulfate, zinc sulfite, zinc chloride, sebacic acid penta 2 ammoniums, ammonium nitrate, Soduxin, hexanodioic acid sodium, disodium EDTA, calcium acetate, Sodium Glycinate, hydroxy-propionic acid potassium, tetrasodium ethylenediamine tetraacetate, dodecylbenzene sulfonate, sodium allyl sulfonate, sodium cetanesulfonate etc.

Claims (1)

1, fiber-grade polyphenyl thioether resin polymerization technology is raw material adopting sodium sulphite and santochlor, and polycondensation is produced in the monomeric technological process of polyphenylene sulfide under the base metal catalysts effect, adopts following processing condition to improve the spinning property of the resin slicer of gained:
1) in the sodium sulphite processed stage, add the auxiliary agent sodium borohydride, stirred slow intensification 2-6 hour down, be warming up to 200 ℃ of dehydrations;
2) polycondensation phase behind the adding dichlorobenzene adds the nitro dichlorobenzene or to Histol, is warming up to 200-275 ℃, polyreaction 6-8 hour;
3) through 1), 2) mixture that obtains of step, add the conditioning agent hexanodioic acids down at 155 ~ 185 ℃ and be warmed up to 210 ~ 275 ℃ again and continue to stir 0.5 hour.
4) through 1), 2), 3) mixture that obtains of step, after 100 ~ 200 ℃ of filtrations, the filtration-washing repetitive process operation more than once again, and add synergistic agent quadrol tetrem disodium in the agitator treating process is washed through deionized water again;
Through 1), 2), 3), 4) polyphenylene sulfide that obtains having better spinning property after the step resulting polymers drying treatment.
CNB2005100224376A 2005-12-29 2005-12-29 Tech., for polymerizing fibre grade polyphenyl sulfoether resin Expired - Fee Related CN1328303C (en)

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Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102675640B (en) * 2011-03-18 2014-06-25 四川得阳工程塑料开发有限公司 Method for controlling process conditions for production and synthesis of polyphenylene sulfide
CN103147154A (en) * 2011-12-06 2013-06-12 江苏阜升环保集团有限公司 Hyperbranched antioxidative polyphenylene sulfide fibers and preparation method thereof
CN102702528A (en) * 2012-05-28 2012-10-03 自贡鸿鹤化工股份有限公司 Production method for polyphenyl thioether
CN103172864B (en) * 2013-04-23 2015-02-25 四川大学 Preparation method of organic acid salt catalytic polyarylene sulfide
CN103601887B (en) * 2013-11-20 2016-04-20 珠海长先化学科技有限公司 A kind of method of adding compound accelerant synthon level polyphenylene sulfide in stage casing
CN103951825B (en) * 2014-04-29 2016-03-30 四川中科兴业高新材料有限公司 A kind of high strength polyphenylene sulfide and preparation method thereof
CN105085917A (en) * 2015-08-05 2015-11-25 广州高八二塑料有限公司 Film-grade polyphenylene sulfide resin and preparation method thereof
KR102196506B1 (en) 2017-10-20 2020-12-29 주식회사 엘지화학 Process for preparing polyarylene sulfide
KR102173641B1 (en) * 2017-11-24 2020-11-03 주식회사 엘지화학 Process for preparing polyarylene sulfide
CN111171320B (en) * 2020-02-13 2022-05-06 四川明道和化学新材料有限公司 Production method of catalyst-removed polyphenylene sulfide resin
CN111548493A (en) * 2020-05-11 2020-08-18 山东滨化滨阳燃化有限公司 Washing treatment method of fiber-grade polyphenylene sulfide industrial product
CN112574414B (en) * 2020-12-09 2022-02-01 浙江大学 Synthetic method of polyarylene sulfide resin
CN114634621A (en) * 2021-12-21 2022-06-17 江苏邦正新材料有限公司 Hydrothermal synthesis method of pps nano composite material

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JPH08120081A (en) * 1994-10-25 1996-05-14 Tonen Chem Corp High-molecular poly(arylene sulfide) for molded sheet
CN1292012A (en) * 1998-03-05 2001-04-18 提克纳有限公司 Method for producing sulfur-containing polymers
CN1309142A (en) * 2000-12-27 2001-08-22 古旗高 Process for preparing high-density high-molecular linear polyphenyl thioether
US20020019501A1 (en) * 2000-07-07 2002-02-14 Petroleum Energy Center Production process for polyarylene sulfide
CN1345891A (en) * 2000-09-30 2002-04-24 四川省华拓实业发展股份有限公司 Method for controlling synthetic technological condition of producing polyphenyl-thioether
JP2003268105A (en) * 2002-03-19 2003-09-25 Toray Ind Inc Method for manufacturing poly(arylene sulfide)

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08120081A (en) * 1994-10-25 1996-05-14 Tonen Chem Corp High-molecular poly(arylene sulfide) for molded sheet
CN1292012A (en) * 1998-03-05 2001-04-18 提克纳有限公司 Method for producing sulfur-containing polymers
US20020019501A1 (en) * 2000-07-07 2002-02-14 Petroleum Energy Center Production process for polyarylene sulfide
CN1345891A (en) * 2000-09-30 2002-04-24 四川省华拓实业发展股份有限公司 Method for controlling synthetic technological condition of producing polyphenyl-thioether
CN1309142A (en) * 2000-12-27 2001-08-22 古旗高 Process for preparing high-density high-molecular linear polyphenyl thioether
JP2003268105A (en) * 2002-03-19 2003-09-25 Toray Ind Inc Method for manufacturing poly(arylene sulfide)

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