CN100441753C - Prepn of hollow high-strength light-modulus polyethylene fiber - Google Patents

Prepn of hollow high-strength light-modulus polyethylene fiber Download PDF

Info

Publication number
CN100441753C
CN100441753C CNB2006100290315A CN200610029031A CN100441753C CN 100441753 C CN100441753 C CN 100441753C CN B2006100290315 A CNB2006100290315 A CN B2006100290315A CN 200610029031 A CN200610029031 A CN 200610029031A CN 100441753 C CN100441753 C CN 100441753C
Authority
CN
China
Prior art keywords
fiber
polyethylene
spinning
hollow
under
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.)
Active
Application number
CNB2006100290315A
Other languages
Chinese (zh)
Other versions
CN1888153A (en
Inventor
于俊荣
胡祖明
潘婉莲
陈蕾
诸静
刘兆峰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Donghua University
Original Assignee
Donghua University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Donghua University filed Critical Donghua University
Priority to CNB2006100290315A priority Critical patent/CN100441753C/en
Publication of CN1888153A publication Critical patent/CN1888153A/en
Application granted granted Critical
Publication of CN100441753C publication Critical patent/CN100441753C/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Artificial Filaments (AREA)

Abstract

The present invention discloses preparation process of hollow high-strength and high-modulus polyethylene fiber. The preparation process includes the following steps: high temperature swelling and dissolving to obtain spinning fluid of ultra high molecular weight polyethylene, gel spinning with inserted tubular spinning jet with high temperature compressed air introduced to inside, quenching to form gel fiber, extracting and super drawing to obtain the hollow high-strength and high-modulus polyethylene fiber. The present invention has shortened path for the solvent inside fiber to diffuse out, high extracting efficiency, simplified extracting process, homogenized structure and raised mechanical performance of fiber.

Description

A kind of preparation method of hollow high-strength high-modulus polyethylene fiber
Technical field
The present invention relates to a kind of preparation method of polyethylene fiber, particularly relate to the preparation method of a kind of hollow high-strength high-modulus polyethylene fiber (UHMWPE, weight average relative molecular weight are 100~5,000,000).
Background technology
The ultra high molecular weight polyethylene fiber is the third generation high-performance fiber that occurs after carbon fiber and aramid fiber, have other high-performance fiber incomparable mechanical property.In present synthetic fiber, the UHMWPE fiber has lower density, higher elongation at break, specific strength and specific modulus maximum have surpassed metal material, the more important thing is that it also has the excellent energy absorption characteristic, optimum absorbs the fragmentation impact energy of low speed, and ballistic performance is best, and does not have the secondary lethal effect, be a kind of desirable bullet resistant material, be widely used in security personnel and military aspect at present.The UHMWPE fiber is owing to have multiple excellent properties such as ultralight, high specific strength, high ratio modulus, shock-resistant, chemicals-resistant, UV resistant, low temperature resistant, electric insulation, be present best hawser material and high-tech armament material, also very desirable on space flight navigation purposes.Its reinforced composite has also obtained using widely because of having excellent characteristic.
The ultra high molecular weight polyethylene fiber normally adopts gel spinning-super drawing method to be prepared from.In CN99111581, reported a kind of production technology of high-strength high-modulus polyethylene fiber as Chen Chengsi, at first the super high molecular weight condensate is dissolved among the corresponding solvent, obtain the solution of low big molecular entanglement, become gel spun fiber through the spinning quenching, through technical process such as extraction, drying and multistage hot-stretchs, make the polyethylene fiber of high-strength and high-modulus then.The process of the preparation high-strength high-modulus polyethylene fiber that other have proposed is mostly similar, patent that just has such as CN90102855, CN97101010, whole gel spinning-ultra-drawn all technical process are described and claim as USP5342567, USP5443904, CN02115024 etc., what have then is described and claim limitation the technical process in a certain stage wherein, discloses the preparation method of extra high molecular polyethylene high-concentrated solution for spinning as CN01123600; CN02160744, CN200410096619, CN200510073249 then disclose extraction, the drying process method in the superhigh molecular weight polyethylene fibers preparation; USP5578374, USP5741451, USP5958582 have carried out detailed description and right qualification to the super drawing process of gel spinning gained fiber.
Above-mentioned the whole bag of tricks gained polyethylene fiber frozen glue is solid fiber.Owing to contain a large amount of solvents in the gel spun fiber of gel spinning-quenching gained, as described in the above-mentioned process like that, need to surpass a times hot-stretch more afterwards and obtain high-strength high-modulus fibre through the solvent that fiber is removed in extraction.Because the mechanism of extraction is based on interpenetrating and spread between fiber solvent and the extractant, then the speed that desolventizes of gel spun fiber depends on the size of the movement velocity of solvent and extractant molecules to a great extent.Outside the Pass the speed of solvent diffuse speed removed and to have with the extraction process condition, also the path of passing through with solvent diffuse was relevant.In the gel spun fiber extraction process, the solvent molecule of fibrous outer preferentially diffuses out in gel spun fiber, because the iris action of polyethylene macromolecular network, the solvent molecule of gel spun fiber core difficulty diffuses out, and can make the fibre section form skin-core structure.Though this skin-core structure is so obvious not as wet spun fibre, this structure irregular can influence the super drawing of fiber, and and then influence the mechanical property of finished fiber.
For the hollow polyethylene fiber, the method that has proposed at present all concentrates on produces on the doughnut filter membrane.Disclose the method for preparing polyethylene hollow fiber as USP4115492, USP5294338, USP6436319, ZL200510049263 etc., used polyethylene is high density polyethylene (HDPE), employing be melt spinning method.And USP5695702 and ZL95193838 disclose thermoplasticity hollow fiber film assembly and manufacture method thereof, wherein mentioned the doughnut that ultrahigh molecular weight polyethylene forms fully, but this fiber only limits to filter the hollow-fibre membrane of usefulness, high-strength and high-modulus far from.
Summary of the invention
Technical problem to be solved by this invention provides a kind of preparation method of hollow high-strength high-modulus polyethylene fiber, to remedy the deficiencies in the prior art or defective, meets the demands of production and living.
In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is: a kind of preparation method of hollow high-strength high-modulus polyethylene fiber comprises the steps:
(1) with the weight average relative molecular weight be 100~5,000,000 polyethylene powders and mineral oil by weight proportion 1-12: 88-99 be made into and poise liquid, ratio in polyethylene and antioxidant weight is 100: the ratio of 0.1-1.0 adds antioxidant, under stirring, be warming up to 105-130 ℃ of swelling 0.5-2 hour, and then be warming up to 160-200 ℃ of dissolving and made spinning solution in 0.5-2 hour, wherein ultra high molecular weight polyethylene contains 1~12%;
(2) adopting slit width is 0.3-0.8mm, bore is the insertion tubular type spinning head of 0.3-0.6mm, spinning solution is sprayed via the slit that inserts the tubular type spinning head, spinning temperature is 140~180 ℃, and spinning pressure is 2~4 times of the feeding compressed air pressure, and inserting the inner compressed air temperature that feeds of pipe is 130~150 ℃, after the ejection of spinning solution stream, through the air layer of 2-10mm, directly enter in-1 ℃-25 ℃ the cold bath, quenching becomes the hollow gel spun fiber;
(3) gained hollow gel spun fiber directly enters and carries out ultrasonic tensioning extraction in the carrene, enter air dry oven and carry out room temperature tensioning drying, the one-level of carrying out 15~30 times then under 60-100 ℃ stretches, under 90-118 ℃, carry out 1.3~3 times of secondary drawing, under 120-150 ℃, carry out 1.1~1.9 times of three grades of stretchings, gained finished product polyethylene fiber.
As optimized technical scheme: described mineral oil is the white oil of commercially available 70#-120#, paraffin oil, one or more in the atoleine.
Described antioxidant is commercial antioxidant 1010,1076,168, B215, B225, B561, B900,3114,1098,1024,1035,1135,245,300, BHT, DSTP, DLTP, TPP, TNPP, one or more in the CA series.
The invention has the beneficial effects as follows: the present invention has shortened the path that the fiber internal solvent diffuses out the gel spun fiber process, improves extraction efficiency, simplied extraction process, and it is irregular to eliminate structure, further improves the mechanical property of fiber.
Description of drawings
The high-strength polyethylene doughnut cross section microscope figure that Fig. 1 the present invention makes
The vertical microscope figure of the high-strength polyethylene doughnut that Fig. 2 the present invention makes
The specific embodiment
Below in conjunction with specific embodiment the present invention is further elaborated.
Embodiment 1
With the weight average relative molecular weight is that 4,500,000 polyethylene (UHMWPE) powder and 90# white oil were made into by weight 10: 90 and poise liquid, in the ratio of polyethylene (UHMWPE) and antioxidant 1010 weight is that 100: 0.6 ratio adds antioxidant, under stirring, be warming up to 130 ℃ of swellings 1 hour, and then be warming up to 180 ℃ of dissolvings and made spinning solution in 1 hour, wherein ultra high molecular weight polyethylene contains 10%;
The employing slit width is 0.5mm, bore is the insertion tubular type spinning head of 0.5mm, with spinning solution slit ejection via insertion tubular type spinning head under 180 ℃, insert the compressed air of 140 ℃ of the inner feedings of pipe, the control spinning pressure is 2 times of compressed air pressure.After the spinning solution stream ejection, the air layer through 5mm directly enters ice-water bath, and quenching becomes the hollow gel spun fiber, the cross section of gained hollow gel spun fiber and vertically microscope figure as shown in Figure 1, degree of hollowness is 20%.Gained hollow gel spun fiber directly enters and carries out ultrasonic tensioning extraction in the carrene, enter air dry oven and carry out room temperature tensioning drying, the one-level of carrying out 20 times then under 90 ℃ stretches, under 100 ℃, carry out 2 times of secondary drawing, under 120 ℃, carry out 1.3 times of three grades of stretchings, the fracture strength of gained finished product UHMWPE fiber is 32.6cN/dtex, and modulus is 1250cN/dtex, extension at break 2.8%.
Embodiment 2
With the weight average relative molecular weight is that 1,000,000 polyethylene (UHMWPE) powder and 80# white oil were made into by weight 1: 99 and poise liquid, in polyethylene (UHMWPE) and antioxidant 1076 weight ratio is that 100: 0.1 ratio adds antioxidant, under stirring, be warming up to 105 ℃ of swellings 2 hours, and then be warming up to 160 ℃ of dissolvings and made spinning solution in 2 hours, wherein ultra high molecular weight polyethylene contains 1%;
The employing slit width is 0.3mm, bore is the insertion tubular type spinning head of 0.6mm, with spinning solution slit ejection via insertion tubular type spinning head under 170 ℃, insert the compressed air of 160 ℃ of the inner feedings of pipe, the control spinning pressure is 3 times of compressed air pressure.After the ejection of spinning solution stream, air layer through 2mm, directly enter ice-water bath, quenching becomes the hollow gel spun fiber, and gained hollow gel spun fiber directly enters and carries out ultrasonic tensioning extraction in the carrene, enters air dry oven and carries out room temperature tensioning drying, the one-level of carrying out 30 times then under 60 ℃ stretches, under 90 ℃, carry out 3 times of secondary drawing, under 150 ℃, carry out 1.1 times of three grades of stretchings, make finished product UHMWPE fiber.
Embodiment 3
With the weight average relative molecular weight is that 5,000,000 polyethylene (UHMWPE) powder and paraffin oil were made into by weight 12: 88 and poise liquid, in polyethylene (UHMWPE) and antioxidant 168 weight ratios is that 100: 1.0 ratio adds antioxidant, under stirring, be warming up to 110 ℃ of swellings 0.5 hour, and then be warming up to 200 ℃ of dissolvings and made spinning solution in 0.5 hour, wherein ultra high molecular weight polyethylene contains 12%;
The employing slit width is 0.8mm, bore is the insertion tubular type spinning head of 0.3mm, with spinning solution slit ejection via insertion tubular type spinning head under 140 ℃, insert the compressed air of 180 ℃ of the inner feedings of pipe, the control spinning pressure is 4 times of compressed air pressure.After the ejection of spinning solution stream, air layer through 10mm, directly enter ice-water bath, quenching becomes the hollow gel spun fiber, and gained hollow gel spun fiber directly enters and carries out ultrasonic tensioning extraction in the carrene, enters air dry oven and carries out room temperature tensioning drying, the one-level of carrying out 15 times then under 100 ℃ stretches, under 118 ℃, carry out 2.8 times of secondary drawing, under 130 ℃, carry out 1.7 times of three grades of stretchings, make finished product UHMWPE fiber.
Comparative example:
Is that spinning head ejection, the quenching of 0.85mm becomes solid UHMWPE gel spun fiber with prepared spinning solution among the embodiment 1 via the aperture, adopt and same extraction, the drawing process of embodiment then, the intensity of prepared UHMWPE fiber is 24.8cN/dtex, modulus is 830cN/dtex, and extension at break is 2.92%.

Claims (3)

1, a kind of preparation method of hollow high-strength high-modulus polyethylene fiber is characterized in that, comprises the steps:
(1) with the weight average relative molecular weight be 100~5,000,000 polyethylene powders and mineral oil by weight proportion 1-12: 88-99 be made into and poise liquid, ratio in polyethylene and antioxidant weight is 100: the ratio of 0.1-1.0 adds antioxidant, under stirring, be warming up to 105-130 ℃ of swelling 0.5-2 hour, and then be warming up to 160-200 ℃ of dissolving and made spinning solution in 0.5-2 hour, wherein ultra high molecular weight polyethylene contains 1~12%;
(2) adopting slit width is 0.3-0.8mm, bore is the insertion tubular type spinning head of 0.3-0.6mm, spinning solution is sprayed via the slit that inserts the tubular type spinning head, spinning temperature is 140~180 ℃, and spinning pressure is 2~4 times of the feeding compressed air pressure, and inserting the inner compressed air temperature that feeds of pipe is 130~150 ℃, after the ejection of spinning solution stream, through the air layer of 2-10mm, directly enter in-1 ℃-25 ℃ the cold bath, quenching becomes the hollow gel spun fiber;
(3) gained hollow gel spun fiber directly enters and carries out ultrasonic tensioning extraction in the carrene, enter air dry oven and carry out room temperature tensioning drying, the one-level of carrying out 15~30 times then under 60-100 ℃ stretches, under 90-118 ℃, carry out 1.3~3 times of secondary drawing, under 120-150 ℃, carry out 1.1~1.9 times of three grades of stretchings, gained finished product polyethylene fiber.
2, preparation method according to claim 1 is characterized in that, described mineral oil is one or more in the white oil of 70#-120#.
3, preparation method according to claim 1 is characterized in that, described antioxidant is commercial antioxidant 1010,1076,168, B215, B225, B561, B900,3114,1098,1024,1035,1135,245,300, BHT, DSTP, DLTP, TPP, TNPP, one or more in the CA series.
CNB2006100290315A 2006-07-18 2006-07-18 Prepn of hollow high-strength light-modulus polyethylene fiber Active CN100441753C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2006100290315A CN100441753C (en) 2006-07-18 2006-07-18 Prepn of hollow high-strength light-modulus polyethylene fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2006100290315A CN100441753C (en) 2006-07-18 2006-07-18 Prepn of hollow high-strength light-modulus polyethylene fiber

Publications (2)

Publication Number Publication Date
CN1888153A CN1888153A (en) 2007-01-03
CN100441753C true CN100441753C (en) 2008-12-10

Family

ID=37577440

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2006100290315A Active CN100441753C (en) 2006-07-18 2006-07-18 Prepn of hollow high-strength light-modulus polyethylene fiber

Country Status (1)

Country Link
CN (1) CN100441753C (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100519847C (en) * 2007-02-12 2009-07-29 北京特斯顿新材料技术发展有限公司 Method for drying extractant during production of superhigh-molecular weight polyvinyl fibre
CN101230499B (en) * 2008-02-26 2010-10-06 山东爱地高分子材料有限公司 Coloured high-strength polyethylene fibre and method for manufacturing same
CN101575742B (en) * 2008-05-05 2011-01-26 宁波荣溢化纤科技有限公司 Preparation method of ultra-high molecular weight polyethylene fiber
CN101575756B (en) * 2008-05-05 2011-01-26 宁波荣溢化纤科技有限公司 Stretching method of ultra-high molecular weight polyethylene precursor fiber
CN101591813B (en) * 2008-05-27 2011-02-09 宁波荣溢化纤科技有限公司 Method for manufacturing super high molecular polyethylene fiber precursor
CN101629331B (en) * 2008-07-17 2011-01-26 宁波荣溢化纤科技有限公司 Method for drawing ultra-high molecular weight polyethylene fiber
CN101775666B (en) * 2010-01-22 2011-07-27 东华大学 Preparation method of high-strength high-modulus polyethylene fiber
CN101886298B (en) * 2010-06-23 2013-05-08 东华大学 Preparation method of ultra-high molecular weight polyethylene monofilaments
CN101962819B (en) * 2010-09-13 2012-07-18 杭州翔盛高强纤维材料股份有限公司 Ultrawhite ultrahigh-molecular weight ultrahigh-modulus polyethylene fibers and preparation process thereof
CN102154749B (en) * 2011-04-20 2013-01-02 东华大学 Preparation method of coarse denier ultrahigh molecular weight polyethylene (UHMWPE) fiber yarn
CN114481343A (en) * 2020-10-23 2022-05-13 中国石油化工股份有限公司 Fiber spinning method and polyethylene spinning fiber
CN116351097B (en) * 2023-04-12 2024-01-23 浙江蓝德能源科技发展有限公司 Extractant for ultra-high molecular weight PE fibers and diaphragms and preparation and application methods thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1056544A (en) * 1990-05-14 1991-11-27 中国纺织大学 The preparation method of high-strength, high-modulus polyethylene fiber
JP2001087636A (en) * 1999-09-21 2001-04-03 Asahi Kasei Corp Method for production of hollow fiber porous membrane made of polyethylene
CN1405367A (en) * 2001-08-13 2003-03-26 中纺投资发展股份有限公司 Method for preparing extra high molecular polyethylene high-concentrated solution for spinning
CN1425811A (en) * 2002-12-27 2003-06-25 东华大学 Extracting and drying process for superhigh relative molecular weight polyvinyl gel fibre
KR20040077322A (en) * 2003-02-28 2004-09-04 주식회사 케이엠에스 Preparation of asymmetric polyethylene hollow fiber membrane having high strength

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1056544A (en) * 1990-05-14 1991-11-27 中国纺织大学 The preparation method of high-strength, high-modulus polyethylene fiber
JP2001087636A (en) * 1999-09-21 2001-04-03 Asahi Kasei Corp Method for production of hollow fiber porous membrane made of polyethylene
CN1405367A (en) * 2001-08-13 2003-03-26 中纺投资发展股份有限公司 Method for preparing extra high molecular polyethylene high-concentrated solution for spinning
CN1425811A (en) * 2002-12-27 2003-06-25 东华大学 Extracting and drying process for superhigh relative molecular weight polyvinyl gel fibre
KR20040077322A (en) * 2003-02-28 2004-09-04 주식회사 케이엠에스 Preparation of asymmetric polyethylene hollow fiber membrane having high strength

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
中空纤维制备技术及其应用. 张春燕,于俊荣,刘兆峰.合成纤维,第2004年第6期. 2004
中空纤维制备技术及其应用. 张春燕,于俊荣,刘兆峰.合成纤维,第2004年第6期. 2004 *
化工原料. 中华人民共和国商业部化工原料贸易局,41,北京出版社. 1958
化工原料. 中华人民共和国商业部化工原料贸易局,41,北京出版社. 1958 *
抗氧剂在UHMWPE溶解过程中的作用. 铉晓群,潘婉莲,于俊荣,刘兆峰.合成纤维工业,第29卷第2期. 2006
抗氧剂在UHMWPE溶解过程中的作用. 铉晓群,潘婉莲,于俊荣,刘兆峰.合成纤维工业,第29卷第2期. 2006 *
超高分子量聚乙烯冻胶纺工艺及机理的探讨. 杨年慈,刘兆峰,张安秋,吴宗铨.合成纤维,第1991年第1期. 1991
超高分子量聚乙烯冻胶纺工艺及机理的探讨. 杨年慈,刘兆峰,张安秋,吴宗铨.合成纤维,第1991年第1期. 1991 *

Also Published As

Publication number Publication date
CN1888153A (en) 2007-01-03

Similar Documents

Publication Publication Date Title
CN100441753C (en) Prepn of hollow high-strength light-modulus polyethylene fiber
US10450676B2 (en) High tenacity high modulus UHMWPE fiber and the process of making
TWI523992B (en) Enhanced ballistic performance of polymer fibers
CA2404449C (en) High tenacity, high modulus filament
US9365953B2 (en) Ultra-high strength UHMWPE fibers and products
WO2006124825A2 (en) Laminated felt articles
CN101307507A (en) High-strength high-modulo ultra-high molecular weight polyethylene hollow flat fiber preparation method
CN108004605A (en) Strong porous superhigh molecular weight polyethylene fibers and preparation method in one kind
CN101289765A (en) Method for preparing hollow northylen of ultra-high relative molecular mass
CN109181300B (en) Bulletproof wall composite material and preparation method thereof
Koohestani et al. Advanced bulletproof and stab-and spike-resistant textiles
CN207435595U (en) A kind of terylene spinneret with disloyalty C-shaped spinneret orifice
CN104404640A (en) Ultra-high-molecular-weight polyethylene protofilament drafting method
CN102154749A (en) Preparation method of coarse denier ultrahigh molecular weight polyethylene (UHMWPE) fiber yarn
CN101307508A (en) High-strength high-modulo ultra-high molecular weight polyethylene hollow flat fiber preparation method
CN208704542U (en) Bulletproof halmet of composite material
CN108396400B (en) Preparation method for differentiated high-strength high-modulus polyethylene fiber by melt spinning
CN103132161A (en) Fine-diameter stretching combined spinneret orifice
CN101487145A (en) Flame-retardant moisture-conducting terylene fibre, as well as preparation method and application thereof
CN104195658A (en) UHMWPP and UHMWPE sheath-core composite fiber, special device and spinning method thereof
CN116499310B (en) Multifunctional stab-resistant garment
Dimeski et al. Resin content and molding pressure influence on ballistic properties and trauma effect of aromatic amide fibers composites
CN115323518A (en) Preparation method of ultra-high molecular weight polyethylene fiber
RU2247308C1 (en) Bullet slug
CN101302662A (en) Method for manufacturing negative oxygen ion fiber with cross-shaped section

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant