CN1403643A - Composite kerating fiber and its production process - Google Patents
Composite kerating fiber and its production process Download PDFInfo
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- CN1403643A CN1403643A CN 01128117 CN01128117A CN1403643A CN 1403643 A CN1403643 A CN 1403643A CN 01128117 CN01128117 CN 01128117 CN 01128117 A CN01128117 A CN 01128117A CN 1403643 A CN1403643 A CN 1403643A
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Abstract
The composite keratin fiber consists of hair keratin in 15-60 wt% and PVA in 40-85 wt%. The production process includes treating hair keratin with Na2S solution to denature via destroying its disulfide bond; dissolving the denatured keratin in pH 9-13.5 NaOH solution to a concentration of 10-20 wt%; water washing and dissolving PVA into 10-20 wt% water solution; mixing the keratin solution; PVA solution and grafting agent for grafting copolymerization to prepare the spinning liquid; and wet spinning in a vinylon producing equipment.
Description
The present invention relates to a kind of method of making composite kerating fiber with hair-keratin and polyvinyl alcohol.
Utilize the native protein azlon, proposed several different methods at present.Spinning the milk protein silk of being called of company exploitation " Star ノ Application " (glad according to) fiber as Japanese Japan, is the composite fibre by the acrylonitrile compolymer of the milk casein of about 40wt% and 60wt%.China's publication and for example provides respectively in the application number 95111366.6,96116532.4,94114071.7 with pupa albumen, milk protein and fibroin and the blend of synthetic high polymer raw material propylene nitrile, acrylamide or polyacrylonitrile, the manufacture method of copolymerized fiber.Also having with the glycinin in addition is the method for raw material production soybean protein composite fibre.
The protein raw material source of above-mentioned protein composite fibre is silkworm chrysalis, milk, soybean meal.These protein raw materials are protein sources that human and animal's body weight is wanted, and they have very high use value and economic worth, use it for the production of protein fibre, and not only cost is higher, also are the wastes to the good protein raw material resources.
The invention provides a kind of is raw material with the hair-keratin, produces the method for composite kerating fiber.Can utilize animal wool (as: pig hair, horsehair, ox hair, wool etc.), poultry feather and people to send out and be raw material.Raw material is worth low, and the source is wide.10-20% can reduce production costs.
The method of the manufacturing composite kerating fiber that the present invention relates to comprises: (1), hair impurity and purification; (2), vulcanizing treatment makes keratinous degeneration; (3), denatured keratin is dissolved in the alkaline aqueous solution; (4), the spinning solution of spinnability is made in keratin and polyvinyl alcohol graft copolymerized copolymerization; (5), make composite kerating fiber with wet spinning.
It is necessary at first the raw material hair being purified.With hand picking or mechanical grading, remove sandstone, metal and bigger smoits in the hair; Cut into the 3-5 millimeter; , under 40-70 ℃ of condition, press hair and mixed agitator treating 30-60 minute with the soda ash solution weight ratio in 1: 10 to 1: 15 with the soda ash solution of 5-10wt%; Filter out hair, dry the hair that must purify with hair weight 2-3 water flushing back doubly.
The hair that purifies is added in the reaction vessel, added the Na of 1-3wt% by weight 1: 10 to 1: 15
2S solution; Under 20-50 ℃ of condition, reacted 10 minutes to 4 hours, disulfide bond, salt type bond in the keratin molecule are opened, generate the sulfuration keratin, keratic network structure is loosened.The PH that adjusts mixed liquor with dilute NaOH solution is 9-13.5, is heated to 60-80 ℃, and stirring reaction 30 minutes to 2 hours dissolves hair-keratin fully.Filter with four layers of stainless (steel) wire of 50,200,200,50 purposes.Filtrate adds in the closed container, under 30-50 ℃, slowly adds alkene hydrochloric acid while stirring, and adjustment PH is 4.5-5.0, and keratin is gone out at isoelectric point sinking precipitation.Na in the while solution
2S generates H under acid condition
2S gas is derived by blast pipe, recycles with NaOH solution.The keratin that generates precipitates static 2-4 hour, and the venting supernatant liquor filters with two layers of Kanakin, and centrifuge dripping obtains the keratin of regenerating.
Measuring the keratic moisture content of regeneration, add deionized water as calculated, is 10-20wt% with dilute NaOH solution furnishing keratin content, PH is the mixed liquor of 9-13.5, and add an amount of disulfide bond blocking agent, and be heated to 60-100 ℃, be stirred to keratin and dissolve fully.Wherein available disulfide bond blocking agent and consumption thereof are cysteine 3-30mg/kg keratin or mercaptoethanol 4-400mg/kg keratin.
The polyvinyl alcohol water solution of 10-20% washed, dissolves, is mixed with by polyvinyl alcohol according to the known vinylon production technology in synthetic fiber field.
With the poly-vinyl alcohol solution of dissolving, after filtration, send into another closed reactor, stir and slowly add the cyanogen bromide (BrCN) of polyvinyl alcohol dry weight 0.5-2%, reacted 10-30 minute.It is (20-50) with above-mentioned keratin solution in keratin and polyvinyl alcohol weight ratio then: ratio (50-80), add in the poly-vinyl alcohol solution after filtration, stirring also is heated to 98 ± 2 ℃, continues to stir 1-2 hour, makes keratin and polyvinyl alcohol graft copolymerized copolymerization.Reaction equation is:
With blend, the copolymerized solution of keratin and polyvinyl alcohol, the footpath is filtered and to be sent into deaerator, and is static and keep 98 ± 2 ℃ of temperature, deaeration 6-10 hour, makes the spinning solution of spinnability.
Filtration in the said process when small scale experiments, can be used candle filter or dish-shaped filter; Use plate and frame type filter-press during industrial production.Its filtering material uses three layers of polyvinyl single-side pile and one deck Kanakin.
Spinning solution after the deaeration can utilize the spinning process method and apparatus of the known vinylon in synthetic fiber field to carry out spinning, drawing-off, dryness finalization, acetalation arrangement, makes keratin and polyvinyl alcohol composite fiber.
Characteristics of the present invention are: cheap, the wide material sources of keratin cost of material: the composite fibre of generation has good hygroscopicity, gas permeability and dyeability, comfortable and easy to wear smooth, skin-friendly is good: the production equipment that can make full use of domestic vinylon plant, suitably increase keratolysis equipment, can produce after the transformation, small investment, instant effect.
Present invention will be further described for following example, but can not think to limit scope of invention.In these examples, deal and percentage are by weight, unless other explanation is arranged.
Example one
Sandstone, metal and the bigger smoits in the wool are removed in hand picking.Take by weighing the 1kg wool, cut into 5 millimeters, 15 liters of the soda ash solutions of adding 5%, under 60 ℃ of conditions, agitator treating 60 minutes filters out wool, dries the wool that must purify with 3 premium on currency flushing back.
The wool that purifies is added in the reaction vessel, add 1.5% Na
215 liters of S solution at room temperature reacted 2 hours, and disulfide bond, salt type bond in the keratin molecule are opened, and generated the sulfuration keratin, and keratic network structure is loosened.The PH that adjusts mixed liquor with dilute NaOH solution is 11-12, is heated to 60 ℃, and stirring reaction 1 hour dissolves hair-keratin fully.Filter with four layers of stainless (steel) wire of 50,200,200,50 purposes.Filtrate adds in the closed container, under 30-50 ℃, slowly adds watery hydrochloric acid while stirring, and adjustment PH is 4.5-5.0, and keratin is gone out at isoelectric point sinking precipitation.Na in the while solution
2S generates H under acid condition
2S gas is derived by blast pipe, recycles with NaOH solution.The keratin that generates precipitates static 2 hours, discharges supernatant liquor, filter with two layers of Kanakin, and centrifuge dripping, the keratin 2.3kg that obtains regenerating, average moisture content is 68 ± 2% after measured.
In the 2.3kg keratin, add the 2.3kg deionized water as calculated, furnishing keratin content is 16% mixed liquor, transferring PH with dilute NaOH solution is 11-12, add disulfide bond blocking agent cysteine 7mg, be heated to 95 ± 5 ℃, be stirred to keratin and dissolve fully, make the keratin solution of 15-16%.
Take by weighing the 1.87kg polyvinyl alcohol, wash, dissolve, be mixed with the polyvinyl alcohol water solution of 15-16% according to the known vinylon production technology in synthetic fiber field.
With poly-vinyl alcohol solution, after filtration, send into another closed reactor, stir and slowly add the cyanogen bromide (BrCN) of 25 grams, reacted 30 minutes.Then above-mentioned keratin solution is added in the poly-vinyl alcohol solution after filtration, stirred 30 minutes, be heated to 98 ± 2 ℃, continue to stir 1 hour, make keratin and polyvinyl alcohol graft copolymerization.It is ellipse to send into deaeration more after filtration, static and keep 98 ± 2 ℃ of temperature, and the spinning solution of spinnability is made in deaeration 8 hours.Wherein keratin content is about 30%, and polyvinyl alcohol content is about 70%.
Spinning solution after the deaeration can utilize the spinning process method and apparatus of the known vinylon in synthetic fiber field to carry out spinning, drawing-off, dryness finalization, acetalation arrangement, makes keratin and polyvinyl alcohol composite fiber.Its main performance index is: filament number 0.5-2.0dtex, and in fracture strength 3.0-4.0CN/dtex, dried elongation at break 15-20%, regain 7-12%, dyeability is better than silk and polyvinyl alcohol, and hot water resistance reaches more than 115 ℃.
Real row two
Take by weighing the pig hair 1kg that removes impurity, cut into 5 millimeters, add 3% Na
210 liters of S solution at room temperature reacted 4 hours, and disulfide bond, salt type bond in the keratin molecule are opened, and generated the sulfuration keratin.Other process is identical with example one.
This example and example one are different is to be raw material with the pig hair.According to the difference of hair kind, can suitably adjust Na
2The concentration of S solution, reaction temperature and time.
Example three
What this example and example one were different is, the mixed proportion that makes keratin solution and poly-vinyl alcohol solution is 50: 50, i.e. keratin content 50% in composite fibre, polyvinyl alcohol content 50%.Other process is identical with example one.
Compare with the product of example one, because the raising of protein content, hygroscopicity, the dyeability of fiber further improve, but the dried fracture strength of fiber drops to 2.0-3.0CN/dtex.
Claims (8)
1, composite kerating fiber is characterized in that it is formed by hair-keratin raw material and the graft copolymerization of polyvinyl alcohol raw material, and above by weight percentage two raw materials respectively account for following ratio: keratin 15-60, polyvinyl alcohol 40-85.
2, according to claim 1, the hair-keratin raw material comprises: animal wool (as pig hair, horsehair, ox hair, wool etc.), poultry feather and people send out.
3, the manufacture method of composite kerating fiber, the hair-keratin after it is characterized in that purifying makes keratinous degeneration through vulcanizing treatment: under the protection of disulfide bond blocking agent denatured keratin is dissolved in the alkaline aqueous solution; Keratin and polyvinyl alcohol graft copolymerized copolymerization: make keratin bicomponent filament yarn or staple fibre with wet spinning.
4, method according to claim 3, the sulfurization of denatured process is characterized in that: the operating weight percent concentration is the sodium sulfide solution of 1-5%, and keratic salt type bond and disulfide bond are opened, and destroys keratic network structure, and it is loosened.
5, method according to claim 3 is characterized in that: dilute alkaline soln, can use NaOH, and adjustment PH is 9-13.5.
6, method according to claim 3 is characterized in that: the disulfide bond blocking agent, can use mercaptoethanol, and consumption is the 4-400mg/kg keratin.
7, method according to claim 3 is characterized in that: the disulfide bond blocking agent, and can use cysteine to replace mercaptoethanol, consumption is the 3-30mg/kg keratin.
8, method according to claim 3, keratin and polyvinyl alcohol graft copolymerized copolymerization is characterized in that: can use cyanogen bromide as the graft copolymerization agent, consumption is the 1-3% of polyvinyl alcohol dry weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011281170A CN1158416C (en) | 2001-08-30 | 2001-08-30 | Composite kerating fiber and its production process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011281170A CN1158416C (en) | 2001-08-30 | 2001-08-30 | Composite kerating fiber and its production process |
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| CN1403643A true CN1403643A (en) | 2003-03-19 |
| CN1158416C CN1158416C (en) | 2004-07-21 |
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| CNB011281170A Expired - Fee Related CN1158416C (en) | 2001-08-30 | 2001-08-30 | Composite kerating fiber and its production process |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005028560A1 (en) * | 2003-09-19 | 2005-03-31 | Keratec Limited | Composite materials containing keratin |
| WO2006002572A1 (en) * | 2004-06-30 | 2006-01-12 | Guanqi Li | Synthetic fiber containing animal hair protein and its preparation |
| US7465321B2 (en) | 2001-08-31 | 2008-12-16 | Keratec Limited | Production of biopolymer film, fibre, foam and adhesive materials from soluble S-sulfonated keratin derivatives |
| CN100462487C (en) * | 2005-02-05 | 2009-02-18 | 李官奇 | Protein fiber spinning dope and its preparing method |
| US7579317B2 (en) | 2005-03-11 | 2009-08-25 | Keratec, Ltd. | Nutraceutical composition comprising soluble keratin or derivative thereof |
| US7732574B2 (en) | 2003-12-19 | 2010-06-08 | Keraplast Technologies, Ltd. | Wound care products containing keratin |
| CN101525490B (en) * | 2009-04-03 | 2010-12-08 | 东华大学 | A kind of keratin whisker reinforced natural protein composite film and preparation method thereof |
| US7892572B2 (en) | 2002-06-10 | 2011-02-22 | Keraplast Technologies, Ltd. | Orthopaedic materials derived from keratin |
| US8124735B2 (en) | 2006-12-11 | 2012-02-28 | Keraplast Technologies, Ltd. | Porous keratin construct and method of making the same |
| US8142807B2 (en) | 2006-12-06 | 2012-03-27 | Keraplast Technologies, Ltd. | Bone void fillers and methods of making the same |
| CN102465354A (en) * | 2010-11-10 | 2012-05-23 | 福建鑫华股份有限公司 | Synthetic animal protein fiber and spinning method thereof |
| CN102775489A (en) * | 2012-07-31 | 2012-11-14 | 上海全宇生物科技遂平有限公司 | Keratin solid and preparation method thereof |
| CN102817101A (en) * | 2012-07-31 | 2012-12-12 | 上海全宇生物科技遂平有限公司 | Hair keratin composite fiber and spinning method thereof |
| CN102839441A (en) * | 2012-09-25 | 2012-12-26 | 天津工业大学 | High-elasticity keratin regenerated fiber and preparation method thereof |
| CN106519146A (en) * | 2016-10-31 | 2017-03-22 | 江南大学 | Method for preparation of waste hair composite material with ionic liquid |
-
2001
- 2001-08-30 CN CNB011281170A patent/CN1158416C/en not_active Expired - Fee Related
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7465321B2 (en) | 2001-08-31 | 2008-12-16 | Keratec Limited | Production of biopolymer film, fibre, foam and adhesive materials from soluble S-sulfonated keratin derivatives |
| US7892572B2 (en) | 2002-06-10 | 2011-02-22 | Keraplast Technologies, Ltd. | Orthopaedic materials derived from keratin |
| WO2005028560A1 (en) * | 2003-09-19 | 2005-03-31 | Keratec Limited | Composite materials containing keratin |
| US7767756B2 (en) | 2003-09-19 | 2010-08-03 | Keraplast Technologies, Ltd. | Composite materials containing keratin |
| US7732574B2 (en) | 2003-12-19 | 2010-06-08 | Keraplast Technologies, Ltd. | Wound care products containing keratin |
| WO2006002572A1 (en) * | 2004-06-30 | 2006-01-12 | Guanqi Li | Synthetic fiber containing animal hair protein and its preparation |
| CN100462487C (en) * | 2005-02-05 | 2009-02-18 | 李官奇 | Protein fiber spinning dope and its preparing method |
| US7579317B2 (en) | 2005-03-11 | 2009-08-25 | Keratec, Ltd. | Nutraceutical composition comprising soluble keratin or derivative thereof |
| US8142807B2 (en) | 2006-12-06 | 2012-03-27 | Keraplast Technologies, Ltd. | Bone void fillers and methods of making the same |
| US8124735B2 (en) | 2006-12-11 | 2012-02-28 | Keraplast Technologies, Ltd. | Porous keratin construct and method of making the same |
| CN101525490B (en) * | 2009-04-03 | 2010-12-08 | 东华大学 | A kind of keratin whisker reinforced natural protein composite film and preparation method thereof |
| CN102465354A (en) * | 2010-11-10 | 2012-05-23 | 福建鑫华股份有限公司 | Synthetic animal protein fiber and spinning method thereof |
| CN102775489A (en) * | 2012-07-31 | 2012-11-14 | 上海全宇生物科技遂平有限公司 | Keratin solid and preparation method thereof |
| CN102817101A (en) * | 2012-07-31 | 2012-12-12 | 上海全宇生物科技遂平有限公司 | Hair keratin composite fiber and spinning method thereof |
| CN102817101B (en) * | 2012-07-31 | 2014-05-21 | 上海全宇生物科技遂平有限公司 | Hair keratin composite fiber and spinning method thereof |
| CN102839441A (en) * | 2012-09-25 | 2012-12-26 | 天津工业大学 | High-elasticity keratin regenerated fiber and preparation method thereof |
| CN106519146A (en) * | 2016-10-31 | 2017-03-22 | 江南大学 | Method for preparation of waste hair composite material with ionic liquid |
| CN106519146B (en) * | 2016-10-31 | 2019-06-07 | 江南大学 | A method of discarded hair composite material is prepared using ionic liquid |
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| Publication number | Publication date |
|---|---|
| CN1158416C (en) | 2004-07-21 |
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