CN102585285A - Recovery method of silk glue and silk glue - Google Patents
Recovery method of silk glue and silk glue Download PDFInfo
- Publication number
- CN102585285A CN102585285A CN2012100143167A CN201210014316A CN102585285A CN 102585285 A CN102585285 A CN 102585285A CN 2012100143167 A CN2012100143167 A CN 2012100143167A CN 201210014316 A CN201210014316 A CN 201210014316A CN 102585285 A CN102585285 A CN 102585285A
- Authority
- CN
- China
- Prior art keywords
- silk gum
- recovery method
- silk
- come unglued
- carried out
- 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.)
- Pending
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a recovery method of silk glue. According to the recovery method, the silk glue is dissolved in a glue-removing liquid; and the glue-removing liquid is electrolyzed so as to produce silk glue precipitate. The invention also discloses the silk glue. According to the invention, equipment used in the recovery method is simple, the operability is good and the silk glue extraction rate is high; and simultaneously, the pollution of the glue-removing liquid on environment can be effectively reduced.
Description
Technical field
The present invention is applied to field of textiles, is specifically related to a kind of recovery method and thus obtained silk gum that is dissolved in the silk gum in the come unglued liquid.
Background technology
China's silk silk fabric industrial scale ranks first in the world, and produces per year about silk cocoon 500,000 t, more than raw silk 70,000 t, accounts for 80% and 60% of world production total amount, and silk output accounts for about 45% of Gross World Product.Along with deepening continuously and i.e. " eastern Sang Xiyi " enforcement that waits of regional industry adjustment of China's development of the West Regions, numerous filature enterprises is by the west area transfer upcountry of coastal, riverine developed regions.But; Silk mill to development this area economy, for improve local people live make contributions in, it also can produce the high concentrated organic wastewater that contains sericin in a large number in the throwing process, like the not treated river course that directly enters; With the dissolved oxygen in the consume water in large quantities; The COD severe overweight that causes water destroys the water quality of original water, and local natural water is caused certain pollution; The contained sericin with very big economic worth also runs off thereupon in the waste water simultaneously, causes the serious waste of resource.According to the data report, China is annual to produce among about 100,000 t of silkworm raw silk, just has the sericine of ten thousand tons of 2-3 to run off with waste water, resource loss rate about 25%.
Silk is mainly formed by accounting for 70%～80% fibroin and being coated on fibroin peripheral account for 20%～30% silk gum and a spot of wax and inorganics.
Coming unstuck refers to the silk gum of removing silk, thus make the silk more soft smooth and be more suitable for follow-up processing (as the spinning and dyeing) operation.
The solution that comes unstuck of the generating step of coming unstuck has very high content of silk gum, and in view of its very high organic content, it must pass through purifying treatment, to meet before being discharged at it and the relevant legal provisions of trade refuse discharging.
Summary of the invention
To the deficiency of prior art, the technical problem that the present invention solves provides a kind of recovery method and silk gum thereof of silk gum, and this recovery method equipment used is fairly simple, operability good, and extraction efficiency is high, can also reduce the pollution of come unglued liquid to environment simultaneously.
For solving the problems of the technologies described above, technical scheme of the present invention is achieved in that a kind of recovery method of silk gum, and said silk gum is dissolved in the come unglued liquid, especially, said come unglued liquid experience electrolysis step, electrolysis step produces the silk gum throw out.
Preferably, in the recovery method of above-mentioned silk gum, said recovery method specifically comprises the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out electrolysis, obtain the silk gum throw out;
(3) extract the silk gum throw out;
(4) the silk gum throw out is carried out purifying and drying, obtain silk gum.
Preferably, in the recovery method of above-mentioned silk gum, said recovery method specifically comprises the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out purifying;
(3) come unglued liquid behind the purifying is carried out electrolysis, obtain the silk gum throw out;
(4) the silk gum throw out is carried out drying, obtain silk gum.
Preferably, in the recovery method of above-mentioned silk gum, the electrode materials that adopts in the electrolysis step is graphite or titanium.
Preferably, in the recovery method of above-mentioned silk gum, the voltage that applies in the electrolysis step is 20～50V.
Preferably, in the recovery method of above-mentioned silk gum, the voltage that applies in the electrolysis step is 25～30V.
Correspondingly, the invention also discloses a kind of silk gum, especially, said silk gum is to obtain according to above-mentioned method.
The invention provides a kind of new method and be dissolved in the silk gum in the come unglued liquid with recovery, it obtains the silk gum throw out through come unglued liquid being carried out electrolysis, and then extracts silk gum.This recovery method equipment used is fairly simple, operability good, and extraction efficiency is high, simultaneously, can also effectively reduce the pollution of come unglued liquid to environment.
Description of drawings
In order to be illustrated more clearly in the embodiment of the invention or technical scheme of the prior art; To do to introduce simply to the accompanying drawing of required use in embodiment or the description of the Prior Art below; Obviously, the accompanying drawing in describing below only is some embodiments of the present invention, for those of ordinary skills; Under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Shown in Figure 1 for reclaiming the process flow diagram that is dissolved in the silk gum method in the come unglued liquid in the embodiment of the invention 1;
Shown in Figure 2 for reclaiming the process flow diagram that is dissolved in the silk gum method in the come unglued liquid in the embodiment of the invention 2.
The method that provides for the embodiment of the invention 2 shown in Figure 3 reclaims the uv absorption spectra of gained sericin;
The method that provides for the embodiment of the invention 2 shown in Figure 4 reclaims the infrared absorpting light spectra of gained sericin;
The method that provides for the embodiment of the invention 1 and 2 shown in Figure 5 is at same voltage (25V), the change curve map of different time points (0-60min) silk gum extraction yield;
The method that provides for the embodiment of the invention 2 shown in Figure 6 is at same added electric field time (2h), the change curve of silk gum extraction yield under the different voltage conditions.
Embodiment
Carry out clear, intactly description in the face of the technical scheme in the embodiment of the invention down, obviously, described embodiment only is the present invention's part embodiment, rather than whole embodiment.Based on the embodiment among the present invention, those of ordinary skills are not making the every other embodiment that is obtained under the creative work prerequisite, all belong to the scope of the present invention's protection.
The embodiment of the invention discloses a kind of recovery method that is dissolved in the silk gum in the come unglued liquid, said come unglued liquid experience electrolysis step, electrolysis step produces the silk gum throw out.
The principle that adopts electrolysis to obtain silk gum is: sericin is a kind of macromolecular compound; Its molecular weight is bigger; Particle diameter is at 1～100nm, because particle size is in the scope of colloidal particle, thereby demonstrates the distinctive dialysis of colloidal sol, cohesion, gelling and peptizing property.Sericin contains carboxyl and amino freely, can interact and forms bipolar ion, has amphoteric properties, and in the less solution of pH value, sericin exists with the positive ion form; At the bigger solution of pH value, sericin exists with the negative ion form.The iso-electric point of sericin is 3.8-4.5.Silk gum solution PH after coming unstuck under the alkaline condition is 8～11, so sericin is electronegative in the solution, after the added electric field, assembles near the rapid anode of electronegative sericin, and produces a large amount of white flocculence materials, coagulation gradually rapidly.Solution produces tangible demixing phenomenon, the upper solution clarification that becomes.
The purpose of coming unstuck is to remove to be wrapped in its outer field silk gum, wax fat, pigment etc.Degumming agent commonly used has the compound of soap, proteolytic ferment, tensio-active agent; Used alkaline agent has sodium hydroxide, yellow soda ash, water glass etc.
In the above-mentioned recovery method that is dissolved in the silk gum in the come unglued liquid, said recovery method specifically comprises the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out electrolysis, obtain the silk gum throw out;
(3) extract the silk gum throw out;
(4) the silk gum throw out is carried out purifying and drying, obtain silk gum.
In the above-mentioned recovery method that is dissolved in the silk gum in the come unglued liquid, said recovery method can also comprise the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out purifying;
(3) come unglued liquid behind the purifying is carried out electrolysis, obtain the silk gum throw out;
(4) the silk gum throw out is carried out drying, obtain silk gum.
Just the process of filter is in order to remove tangible impurity in the come unglued liquid.The process of purifying is to realize desalination through means such as dialysis.
Preferably, in the above-mentioned recovery method that is dissolved in the silk gum in the come unglued liquid, the electrode materials that adopts in the electrolysis is graphite or titanium.
Preferably, in the above-mentioned recovery method that is dissolved in the silk gum in the come unglued liquid, the voltage that applies in the electrolysis step is 20～50V.Preferred, the voltage that applies is 25V～30V.
Correspondingly, the invention also discloses a kind of silk gum, especially, said silk gum is to obtain according to above-mentioned recovery method.
In order to further specify technical scheme of the present invention; Below in conjunction with embodiment the preferred embodiment of the invention is described; Describe just to further specifying feature and advantage of the present invention but should be appreciated that these, rather than to the restriction of claim of the present invention.
Embodiment 1
Join shown in Figure 1ly, the recovery method that is dissolved in the silk gum in the come unglued liquid is realized through following laboratory facilities:
(1) extracts trade effluent (come unglued liquid) and place container, trade effluent is tentatively filtered, remove tangible impurity;
(2) negative electrode graphite rod and the graphite anode rod that diameter is 4mm is inserted into just in the filterable waste water, applies voltage 25V, and electrolysis time is 1 hour; Can find in the electrolysis, produce a large amount of white agglutinating matters near the graphite anode rod, and sink to container bottom gradually; Tangible demixing phenomenon appears in solution; After reaction finishes, leave standstill and treat that the solution layering is stable, wherein top liquid is supernatant;
(3) remove supernatant, extract sedimentable matter;
(4) sedimentable matter is carried out purifying,, remove materials such as yellow soda ash,, obtain the powder of white then through drying treatment to realize concentrating and desalinating.
Powder to white among the embodiment 1 detects, and can know that this powder is a silk gum.
Embodiment 2
Join shown in Figure 2ly, the recovery method that is dissolved in the silk gum in the come unglued liquid is realized through following laboratory facilities:
(1) extracts trade effluent (come unglued liquid) and place container, trade effluent is tentatively filtered, remove tangible impurity;
(2) further the waste water after filtering is carried out purifying,, remove materials such as yellow soda ash to realize desalination;
(3) negative electrode graphite rod and the graphite anode rod that diameter is 4mm is inserted in the waste water behind the purifying, applies voltage 25V, and electrolysis time is 2 hours; Can find in the electrolysis, produce a large amount of white agglutinating matters near the graphite anode rod, and sink to container bottom gradually; Tangible demixing phenomenon appears in solution; After reaction finishes, leave standstill and treat that the solution layering is stable, wherein top liquid is supernatant;
(4) remove supernatant, extract sedimentable matter;
(5) sedimentable matter is carried out drying treatment, obtain the powder of white.
Ginseng Fig. 3 and shown in Figure 4 carries out spectroscopic analysis to the white powder among the embodiment 2, can know that this powder is a sericin.
Join shown in Figure 5ly, the method that provides for embodiment 1 and 2 is at same voltage (25V), the change curve map of different time points (0-60min) silk gum extraction yield.Can be known that by Fig. 5 the method effect of embodiment 2 is obvious relatively, extraction yield is than higher.
Among the embodiment 2, the voltage that applies in the step (3) is changed into 8V, 10V, 15V, 20V and 30V respectively and tests again, other conditions are constant.
Join shown in Figure 6ly, the method that provides for embodiment 2 is at same added electric field time (2h), the change curve of silk gum extraction yield under the different voltage conditions.Can know that by Fig. 6 when voltage reached 25～30V, about the extraction rate reached to 70% of silk gum, extraction yield was higher.
In sum, beneficial effect of the present invention is:
(1) obtains the silk gum throw out through come unglued liquid being carried out electrolysis, and then extract silk gum.Electrolytic appointed condition only need be used to hold waste water container, be located at the anodic-cathodic at container two ends and put on the dipolar voltage of negative and positive, container can be the pond that is built into through cement in practical application, so this recovery method equipment used is fairly simple; When the waste water in container carries out electrolysis simultaneously, can directly realize that through unlatching and the closure of controlling electric field operability is good; Under effect of electric field, can silk gum be precipitated fast, so the silk gum extraction yield that this method obtains is high.
(2) after the silk gum in the waste water is extracted; Can effectively reduce the pollution of waste water, can the silk gum that reclaim be applied to put in order behind the health-care textile thing inhibitor and the medicine material of coating, makeup beautifying nourishing additive and oils food again, enterprise's consumption reduction is taped the latent power environment; Economize on resources; Refuse reclamation, it is significant with comprehensive social benefit to improve self economic benefit, so this method has the wide development prospect.
(3) can be known by Fig. 5 and Fig. 6, utilize the method for technical scheme of the present invention, the silk gum extraction yield is high.
To those skilled in the art, obviously the invention is not restricted to the details of above-mentioned example embodiment, and under the situation that does not deviate from spirit of the present invention or essential characteristic, can realize the present invention with other specific form.Therefore; No matter from which point; All should regard embodiment as exemplary; And be nonrestrictive, scope of the present invention is limited accompanying claims rather than above-mentioned explanation, therefore is intended to the implication of the equivalents that drops on claim and all changes in the scope are included in the present invention.Should any Reference numeral in the claim be regarded as limit related claim.
In addition; Describing according to embodiment though should be appreciated that this specification sheets, is not that each embodiment only comprises an independently technical scheme; This narrating mode of specification sheets only is for clarity sake; Those skilled in the art should make specification sheets as a whole, and the technical scheme among each embodiment also can form other embodiments that it will be appreciated by those skilled in the art that through appropriate combination.
Claims (7)
1. the recovery method of a silk gum, said silk gum is dissolved in the come unglued liquid, it is characterized in that, said come unglued liquid experience electrolysis step, electrolysis step produces the silk gum throw out.
2. the recovery method of silk gum according to claim 1 is characterized in that, said recovery method specifically comprises the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out electrolysis, obtain the silk gum throw out;
(3) extract the silk gum throw out;
(4) the silk gum throw out is carried out purifying and drying, obtain silk gum.
3. the recovery method of silk gum according to claim 1 is characterized in that, said recovery method specifically comprises the steps:
(1) come unglued liquid is carried out filter just;
(2) first filter back come unglued liquid is carried out purifying;
(3) come unglued liquid behind the purifying is carried out electrolysis, obtain the silk gum throw out;
(4) the silk gum throw out is carried out drying, obtain silk gum.
4. the recovery method of silk gum according to claim 1 is characterized in that, the electrode materials that adopts in the electrolysis step is graphite or titanium.
5. the recovery method of silk gum according to claim 1 is characterized in that, the voltage that applies in the electrolysis step is 20～50V.
6. the recovery method of silk gum according to claim 5 is characterized in that, the voltage that applies in the electrolysis step is 25～30V.
7. a silk gum is characterized in that, said silk gum obtains according to any described method of claim 1 to 6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100143167A CN102585285A (en) | 2012-01-17 | 2012-01-17 | Recovery method of silk glue and silk glue |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012100143167A CN102585285A (en) | 2012-01-17 | 2012-01-17 | Recovery method of silk glue and silk glue |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102585285A true CN102585285A (en) | 2012-07-18 |
Family
ID=46474566
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012100143167A Pending CN102585285A (en) | 2012-01-17 | 2012-01-17 | Recovery method of silk glue and silk glue |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102585285A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103242440A (en) * | 2013-05-03 | 2013-08-14 | 广西立盛茧丝绸有限公司 | Sericin extracting method |
| CN107176987A (en) * | 2017-07-14 | 2017-09-19 | 重庆市畜牧科学院 | The method and device of Silk Reeling Waste Liquor recovery purifying sericin |
| CN108164059A (en) * | 2018-01-30 | 2018-06-15 | 浙江工业大学膜分离与水处理协同创新中心湖州研究院 | A kind of embrane method processing cocoon boiling wastewater and the method for recycling sericin |
| CN108409847A (en) * | 2018-03-05 | 2018-08-17 | 苏州先蚕丝绸有限公司 | A kind of recovery method of silk silk gum |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003165843A (en) * | 2001-11-29 | 2003-06-10 | Okamoto Lace Kk | Method for extracting sericin, the extract solution and method for modifying fiber or fabric |
| JP2003342870A (en) * | 2002-05-24 | 2003-12-03 | Toshio Hagiwara | Degumming of silk with reducing alkali ion water |
| CN101857320A (en) * | 2010-05-25 | 2010-10-13 | 苏州大学 | Method for treatment of silk degumming wastewater and recovery of silk gum |
-
2012
- 2012-01-17 CN CN2012100143167A patent/CN102585285A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003165843A (en) * | 2001-11-29 | 2003-06-10 | Okamoto Lace Kk | Method for extracting sericin, the extract solution and method for modifying fiber or fabric |
| JP2003342870A (en) * | 2002-05-24 | 2003-12-03 | Toshio Hagiwara | Degumming of silk with reducing alkali ion water |
| CN101857320A (en) * | 2010-05-25 | 2010-10-13 | 苏州大学 | Method for treatment of silk degumming wastewater and recovery of silk gum |
Non-Patent Citations (2)
| Title |
|---|
| 《苏州丝绸工学院学报》 19901001 杨百春等 "真丝绸精练工艺的监测与控制" 第15～21页 1－7 第10卷, 第3期 * |
| 杨百春等: ""真丝绸精练工艺的监测与控制"", 《苏州丝绸工学院学报》, vol. 10, no. 3, 1 October 1990 (1990-10-01), pages 15 - 21 * |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103242440A (en) * | 2013-05-03 | 2013-08-14 | 广西立盛茧丝绸有限公司 | Sericin extracting method |
| CN103242440B (en) * | 2013-05-03 | 2015-09-16 | 广西立盛茧丝绸有限公司 | A kind of Extraction Method for Sericin |
| CN107176987A (en) * | 2017-07-14 | 2017-09-19 | 重庆市畜牧科学院 | The method and device of Silk Reeling Waste Liquor recovery purifying sericin |
| CN108164059A (en) * | 2018-01-30 | 2018-06-15 | 浙江工业大学膜分离与水处理协同创新中心湖州研究院 | A kind of embrane method processing cocoon boiling wastewater and the method for recycling sericin |
| CN108409847A (en) * | 2018-03-05 | 2018-08-17 | 苏州先蚕丝绸有限公司 | A kind of recovery method of silk silk gum |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Udom et al. | Harvesting microalgae grown on wastewater | |
| CN102585285A (en) | Recovery method of silk glue and silk glue | |
| CN103172196A (en) | Treatment and recycling technology of white water in production of paper-making reconstituted tobacco | |
| CN102668760A (en) | Method and device for governing saline-alkali soil | |
| CN102399040A (en) | Comprehensive treatment process for sulfur dye wastewater | |
| CN102757138B (en) | Seawater desalination treatment method adopting combination of wind energy power generation and salt chemical industry | |
| CN205204934U (en) | Multistage formula reverse osmosis seawater desalts system | |
| CN104193051A (en) | Deep purification treatment method for printing ink wastewater | |
| CN110734185A (en) | sulfonated mud wastewater treatment method and system | |
| CN103723849A (en) | Process and device for recovering Fe(OH)2 and Na2SO4 from ferric oxide stain material wastewater concentration system | |
| CN106348562A (en) | Method for treating active sludge generated by sewage treatment and extracting protein | |
| CN102351364B (en) | Treatment method of wood chip washing waste water | |
| CN103553283A (en) | Novel process for treating wastewater in tea deep processing industry | |
| CN103319023A (en) | Process and system for treatment of ceramic processing wastewater | |
| CN104276687B (en) | A kind of method of animal protein feed in recycling casing processing-waste | |
| CN107265798A (en) | A kind of method for sludge treatment | |
| CN110642435A (en) | Clean treatment system and method for ASP flooding oil extraction wastewater | |
| CN206666261U (en) | A kind of viscose fiber acid waste water processing unit | |
| Giwa et al. | Textile wastewater treatment using sodom apple (calotropis procera)-aided tamarind seed as a coagulant | |
| CN202988897U (en) | Coal-bearing wastewater treatment device | |
| CN103387313A (en) | Method for treating cellulosic ethanol waste water | |
| CN113200647A (en) | Method and system for treating oil field wastewater by electrocatalytic oxidation | |
| CN105523664A (en) | Algin production wastewater pretreatment method | |
| CN105399248A (en) | Treating process and treating system for sewage of concentrating plant or sand producing plant | |
| CN102417270A (en) | Printing and dyeing wastewater treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20120718 |