CN101581034A - Biologically-aided totally-chlorine-free bleaching technology of flax cloth or fiber - Google Patents

Biologically-aided totally-chlorine-free bleaching technology of flax cloth or fiber Download PDF

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CN101581034A
CN101581034A CNA2008100645025A CN200810064502A CN101581034A CN 101581034 A CN101581034 A CN 101581034A CN A2008100645025 A CNA2008100645025 A CN A2008100645025A CN 200810064502 A CN200810064502 A CN 200810064502A CN 101581034 A CN101581034 A CN 101581034A
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bleaching
chlorine
sodolin
free
hydrogen peroxide
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张辉
刘波
黄文清
王柏臣
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Harbin University of Science and Technology
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Harbin University of Science and Technology
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Abstract

The invention relates to a biologically-aided totally-chlorine-free bleaching technology of flax cloth or fiber. An oxygen-contained bleaching agent generally functions on lignin far less than a chloride-contained bleaching agent, so developing a novel pollution-free method for removing lignin in cloth fibers is necessary to realize chlorine-free bleaching; the removal of the lignin is the key of effective bleaching especially for fibers such as the flax fibers containing more lignin. The biologically-aided totally-chlorine-free bleaching technology of flax cloth or fiber comprises the following steps: flax raw cloth is subjected to the alkali boiling off and acid pickling, then is subjected to the biological pretreatment and bleached by hydrogen peroxide; and the hydrogen peroxide re-bleaching process is carried out at the following conditions: 4-15g/L hydrogen peroxide, the pH value of 7-11, the bleaching temperature of 40-80 DEG C, the bath ratio of 1:5-20, and the bleaching time of 0.5-2 hours; and the whiteness of products after bleaching can reach up to more than 80 percent, the tensile strength can reach up to 500-900*800-1200N, the capillary effect is more than 8 cm, and the prior requirements of the bleaching technical indications of flax cloth are met. The invention is used for the treatment of flax cloth or fibers under the chlorine-free condition.

Description

Biological auxiliary sodolin or fiber Totally-chlorine-free bleaching technology
Technical field:
The invention belongs to the textile industry field.Be characterized in a kind of and utilize lignin in the microbial degradation sodolin (fiber), and then finish the Totally-chlorine-free bleaching technology of bleaching with hydrogen peroxide.
Background technology:
Flax is the good natural fabric of a kind of kind, has the characteristics of comfortable and easy to wear, nice and cool pleasant, good permeability, thereby at home and abroad always as the raw material of high-grade clothing and ornament and popular to people deeply.
Bleaching is the significant process during sodolin is produced, and the outward appearance and the processability of sodolin played an important role.The linum bast fiber, content of cellulose has only 70-80% in the raw ramie, contains about 25% lignin.Linen fibre after retted fibre is handled also contains the lignin of 2-5%, is higher than cotton fiber far away.Because lignin molecule is made up of dysoxidizable aromatic ring and alkyl side chain, the bleaching difficulty that makes linen fibre is much larger than cotton fiber.At present, the bleaching medicament that uses in sodolin production mainly contains two big class, chlorine bleaches and oxygen-bearing bleaching agents.Chlorine bleaches principal item has chlorine, hypochlorite, chlorite, chlorine dioxide etc.Because chlorine and hypochlorite can produce chlorine when bleaching, thereby they are called contain the elemental chlorine bleaching agent.It is fine to contain elemental chlorine bleaching agent low price, easy to use, bleaching and delignification's ability, less to the cellulose degradation ability, be class selectivity bleaching agent preferably, its application technology is also very ripe, is the main bleaching agent that uses during linen industry is produced in a very long time.
1985, the scholar of European Section detected the extremely toxic substance dioxin first from the sodium hypochlorite bleaching waste liquid, had caused people to containing the attention to the organic matter chlorination in bleaching process of elemental chlorine bleaching agent.So far the dioxin-like chemical that detected from the bleaching waste liquor of flax of scientist reaches kind more than 200, also has strong carcinogens such as chloroform, alpha-halogen aldehydes in addition.Quite a few has carcinogenic, teratogenesis sex change, causes sudden and multiple cranial nerve pathology etc. in these organohalogen compounds, and has accumulation toxicity.They or be dissolved in the bleaching waste liquor or be deposited in the fabric fibre surface, bring serious pollution to environment.Foreign technology developed country, particularly western countries are after having experienced the pollution disturbance of dioxin to food, formulated strict environmental legislation one after another, the restriction chlorine bleaches use, and the AOX in the bleaching waste liquor (Absorbable Organic Halogens) content as an important control criterion.From then on, replace chlorine bleaches with chlorine-free bleaching process gradually abroad, to reduce the AOX in the bleaching waste liquor.Now, developed countries such as Europe, the U.S., Japan have stopped containing the application of elemental chlorine bleaching agent in weaving substantially.
Oxygen-bearing bleaching agent generally is far smaller than chlorine bleaches to the effect of lignin, so, realize chlorine-free bleaching, must develop the method for lignin in the new free of contamination removal fabric fibre.Particularly contain the more fiber of lignin like this for linen fibre, can remove delignification be the key that effectively bleach.
The bio-bleaching technology is the nearly 30 years a kind of new technologies that grow up in paper industry, owing to equally also contain a large amount of lignin in the lumber fibre, the removal lignin is the key technology in the lumber fibre bleaching process too.The reported first such as Viikari of Finland in 1986 handle with the zytase of whiterot fungi (Phanerochaete chrysosporium) secretion and do not float paper pulp and can strengthen its bleachability, this is that related microorganism participates in the report of bleaching for the first time.Because potential application prospect, this report has excited the research extensive interest of people to this respect.Finland in 1989 have taken the lead in carrying out the industrial test of zytase bleached pulp, and some pulp mills of Northern Europe and north America region begin to adopt this technology subsequently.Further research work shows, a lot of subspecies of whiterot fungi all have the effect of decomposing lignin, for example Phanerochaete chrysosporium (Phanerochaete Chrysosporium) conchoidal grass ear bacterium (Panusconchatus), variegated manyzoned polypore bacteria (Coriolus versicolor), oyster cap fungus bacterium (Pleurotusostreatus) etc.In addition, discover that some black rot genus, bacterium, actinomyces also have secretion such as zytase, hemicellulase ability, these enzymes also have good booster action to the bleaching of paper pulp.
The mechanism of action of bio-bleaching mainly is that used Pseudomonas can produce fiber bleached useful enzyme system, mainly by zytase, hemicellulase, lignin-degrading enzymes (comprising manganese catalase, lignin peroxidase, laccase etc.).Zytase and hemicellulase change the string structure, from the effect that cellulose is peeled off lignin, and the then direct lignin degrading of lignin-degrading enzymes.Lignin in string is removed, and uses the bleaching of oxygen water again and just can obtain satisfied result.
The bio-bleaching of developed countries paper pulp has entered industrialized level, and China then still is in conceptual phase.The bio-bleaching technology of paper pulp has direct use microbial fermentation solution pulp treatment, also has various enzymes are separated to re-use, and obviously latter's use cost is greatly improved.
A significant deficiency of bio-bleaching is that microorganism is gone back the plain digestive enzyme of eccrine fiber in the required enzyme of secretion bleaching, so bio-bleaching process makes cellulosic molecular weight that bigger reduction be arranged.This shortcoming can also accepted the less relatively field of papermaking of cellulose requirement of strength, but just unacceptable concerning the textiles of cellulose requirement of strength strictness.So, up to the present, also do not have the bio-bleaching technology in the bleaching of linen fibre, to be applied.
Summary of the invention:
The present invention utilizes microorganism being aided with cellulase inhibitor, has solved cellulosic degradation problem in lignin removal process, obtains a kind of bleaching process of biodegradation lignin.
Above-mentioned purpose realizes by following technical scheme:
Biological auxiliary sodolin or fiber Totally-chlorine-free bleaching technology, with the former cloth of flax through alkaline scouring, pickling, after Biological Pretreatment, carry out hydrogen peroxide bleaching, described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 4-15g/L, pH value 7-11, bleaching temperature 40-80 ℃; bath raio 1: 5-20; bleaching time 0.5-2 hour; the product whiteness after the bleaching can reach more than 80%; tensile strength reaches 500-900 * 800-1200N, capillary effect meets existing sodolin bleaching technology index request greater than 8cm.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin being immersed in the Biological Pretreatment process time described in the nutrient solution of 10-50 times of weight is that 2-8 hour described Biological Pretreatment process added cellulase inhibitor, and its consumption is 2-20g/L.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin is immersed in the nutrient solution of 10-50 times of weight, best 1: 20-30, described Biological Pretreatment process time is 3-5 hour, described Biological Pretreatment process has added cellulase inhibitor, and its consumption is 8-12g/L.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described cellulase comprises shitosan, methylcellulose, carboxymethyl cellulose, hydroxyethylcellulose.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described alkaline scouring process is undertaken by following condition: contain alkali 8-25g/L in every liter of solution, described alkali is NaOH and/or sodium carbonate and/or sodium phosphate, boiling-off additive is non-ionic surface active agent+anionic surfactant mixture, the total amount 5-20g/L that mixture adds; bath raio is 1: 1-10,80-105 ℃ of kiering temperature, 0.5-4 hour kiering time.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described alkaline scouring process is undertaken by following condition: mixed base, the mixture ratio that comprises the mixture three of NaOH, sodium carbonate, sodium phosphate is NaOH 5g/L, sodium carbonate 8g/L, sodium phosphate 4g/L, addition is 15-20g/L; Boiling-off additive is non-ionic surface active agent+anion surfactant, 6-12g/L; Bath raio is 1: 8-10; 80-90 ℃ of kiering temperature; 1-1.5 hour kiering time.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, non-ionic surface active agent is alkylol polyoxyethylene ether, alkylphenol polyoxyethylene or polyoxyethylene carboxylate in the described boiling-off additive prescription, its example is 2: 1: 1; Silver ion surfactant in the boiling-off additive prescription is that its ratio of alkylbenzenesulfonate, alkylsulfonate, alkyl sulfate and soap is 1: 0.5, and the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, non-ionic surface active agent is the mixture of JFC, OP-10 and AEO-9 in the described boiling-off additive prescription, its example is 2: 1: 1; Silver ion surfactant LAS in the boiling-off additive prescription and the mixture of AES, its ratio is 1: 0.5, the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 6-8g/L; PH value 9-10; Bleaching temperature 60-70 ℃; Bath raio 1: 10-15; Bleaching time 1-1.5 hour.
Effect of the present invention:
For further reducing the cellulosic damage of lignin degradation process, the present invention selects shitosan, methylcellulose for use, and hydroxyethylcellulose equals the competitive inhibitor of the close material of cellulosic molecule as cellulase.Result of study shows, adds 1% shitosan in the biodegradation sodolin in the system of lignin, can make the vigor of cellulase reduce by 43%, has improved the intensity of the sodolin of handling through whiterot fungi effectively.
The technique effect that adopts different technical schemes to reach in the scope of the invention comprises whiteness, tensile strength, capillary effect, sees corresponding different embodiment.
The specific embodiment of the present invention:
Embodiment 1:
Biological auxiliary sodolin or fiber Totally-chlorine-free bleaching technology, with the former cloth of flax through alkaline scouring, pickling, after Biological Pretreatment, carry out hydrogen peroxide bleaching, described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 4-15g/L, pH value 7-11, bleaching temperature 40-80 ℃; bath raio 1: 5-20; bleaching time 0.5-2 hour; the product whiteness after the bleaching can reach more than 80%; tensile strength reaches 500-900 * 800-1200N, capillary effect meets existing sodolin bleaching technology index request greater than 8cm.
Embodiment 2:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin being immersed in the Biological Pretreatment process time described in the nutrient solution of 10-50 times of weight is that 2-8 hour described Biological Pretreatment process added cellulase inhibitor, and its consumption is 2-20g/L.
Embodiment 3:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin is immersed in the nutrient solution of 10-50 times of weight, best 1: 20-30, described Biological Pretreatment process time is 3-5 hour, described Biological Pretreatment process has added cellulase inhibitor, and its consumption is 8-12g/L.
Embodiment 4:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described cellulase comprises shitosan or methylcellulose or carboxymethyl cellulose or hydroxyethylcellulose.
Embodiment 5:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described alkaline scouring process is undertaken by following condition: contain alkali 8-25g/L in every liter of solution, described alkali is NaOH and/or sodium carbonate and/or sodium phosphate, boiling-off additive is non-ionic surface active agent+anionic surfactant mixture, the total amount 5-20g/L that mixture adds; bath raio is 1: 1-10,80-105 ℃ of kiering temperature, 0.5-4 hour kiering time.
Embodiment 6:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described alkaline scouring process is undertaken by following condition: mixed base, the mixture ratio that comprises the mixture three of NaOH, sodium carbonate, sodium phosphate is NaOH 5g/L, sodium carbonate 8g/L, sodium phosphate 4g/L, addition is 15-20g/L; Boiling-off additive is non-ionic surface active agent+anion surfactant, 6-12g/L; Bath raio is 1: 8-10; 80-90 ℃ of kiering temperature; 1-1.5 hour kiering time.
Embodiment 7:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, non-ionic surface active agent is alkylol polyoxyethylene ether, alkylphenol polyoxyethylene or polyoxyethylene carboxylate in the described boiling-off additive prescription, its example is 2: 1: 1; Silver ion surfactant in the boiling-off additive prescription is that its ratio of alkylbenzenesulfonate, alkylsulfonate, alkyl sulfate and soap is 1: 0.5, and the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
Embodiment 8:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, non-ionic surface active agent is the mixture of JFC, OP-10 and AEO-9 in the described boiling-off additive prescription, its example is 2: 1: 1; Silver ion surfactant LAS in the boiling-off additive prescription and the mixture of AES, its ratio is 1: 0.5, the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
Embodiment 9:
Auxiliary sodolin of described biology or fiber Totally-chlorine-free bleaching technology, described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 6-8g/L; PH value 9-10; Bleaching temperature 60-70 ℃; Bath raio 1: 10-15; Bleaching time 1-1.5 hour.
Embodiment 10:
The original strain that the above embodiment of the present invention uses be by institute of microbiology of the Chinese Academy of Sciences provide to the wooden 4 strain whiterot fungi bacterial classifications that have better degradation capability in the wood pulp, be respectively: Phanerochaete chrysosporium (5.776), conchoidal grass ear (5.154), variable color bolt bacterium (5.48) and layer of wood pore fungi (5.132)
The method of solid slant culture and Liquid Culture combination is adopted in the cultivation of original strain.The ability of each strains for degrading lignin is directly tested with the former cloth of flax, be about to the former cloth of flax that nutrient solution filtering thalline (or not filtering thalline) back adds known content of lignin, measure residual lignin content in the former cloth of flax after cultivating a period of time again, estimate the lignin degrading ability of bacterial strain with this.
The condition of culture of bacterial strain is as follows:
The solid slant culture: potato 200g, add 1 liter in water, slow fire boils 30min, extrudes juice after the cooling, adds glucose 20g, KH in juice 2PO 43g, MgSO 41.5g, agar 15g and trace V B 1, be settled to 1000ml after the heating for dissolving, use H 2SO 4Or NaOH solution adjusting PH=6, pour into (1/4 of test tube highly is advisable) in the test tube, autoclaving P=0.1MPa, 30min takes out the back bevel.Test strain is received on the solid slant medium, put into constant incubator and cultivate, 28 ℃ of cultivation temperature, incubation time 72 hours.
Liquid is once cultivated: potato 200g, and add water and boil 30min for 1 liter, shut out juice, in juice, add glucose 20g, KH 2PO 43g, MgSO 41.5g, VB 1Trace is settled to 1000ml after the dissolving, use H 2SO 4Or NaOH solution is regulated PH=6.Add the 250ml culture medium in the 500ml conical flask, cooling is standby behind sterilization 30min under the P=0.1MPa pressure.Get involved two ring bacterial classifications in the fluid nutrient medium after sterilization, cultivated 72 hours down for 28 ℃.
The liquid second incubation: culture medium is formed the same.Get nutrient solution 40ml one time, insert in the 200ml fluid nutrient medium, 28 ℃ are used for the former cloth lignin degradation test of flax behind the cultivation certain hour down.
The content of lignin of the former cloth of flax is 3.89%, and the bath raio of former cloth of flax and second incubation liquid is 1: 20, and the cultivation temperature after the former cloth of flax adds is 28 ℃, incubation time 4 hours, and the sulfuric acid gravimetric method is adopted in the content of lignin analysis.Concrete outcome sees Table 1.
Four kinds of whiterot fungis of table 1 are to the degradation rate of lignin in the former cloth of flax
Figure A20081006450200111
Result of the test shows, 4 kinds of white rot bacterial strains all have certain degradation to wooden in the former cloth of flax, wherein best with conchoidal grass ear bacterium effect, the bacterium liquid of second incubation after 120 hours can make the content of lignin in the former cloth of flax reduce by 71.4% in 4 hours, can satisfy the requirement of bleaching basically.But because the effect of cellulase, the intensity of the former cloth of flax also has bigger decline, and this bacterial strain is applied industrial, preferably reduces the activity of cellulase.
The present invention handles conchoidal grass ear bacterium, and concrete operations are as follows:
Get the thalline that a ring was cultivated 72 hours on slant medium, be seeded in the 100ml nutrient solution, shaken cultivation 24 hours is taken out the 10ml centrifugation, the collecting precipitation thing, and washing is smashed with the bead of sterilization, filters, and is diluted to 5ml as original bacteria liquid with sterilized water.With 1000 times of original bacteria liquid dilutions, calculate cell concentration with colony counting method, be diluted to 10 then 4/ ml is as the outstanding bacterium liquid of handling usefulness.
Minimal medium: potassium dihydrogen phosphate 0.5g, dipotassium hydrogen phosphate 2g, magnesium sulfate 0.5g, calcium chloride 0.2g, manganese sulfate 0.05g, sodium sulphate 0.5g, ferrous sulfate 0.05g, add water 1000ml, as adding 15-20g agar again with solid medium, sterilization 30min gets final product under P=0.1MPa pressure.
Get that 3 suspension are flat to be coated on the solid culture base plane, with 40W, 253.7nm ultra violet lamp 2,3,5min.Stopping to shine the back continues to cultivate 48 hours.Get a ring and be inoculated in the 40ml fluid nutrient medium shaken cultivation 20 hours.Get the 10ml medium centrifugal and separate, use the sterilized water washing precipitation, be diluted to 5ml, get 3 and be evenly coated on the minimal medium plane of containing 2% glucose, cultivated 48 hours.Eugonic bacterium colony is taken out, inoculate and shake bottle cultivation 48 hours in the fluid nutrient medium, get the 10ml centrifugation, the sterilized water washing precipitation is diluted to 5ml then, adds the 20ml minimal medium and cultivates 6 hours (consumption endogenous substance), centrifugation again.Precipitation was added in the minimal medium that contains 2% microfine cellulose shaken cultivation 6 hours, and added the benzyl penicillin of 200 units/ml, continue to cultivate 24 hours.Get 3 nutrient solutions and place on the solid medium flat board, cultivated 24 hours, with impression method the bacterium colony on the solid medium is imprinted on the solid medium flat board respectively and contains on the minimal medium flat board of microfine cellulose then.Cultivate and contrast the two after 48 hours, containing the bacterial strain of not growing on the minimal medium of microfine cellulose at well-grown on the solid medium is cellulolytic enzyme defective bacterial strain.It is chosen down one by one, be inoculated on the slant medium and cultivate, just obtained deficient strain.
Through decomposing the screening of lignin, determine that wherein 20 strains are as former bacterial strain.Former bacterial strain is inoculated 10 rejuvenation repeatedly, get 2ml suspension, add a certain amount of NTG and make its concentration reach 200mg/l, cultivated 3 hours, add the sterilized water centrifuge washing 3 times.Then it is forwarded on the solid medium and cultivated 48 hours.All the other operate the same processing.Obtain cellulase and support deficient strain 400 strains, further do to decompose the screening of lignin.Through screenability preferably 10 strain bacterium lignin degrading performances see Table 2.
Table 2 mutagenic strain is to lignin and cellulosic effect in the former cloth of flax *
Figure A20081006450200131
* the former cloth content of lignin 3.89% of flax, tensile strength 1220N (warp-wise).
Can see from test data, the conchoidal grass ear bacterium ability of lignin degrading is after treatment improved a lot, the vigor of cellulase reduces greatly, AB-210 bacterial strain particularly, the lignin degradation ability improves 17%, fibre strength after the processing improves more than 2 times, has reached the level of industrial applications substantially.
The present invention utilizes the bleaching of the auxiliary sodolin of white rot bacterial strain, and its technical process is as follows: the former cloth of flax is through alkaline scouring, pickling, biological treatment, hydrogen peroxide bleaching, and product whiteness that obtains and tensile strength all meet technological requirement.
The tensile strength of sodolin is pressed the method for GB/T3923.1-1997 " mensuration of textile fabric tensile property ultimate strength and elongation at break " regulation and is measured, and the whiteness of sodolin is pressed the method for GB/T8421-2001 " the objective ranking method of the relative whiteness of textiles " regulation and measured.
Embodiment 11:
The former cloth of flax is bleached by the technological process of alkaline scouring-pickling-microbial pretreatment-hydrogen peroxide bleaching.Wherein the alkaline scouring condition is as follows, NaOH 5g/L, and sodium carbonate 8g/L, 4g/L such as sodium phosphate, boiling-off additive 8g/L, bath raio is 1: 10,95 ℃ of kiering temperature, 1 hour kiering time.Alkaline scouring carries out pickling by following condition after finishing again, sulfuric acid 8g/L, and bath raio is 1: 10,40 ℃ of pickling temperatures, 1 hour pickling time.Pickling washes with water to neutrality after finishing.
The present invention carries out Biological Pretreatment with the strains A B-210 of conchoidal grass ear bacterium to the former cloth of flax.AB-210 places on the solid slant medium and preserves.To be kept at bacterial classification on the slant medium in use and get a ring and be inoculated on the 200ml fluid nutrient medium, 28 ℃ are cultivated 72 hours is a nutrient solution.Get a nutrient solution 20ml and be inoculated in the 400ml fluid nutrient medium, 28 ℃ are cultivated 72 hours is second incubation liquid, and second incubation liquid removes by filter mycelium, and filtrate is as the pretreatment fluid of the former cloth bleaching of flax.
Bath raio by 20: 1 in the above-mentioned again Biological Pretreatment liquid adds the former cloth of flax, places 4 hours for 28 ℃, takes out after washing and once enters hydrogen peroxide bleaching process.The hydrogen peroxide bleaching condition is as follows, and hydrogen peroxide 8g/L regulates bleaching liquid pH value to 9,80 ℃ of bleaching temperatures, bath raio 1: 20, bleaching time 1 hour with sodium hydroxide solution.Wash with water after bleaching finishes and remove bleach residue, the physical performance index of products obtained therefrom is as follows: whiteness 80.5%, tensile strength 560 * 865N, capillary effect 9.1cm.
Embodiment 12:
Various experimental conditions are with embodiment 11, and just the incubation time of second incubation liquid changes 48 hours into, and the physical performance index of products obtained therefrom is as follows: whiteness 78.5%, tensile strength 650 * 880N, capillary effect 8.1cm.
Embodiment 13
Various experimental conditions are with embodiment 11, and just the incubation time of second incubation liquid changes 96 hours into, and the physical performance index of products obtained therefrom is as follows: whiteness 80.1%, tensile strength 530 * 850N, capillary effect 9.5cm.
Embodiment 14
Various experimental conditions are with embodiment 11, and just the incubation time of second incubation liquid changes 120 hours into, and the physical performance index of products obtained therefrom is as follows: whiteness 81%, tensile strength 540 * 810N, capillary effect 9.0cm.
Embodiment 15
Various experimental conditions are with embodiment 11, and just the shitosan that adds 5g/L in Biological Pretreatment liquid is as cellulase inhibitor, and the physical performance index of products obtained therefrom is as follows: whiteness 81%, tensile strength 680 * 970N, capillary effect 9.5cm.
Embodiment 16
Various experimental conditions are with embodiment 11, and just the shitosan that adds 10g/L in Biological Pretreatment liquid is as cellulase inhibitor, and the physical performance index of products obtained therefrom is as follows: whiteness 80.5%, tensile strength 675 * 980N, capillary effect 9.4cm.
Embodiment 17
Various experimental conditions are with embodiment 15, and just the Biological Pretreatment time shortened to 2 hours by 4 hours, and the physical performance index of products obtained therefrom is as follows: whiteness 70%, tensile strength 720 * 990N, capillary effect 7.5cm.
Embodiment 18
Various experimental conditions are with embodiment 15, and just the concentration of hydrogen peroxide is 10g/L when hydrogen peroxide bleaching, and the physical performance index of products obtained therefrom is as follows: whiteness 81.5%, tensile strength 630 * 925N, capillary effect 9.4cm.
Embodiment 19
Various experimental conditions are with embodiment 15, and just the concentration of hydrogen peroxide is 6g/L when hydrogen peroxide bleaching, and the physical performance index of products obtained therefrom is as follows: whiteness 78%, tensile strength 645 * 965N, capillary effect 9.3cm.

Claims (9)

1. a biology is assisted sodolin or fiber Totally-chlorine-free bleaching technology, with the former cloth of flax through alkaline scouring, pickling, it is characterized in that: after Biological Pretreatment, carry out hydrogen peroxide bleaching, described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 4-15g/L, pH value 7-11, bleaching temperature 40-80 ℃; bath raio 1: 5-20; bleaching time 0.5-2 hour; the product whiteness after the bleaching can reach more than 80%; tensile strength reaches 500-900 * 800-1200N, capillary effect meets existing sodolin bleaching technology index request greater than 8cm.
2. auxiliary sodolin of biology according to claim 1 or fiber Totally-chlorine-free bleaching technology, it is characterized in that: the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin being immersed in the Biological Pretreatment process time described in the nutrient solution of 10-50 times of weight is that 2-8 hour described Biological Pretreatment process added cellulase inhibitor, and its consumption is 2-20g/L.
3. auxiliary sodolin of biology according to claim 1 or fiber Totally-chlorine-free bleaching technology, it is characterized in that: the used bacterial strain of described Biological Pretreatment process is: conchoidal grass ear bacterium (Panus conchatus) is through ultraviolet irradiation and NTG cellulose deficiency dissociant AB-210, described Biological Pretreatment process is used the second incubation liquid of bacterial classification, sodolin is immersed in the nutrient solution of 10-50 times of weight, best 1: 20-30, described Biological Pretreatment process time is 3-5 hour, described Biological Pretreatment process has added cellulase inhibitor, and its consumption is 8-12g/L.
4. according to claim 1 or auxiliary sodolin of 2 or 3 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: described cellulase comprises shitosan, methylcellulose, carboxymethyl cellulose, hydroxyethylcellulose.
5. according to claim 1 or auxiliary sodolin of 2 or 3 or 4 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: described alkaline scouring process is undertaken by following condition: contain alkali 8-25g/L in every liter of solution, described alkali is NaOH and/or sodium carbonate and/or sodium phosphate, boiling-off additive is non-ionic surface active agent+anionic surfactant mixture, the total amount 5-20g/L that mixture adds; bath raio is 1: 1-10,80-105 ℃ of kiering temperature, 0.5-4 hour kiering time.
6. according to claim 1 or auxiliary sodolin of 2 or 3 or 4 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: described alkaline scouring process is undertaken by following condition: mixed base, the mixture ratio that comprises the mixture three of NaOH, sodium carbonate, sodium phosphate is NaOH 5g/L, sodium carbonate 8g/L, sodium phosphate 4g/L, addition is 15-20g/L; Boiling-off additive is non-ionic surface active agent+anion surfactant, 6-12g/L; Bath raio is 1: 8-10; 80-90 ℃ of kiering temperature; 1-1.5 hour kiering time.
7. according to claim 1 or auxiliary sodolin of 2 or 3 or 4 or 5 or 6 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: non-ionic surface active agent is alkylol polyoxyethylene ether, alkylphenol polyoxyethylene or polyoxyethylene carboxylate in the described boiling-off additive prescription, and its example is 2: 1: 1; Silver ion surfactant in the boiling-off additive prescription is that its ratio of alkylbenzenesulfonate, alkylsulfonate, alkyl sulfate and soap is 1: 0.5, and the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
8. according to claim 1 or auxiliary sodolin of 2 or 3 or 4 or 5 or 6 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: non-ionic surface active agent is the mixture of JFC, OP-10 and AEO-9 in the described boiling-off additive prescription, and its example is 2: 1: 1; Silver ion surfactant LAS in the boiling-off additive prescription and the mixture of AES, its ratio is 1: 0.5, the ratio of non-ionic surface active agent and anion surfactant is 1: 2-5.
9. according to claim 1 or auxiliary sodolin of 2 or 3 or 4 or 5 or 6 described biologies or fiber Totally-chlorine-free bleaching technology, it is characterized in that: described hydrogen peroxide floats process again to be undertaken by following condition: hydrogen peroxide 6-8g/L; PH value 9-10; Bleaching temperature 60-70 ℃; Bath raio 1: 10-15; Bleaching time 1-1.5 hour.
CNA2008100645025A 2008-05-14 2008-05-14 Biologically-aided totally-chlorine-free bleaching technology of flax cloth or fiber Pending CN101581034A (en)

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CN103290688A (en) * 2013-05-16 2013-09-11 任芳芳 Cotton fabric refining agent
CN104611936A (en) * 2015-02-10 2015-05-13 苏州陈恒织造有限公司 Pretreatment process of linen fabric
CN104805678A (en) * 2015-05-12 2015-07-29 湖州厉华妤婕联合纺织有限公司 Novel bleaching agent for textile pretreatment
CN105442296A (en) * 2015-11-17 2016-03-30 梅庆波 Method for biologically bleaching linen fibers
CN105624800A (en) * 2014-11-04 2016-06-01 华中科技大学 Biological bleaching method for production of refined dried ramie
CN107201642A (en) * 2017-04-10 2017-09-26 浙江金莱诺纤维有限公司 Flax high-quality yarn bleaching process
CN107780085A (en) * 2017-11-30 2018-03-09 英泰时尚服饰(苏州)有限公司 A kind of sodolin and its pre-treating method
CN105733018B (en) * 2016-05-11 2018-07-31 恒天海龙(潍坊)新材料有限责任公司 A kind of cleaning for the production of cellulose expanded material
CN109535444A (en) * 2018-11-30 2019-03-29 泸州北方纤维素有限公司 The bleaching process of hydroxyethyl cellulose
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CN114836974A (en) * 2022-05-06 2022-08-02 中国农业科学院麻类研究所 Ramie fiber bleaching method
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CN103290688B (en) * 2013-05-16 2015-04-29 浙江伊秀服饰有限公司 Cotton fabric refining agent
CN103290688A (en) * 2013-05-16 2013-09-11 任芳芳 Cotton fabric refining agent
CN105624800B (en) * 2014-11-04 2018-01-23 华中科技大学 A kind of bio-bleaching method for degummed ramie fiber production
CN105624800A (en) * 2014-11-04 2016-06-01 华中科技大学 Biological bleaching method for production of refined dried ramie
CN104611936A (en) * 2015-02-10 2015-05-13 苏州陈恒织造有限公司 Pretreatment process of linen fabric
CN104805678A (en) * 2015-05-12 2015-07-29 湖州厉华妤婕联合纺织有限公司 Novel bleaching agent for textile pretreatment
CN105442296A (en) * 2015-11-17 2016-03-30 梅庆波 Method for biologically bleaching linen fibers
CN105733018B (en) * 2016-05-11 2018-07-31 恒天海龙(潍坊)新材料有限责任公司 A kind of cleaning for the production of cellulose expanded material
CN107201642A (en) * 2017-04-10 2017-09-26 浙江金莱诺纤维有限公司 Flax high-quality yarn bleaching process
CN107780085A (en) * 2017-11-30 2018-03-09 英泰时尚服饰(苏州)有限公司 A kind of sodolin and its pre-treating method
CN109535444A (en) * 2018-11-30 2019-03-29 泸州北方纤维素有限公司 The bleaching process of hydroxyethyl cellulose
WO2022015179A1 (en) 2020-07-13 2022-01-20 Firma Handlowo-Usługowa Instbud Stanisław Boguta Spółka Jawna The multi-layer composite sleeve, in particular for trenchless pipeline rehabilitation
CN114836974A (en) * 2022-05-06 2022-08-02 中国农业科学院麻类研究所 Ramie fiber bleaching method
CN115110305A (en) * 2022-08-12 2022-09-27 淄博大染坊丝绸集团有限公司 Flax fiber cone yarn bleaching process

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