CN109208102A - A kind of class spider silk polymer fiber and preparation method thereof based on column chromatography silica gel - Google Patents

A kind of class spider silk polymer fiber and preparation method thereof based on column chromatography silica gel Download PDF

Info

Publication number
CN109208102A
CN109208102A CN201710528437.6A CN201710528437A CN109208102A CN 109208102 A CN109208102 A CN 109208102A CN 201710528437 A CN201710528437 A CN 201710528437A CN 109208102 A CN109208102 A CN 109208102A
Authority
CN
China
Prior art keywords
silica gel
column chromatography
chromatography silica
microns
spider silk
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.)
Granted
Application number
CN201710528437.6A
Other languages
Chinese (zh)
Other versions
CN109208102B (en
Inventor
乔金樑
姜超
戚桂村
张晓红
宋志海
赖金梅
蔡传伦
李秉海
王湘
蒋海斌
张江茹
茹越
高建明
张红彬
韩朋
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.)
Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
Original Assignee
Sinopec Beijing Research Institute of Chemical Industry
China Petroleum and Chemical Corp
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
Priority to CN201710528437.6A priority Critical patent/CN109208102B/en
Application filed by Sinopec Beijing Research Institute of Chemical Industry, China Petroleum and Chemical Corp filed Critical Sinopec Beijing Research Institute of Chemical Industry
Priority to EP18828449.1A priority patent/EP3650587A4/en
Priority to KR1020207002521A priority patent/KR102538295B1/en
Priority to CN201880043553.1A priority patent/CN110914488B/en
Priority to US16/627,929 priority patent/US11572638B2/en
Priority to CA3068755A priority patent/CA3068755A1/en
Priority to JP2020500159A priority patent/JP7353262B2/en
Priority to AU2018296341A priority patent/AU2018296341B2/en
Priority to PCT/CN2018/092645 priority patent/WO2019007217A1/en
Priority to TW107122475A priority patent/TWI786144B/en
Publication of CN109208102A publication Critical patent/CN109208102A/en
Application granted granted Critical
Publication of CN109208102B publication Critical patent/CN109208102B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/06Wet spinning methods
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/50Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polyalcohols, polyacetals or polyketals
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/54Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polymers of unsaturated nitriles
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/70Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Artificial Filaments (AREA)

Abstract

The present invention relates to a kind of class spider silk polymer fibers and preparation method thereof based on column chromatography silica gel of chemobionics technical field.The polymer fiber of the class spider silk includes following components based on parts by weight: 100 parts of fibrous matrix polymer;1~44 part of column chromatography silica gel.Its monofilament of the polymer fiber has the microstructure of the class spider silk of spindle section structure unit interval distribution, the spindle section structure unit radial height is 10~300 microns, the axial length of the spindle section structure unit is 10~1000 microns, and the spacing of the spindle section structure unit is 10~5000 microns.Method of the invention is not necessarily to substantially change existing spinning technique and equipment is without change, simple process and low cost.Water droplet may be implemented in the displacement of the fiber surface in the polymer fiber for the class spider silk that the present invention obtains, and has water collecting function, and better mechanical property.

Description

A kind of class spider silk polymer fiber and preparation method thereof based on column chromatography silica gel
Technical field
The present invention relates to chemobionics technical fields, furtherly, are related to a kind of class spider based on column chromatography silica gel Silk polymer fiber and preparation method thereof.
Background technique
Water resource is the important natural resources of human social development.Tellurian water can direct quilt although enormous amount People's production and life utilize pitiably little, about only account for the 0.26% of earth total Water.The sustainable use of water resource is A most important problem in all natural resources Sustainable Development and Utilizations.Today's society, freshwater resources situation in short supply is Gradually show.About 1,500,000,000 populations of more than 80 countries in the whole world face fresh water deficiency, wherein 26 300,000,000 national populations are lived completely In exsiccosis.It expects 2025, the whole world will have 3,000,000,000 population water shortages, and the countries and regions being related to are up to more than 40.Fresh water Shortage of resources oneself through restrict society development, solve the problems, such as that freshwater resources are extremely urgent.Solution may be present in air In -- here collection be knotted 12.9 trillion tons of vaporous waters -- air is likely to become important " water source " of following mankind's domestic water.
Spider is one of the pioneer that air water source is utilized in nature.When cobweb is placed in moist environment, steam exists Capture silk table face therein condenses, forms small water droplet;And periodic spindle nodule present in the fiber is configured to capture silk Radius of curvature generating period variation, generate Laplce's pressure difference, cause water droplet along fiber radial direction unbalance stress, push away It is mobile that orientation (being directed toward spindle section) occurs for dynamic water droplet.This displacement of water droplet is conducive to droplet quick collecting and forms flood Pearl weakens transpiration, conducive to the quick collection of moisture in air.Spider collects moisture guarantee in air by the above process The mode of existence solves fresh water crisis for us and provides new thinking: developing the imitative spider silk fiber with spindle section structure, The quick collection for realizing moisture in air, has broad application prospects in areas such as desert, islands, is also expected to be used for airport etc. Code in Hazardous Special Locations steam disperses.
There are mainly three types of the methods for preparing the imitative spider silk fiber of similar structures in the prior art.
First is that infusion process: the Chinese patent of Publication No. CN102776785A (application No. is 201110223679.7) discloses The polymer filament of catchmenting of imitative spider silk structure a kind of use this kind of method, after existing fiber is immersed Polymer Solution, take Out in drying process, Polymer Solution hangs on fiber surface since Rayleigh unstability forms a string of drops in fiber surface, The spindle section of axial alignment is obtained through dry solidification, obtains the fiber of similar spider silk structure.Publication No. CN102587139A The Chinese patent of (application No. is 201210004686.2), for patent basis, is furthermore achieved with above-mentioned and prepares resulting fiber Uniform, controllable, surface have more microcosmic protrusion or micropore, improve the collection of fiber the height of the protrusion section on surface from small to large Water efficiency.This method belongs to the post-processing to existing fiber.
Second is that using electrospinning process, the high requirements on the equipment: Publication No. CN103334244A (application No. is 201710227113.0) Chinese patent discloses a kind of self-assembly preparation method thereof of electrospinning bead string fiber, and the invention is using quiet Electrospinning forms micron order bead string structure in the surface self-organization of staple fibre, obtains imitative spider silk fiber.But Static Spinning Costly, and the type of polymer for being able to use electrostatic spinning is less for the equipment of silk.
Third is that utilizing wet spinning process: application No. is one kind that 201710166815.0 Chinese patent provides to have collection The polymer fiber and preparation method thereof of the bionical spider silk of water characteristic, which uses solution-polymerized SBR technology, in spinning solution Middle introducing micron order spray-dried powders rubber, fibre solidification form periodic spindle section in the process, and one-step method is imitated Spider silk fiber.But since the interaction of additive and fibrous matrix is weaker, the mechanicalness of fiber is affected to a certain extent Energy.
Summary of the invention
In order to solve the above-mentioned problems in the prior art, the present invention is proposed between a kind of having based on column chromatography silica gel Every the polymer fiber of the class spider silk of the spindle section structure of distribution.Relate in particular to a kind of class spider based on column chromatography silica gel Spider's thread polymer fiber and preparation method thereof.The present processes by being added column chromatography silica gel during the spinning process, in fiber It can be obtained spindle section structure in preparation process, it, can be in column in spinning process there is porous structure inside column chromatography silica gel Microfiber network is formed in chromatographic silica gel inner void, solves interaction force between additive and fibrous matrix to a certain extent Weaker problem reduces influence of the additive to fiber mechanical performance, and this method is without substantially changing existing spinning technique Dynamic and equipment is without change, and from technique, more simply, cost is also lower.
The present invention of the application first purpose proposes a kind of class spider silk polymer fiber based on column chromatography silica gel.It is described Its monofilament of polymer fiber has the microstructure of the class spider silk of spindle section structure unit interval distribution, and water droplet may be implemented and exist The displacement of the fiber surface has water collecting function.Described herein is spaced apart, and refers to adjacent two be distributed on monofilament It is connected between a spindle section structure unit for monofilament.
A kind of class spider silk polymer fiber based on column chromatography silica gel, comprising in parts by weight with the following group Point:
A. 100 parts by weight of fibrous matrix polymer;
B. 1~44 parts by weight of column chromatography silica gel, preferably 3~40 parts, more preferably 5~30 parts by weight, yet more preferably 5 ~25 parts by weight.
The component a fibrous matrix polymer is as fibrous matrix, and the component b column chromatography silica gel is as additive, shape At spindle section structure.
The spindle section structure unit radial height is 10~300 microns, preferably 20~200 microns, more preferably 30 ~150 microns;The axial length of the spindle section structure unit be 10~1000 microns, preferably 20~700 microns, more preferably It is 100~300 microns;The spacing of the spindle section structure unit is 10~5000 microns, preferably 50~3000 microns, more excellent It is selected as 100~1000 microns.
The average particle size of the column chromatography silica gel be 60~400 mesh, preferably 60~300 mesh, more preferably 80~ 300 mesh.
The porosity of the column chromatography silica gel is 10~80%, preferably 20~60%, more preferably 20~50%.
The aperture of the column chromatography silica gel is 0.1~200 nanometer, and preferably 0.5~150 nanometer, more preferably 1~50 receives Rice.
The column chromatography silica gel can also be by existing selected from the commercially available various column chromatography silica gels for meeting the above parameter The method of technology is made by oneself and is obtained.
The fibrous body diameter is 5~250 microns, preferably 10~150 microns, more preferably 20~50 microns.
The fibrous matrix polymer is selected from the existing various polymer that can form fiber in the prior art, such as poly- Acrylonitrile, polyurethanes, polyvinyl alcohol, viscose fiber, nylon, cellulose sulfonate, cellulose acetate, polychlorostyrene second At least one of alkene, poly- isophtalamide, poly, poly(p-phenylene terephthalamide);It is preferred that For polyacrylonitrile, polyurethanes, polyvinyl alcohol, viscose fiber, poly, poly- paraphenylene terephthalamide couple At least one of phenylenediamine, polyvinyl chloride, more preferably polyacrylonitrile, polyurethanes, at least one in polyvinyl alcohol Kind, yet more preferably polyvinyl alcohol.
When the fibrous matrix polymeric oxidizer polyvinyl alcohol is as fibrous body, the degree of polymerization of the polyvinyl alcohol is 400~4000, preferably 500~3000, more preferably 1000~2500;Alcoholysis degree be 55%~99%, preferably 88%~ 99%.
The application second purpose is to provide a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel. This method is by traditional wet spinning technology, by polymer and the common spinning of column chromatography silica gel, since column chromatography silica gel exists Porous structure, therefore during being scattered in polymer solution, number of polymers solution diffuses into inside column chromatography silica gel; During spinning solution miniflow forms fiber, posterior drawing by coagulating bath, since solvent is constantly precipitated and radial drawing, fibre Dimension body volume generation is significantly shunk, and column chromatography silica gel volume is unaffected, therefore at silica gel presence, and fiber can occur Microcosmic protrusion forms fusellal fabric;Into the polymer solution inside column chromatography silica gel through supersolidification, microfiber network is formed, it will Silica gel is bundled in fibrous inside, efficiently solves the problems, such as that interaction force is weaker between column chromatography silica gel and fibrous matrix, drop Low influence of the additive to fiber mechanical performance.This method simple process is easy to without largely being improved prior art Industrialized production.
A kind of preparation method of the class spider silk polymer fiber based on column chromatography silica gel, comprising the following steps:
(1) it disperses the fibrous matrix polymer and column chromatography silica gel additive in solvent by the dosage, heating, Stirring is dissolved in solvent to fibrous matrix polymer, and column chromatography silica gel is evenly dispersed in the solution, obtains uniform spinning solution; Wherein, the heating temperature is 30~95 degrees Celsius, preferably 50~95 degrees Celsius, more preferably 70~95 degrees Celsius;
(2) corresponding used polymer and solvent, prepare corresponding coagulating bath;
(3) spinning solution is squeezed into coagulating bath by wet-spinning frame or peristaltic pump etc., through supersolidification, drying, is collected Obtain as-spun fibre;
(4) by stretching as-spun fibre, the bionic fiber with the spindle section structure being spaced apart is obtained.
It is preferred that after the above step, comprising: (5) above-mentioned gained bionic fiber is placed in certain time in crosslinked fluid;Water It washes, dry, collect, obtain fiber.Cross-linking process can change the water resistance of the fiber, but not influence the base of fiber This physical structure, the spindle section structure being spaced apart, therefore, cross-linking process are selection process, and the reality for not influencing fiber is answered With.
Specifically,
It is in terms of 100 parts by weight of solvent, the dosage of the fibrous matrix polymer is 5~50 weight in the step (1) Part, preferably 10~40 parts, more preferably 10~25 parts;The dosage of the column chromatography silica gel is with the fibrous matrix polymer Dosage is 100 parts by weight meters, and the dosage of the column chromatography silica gel is 1~44 parts by weight, preferably 3~40 parts, more preferably 5~ 30 parts by weight, yet more preferably 5~25 parts by weight.
In the step (1), the solvent is polymer used common wet spinning solvent accordingly, specifically may be used Selected from least one of Isosorbide-5-Nitrae-dioxane, n,N-Dimethylformamide, tetrahydrofuran, water, sulfuric acid, more preferably N, N- bis- At least one of methylformamide, Isosorbide-5-Nitrae-dioxane.
In the step (2), coagulating bath is that common wet spinning coagulating bath is equal accordingly for fibrous matrix polymer used It can.Mixed process can use existing any liquid liquid mixing apparatus, such as mechanical stirring, ultrasonic disperse.The coagulating bath Specifically can be selected from aqueous sodium persulfate solution, methanol, ethyl acetate, water, Isosorbide-5-Nitrae-dioxane, in n,N-Dimethylformamide at least A kind of or mixed solvent, preferably sulfuric acid sodium water solution, methanol, water, Isosorbide-5-Nitrae-dioxane, in n,N-Dimethylformamide at least A kind of or mixed solvent;The concentration of the aqueous sodium persulfate solution is 300~500g/L, preferably 350~450g/L.
If the aqueous solution of polyvinyl alcohol is selected to be used as spinning solution, optional aqueous sodium persulfate solution, methanol, in ethyl acetate At least one as coagulating bath, wherein the concentration of the aqueous sodium persulfate solution is 300~500g/L, preferably 350~450g/ L;At least one of preferably sulfuric acid sodium water solution, methanol;More preferably aqueous sodium persulfate solution.If selecting the 1 of polyvinyl alcohol, At least one of methanol, ethyl acetate or selection methanol and Isosorbide-5-Nitrae-can be selected as spinning solution in 4- dioxane solution The binary solution of dioxane composition is as coagulating bath, wherein the content of the Isosorbide-5-Nitrae-dioxane is with methanol weight for 100 weights Part meter is measured, Isosorbide-5-Nitrae-dioxane parts by weight are 0.1~50 part, preferably 5~40 parts, more preferably 10~30 parts;It is preferred that For methanol or methanol and Isosorbide-5-Nitrae-dioxane composition binary solution;More preferably methanol.
When carrying out spinning using the spinning solution, spinneret orifice is usually used spinneret orifice in spinning process, described Spinneret orifice internal diameter can be 10~1000 microns, preferably 50~500 microns, more preferably 50~300 microns;Receiving silk rate can be 0.01~100 meter per minute, and preferably 0.05~10 meter per minute, and more preferable 0.1~1 meter per minute.
In the step (4), draft temperature is fibrous matrix polymer used common draft temperature accordingly.If Using polyvinyl alcohol as fibrous matrix polymer, draft temperature is 100~220 degrees Celsius, preferably 120~200 degrees Celsius, more Preferably 150~180 degrees Celsius.
In the step (5), the crosslinked fluid is fibrous matrix polymer used common wet spinning crosslinking accordingly Liquid.
According to polyvinyl alcohol as fibrous matrix polymer, crosslinked fluid can by acids and aldehydes and/or sodium sulphate, with The solution of water is constituted, that is to say, that crosslinked fluid is the aqueous solution of acids and aldehydes, may be optionally added sodium sulphate.Acids can be common Inorganic acid, preferably at least one of hydrochloric acid, sulfuric acid, more preferably sulfuric acid;Aldehydes be preferably formaldehyde, in glutaraldehyde extremely Few one kind.Specifically, the aqueous solution of crosslinked fluid preferably sulfuric acid, glutaraldehyde (or formaldehyde) and sodium sulphate, wherein the concentration of sulfuric acid can It is 100~500 gram per liters, preferably 200~350 gram per liters;The concentration of glutaraldehyde can be 1~80 gram per liter, preferably 30~ 60 gram per liters;The concentration of formaldehyde can be 1~50 gram per liter, preferably 20~35 gram per liters;The concentration of sodium sulphate can be 0~350 Gram per liter, preferably 50~200 gram per liters.
A kind of class spider silk polymer fiber and preparation method thereof based on column chromatography silica gel proposed by the present invention, obtains Staple fibre in high humility, steam is coagulated in fiber surface, subsequent droplet merges to spindle section structure part, Acceleration collects to form big water droplet, is conducive to collect.
Advantages of the present invention:
(1) present invention is using column chromatography silica gel as additive, due to there is a large amount of porous knot inside column chromatography silica gel Structure, therefore the microfiber network that polymer solution existing for cellular internal will form during fibre solidification, by column chromatography silica gel It is bundled in fibrous inside, solves the problems, such as that interfacial interaction is weaker between additive and basis material, reduces additive Influence to fiber mechanical performance;
(2) present invention process is simple, can be realized using traditional spinning equipment, increases optional equipment without additional, fits Preferably continuously prepared on a large scale;
(3) fiber for the class spider silk with the spindle section structure being spaced apart that the present invention obtains is low in cost, tool There is good stability;
(4) fiber of the class spider silk with the spindle section structure being spaced apart that the present invention obtains can be used for island, The thick fog that the area such as desert and foggy mountain area is collected around water droplet and the Code in Hazardous Special Locations such as airport in air that borders on the sea disperses.
Detailed description of the invention
Fig. 1 is the microscope photo of the class spider silk polymer fiber based on column chromatography silica gel made from embodiment 1;
Fig. 2 is that the class spider silk polymer fiber based on column chromatography silica gel made from embodiment 1 is aobvious at nonwoven club Micro mirror photo;
Fig. 3 is the microscope photo of the class spider silk polymer fiber based on column chromatography silica gel made from embodiment 3.
Fig. 1 and Fig. 2 is the sample that embodiment 1 obtains, and difference is that Fig. 1 is the micrograph at spindle section, and Fig. 2 is to spin The pattern of the pure fiber of club interval.Show on fiber that without column chromatography silica gel, fiber surface is smooth, smooth there are part in Fig. 2.
Fig. 1 and Fig. 3 as it can be seen that due to column chromatography silica gel presence, form spindle section structure, color deeper part in spindle section Dividing is additive, and translucency is weaker, is aspherical various irregular shapes.
Fig. 1 and Fig. 3 is respectively illustrated in the case where different column chromatography silica gel additive amounts, the microcosmic knot of the fiber of acquisition Structure, size, distribution including bulge-structure.As column chromatography silica gel additive amount improves, bulge-structure becomes large-sized and more encrypts Collection.Therefore, the fiber of different structure can be obtained by size, the additional amount of regulation column chromatography silica gel.And without column chromatography silica gel There are part, fiber surface is smooth, smooth.
Specific embodiment
Below with reference to embodiment, the present invention is further illustrated.But the present invention is not restricted by the embodiments.In embodiment The following instrument and equipment of experimental data and measuring method measurement:
(1) experiment basis equipment: extrusion equipment is the SPLab01 type peristaltic pump of Baoding Shen Chenbeng industry Co., Ltd production, Stretcher is 3366 universal testing machine of INSTRON.
(2) instrument of experimental data measurement: microscope photo is shown by NIKON ECLIPSE lC100N POL type in experiment Micro mirror obtain, water droplet fiber surface displacement process by German dataphysics company SCA20 type Contact-angle measurement Instrument observation.
The tensile property test of fiber uses monofilament method, according to ASTM D3379-1975 " Standard Test Method for Tensile Strength and Young’s Modulus for High-Modulus Single-Filament Materials " it executes.
Embodiment 1
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 1.05 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), heating stirring 2 hours, obtain uniform spinning at 80 degrees celsius Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber, tested, test result is shown in Fig. 1 and Fig. 2.The main diameter of gained fiber is 26 micro- Rice, spindle section radial height are 55~120 microns, and axial length is 100~500 microns, and spindle internode spacing is 80~2000 Micron.
It is observed through contact angle measurement, the fiber is in high humility, fiber surface formation droplet random first, Subsequent drop is to displacement at central protuberance, forming big drop around fusellal fabric.
Comparative example 1
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 0.7 gram of carboxyl fourth Benzene spray-dried powders rubber is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), heating stirring 2 hours at 80 DEG C, is obtained Uniform spinning solution.At room temperature, above-mentioned spinning solution is squeezed into coagulating bath by peristaltic pump (methanol and DMSO's is mixed Close solution, based on 100 parts by weight of methanol, DMSO20 parts by weight) in carry out spinning: 0.01 milliliter of practical rate of extrusion per minute, Spinning head model 25G (round, diameter be 260 microns), receive silk rate be 0.42 meter per minute, fiber in coagulating bath at least 5 minutes.Obtained fiber after sufficiently drying, is collected in air, obtains the polymer fiber of class spider silk, carries out machine Tool performance test, tensile break strength are 94 ± 12MPa.
The preparation method of above-mentioned Carboxy spray-dried powders rubber: by the carboxylic styrene butadiene latex of 1kg solid content 50%, the Yanshan Mountain Petrochemical iy produced, trade mark XSBRL-54B1 are placed in a container, and Isooctyl acrylate monomer 15g is added dropwise under stiring, is added dropwise to complete subsequent Continuous stirring one hour, is irradiated with cobalt source, dosage 2.5Mrad, dosage rate 50Gy/min, the latex after radiation passes through spray later The spray drying of mist drier, the inlet temperature of spray dryer are 140 DEG C~160 DEG C, and outlet temperature is 60 DEG C~70 DEG C, are collected Carboxylic styrene-butadiene rubber powder after drying obtains the carboxylic styrene-butadiene rubber powder sample that average grain diameter is 30 microns by screening For this comparative example.
Comparative example 2
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 2.1 grams of carboxyl fourths Benzene spray-dried powders rubber (with comparative example 1) is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), the heating stirring at 80 DEG C 2 hours, obtain uniform spinning solution.At room temperature, above-mentioned spinning solution is squeezed into coagulating bath (methanol by peristaltic pump With the mixed solution of DMSO, based on 100 parts by weight of methanol, 20 parts by weight of DMSO) in carry out spinning: practical rate of extrusion 0.01 Milliliter is per minute, and spinning head model 25G (round, diameter is 260 microns), receiving silk rate is 0.42 meter per minute, and fiber exists At least 5 minutes in coagulating bath.Obtained fiber after sufficiently drying, is collected in air, obtains the polymerization of class spider silk Fibres, carry out measuring mechanical property, and tensile break strength is 36 ± 6MPa.
Comparative example 3
7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 1.4 grams of glass are micro- Ball (is purchased from Suzhou Hua Nixi Chemical Co., Ltd., non-porous solid glass microballoon, 15~30 microns), is scattered in 43 grams of Isosorbide-5-Nitrae-dioxies In six rings (DMSO), heating stirring 2 hours at 80 DEG C obtain uniform spinning solution.At room temperature, by above-mentioned spinning Stoste by peristaltic pump squeeze into coagulating bath (mixed solution of methanol and DMSO, based on 100 parts by weight of methanol, 20 weight of DMSO Part) in carry out spinning: 0.01 milliliter of practical rate of extrusion per minute, spinning head model 25G (round, diameter is 260 microns), Receiving silk rate is 0.42 meter per minute, and fiber is at least 5 minutes in coagulating bath.Obtained fiber is in air by sufficiently dry It after dry, collect, obtains the polymer fiber of class spider silk, carry out measuring mechanical property, tensile break strength is 54 ± 10MPa。
Embodiment 2
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 1.4 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), heating stirring 2 hours, obtain uniform spinning at 80 degrees celsius Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 25 microns, and spindle section radial height is 60~130 micro- Rice, axial length are 90~500 microns, and spindle internode spacing is 70~1500 microns.Measuring mechanical property is carried out, is stretched disconnected Resistance to spalling is 300 ± 34MPa.
Embodiment 3
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 2.1 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%), be scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 70 degrees Celsius lower heating stirring 2 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber, tested, test result is shown in Fig. 3.The main diameter of gained fiber is 26 microns, spindle Saving radial height is 60~120 microns, and axial length is 100~520 microns, and spindle internode spacing is 70~1000 microns.Into Row measuring mechanical property, tensile break strength are 185 ± 20MPa.
It is observed through contact angle measurement, the fiber is in high humility, fiber surface formation droplet random first, Subsequent drop is to displacement at central protuberance, forming big drop around fusellal fabric.
Embodiment 4
By 8 grams of polyvinyl alcohol (PVA 2499, Aladdin, the degree of polymerization 2400, alcoholysis degree 99%), 0.8 gram of column chromatography Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 40~70 angstroms of aperture, porosity be 40~ 60%), be scattered in 42 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 95 degrees Celsius lower heating stirring 2 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed into coagulating bath by peristaltic pump (mixed solution of methanol and DMSO, is pressed 100 parts by weight meter of methanol, 20 parts by weight of DMSO) in carry out spinning: 0.02 milliliter of practical rate of extrusion per minute, spinneret head dummy Number be 22G (diameter is 410 microns), receive silk rate be 0.4 meter per minute, fiber is at least 5 minutes in coagulating bath;By abundant Dry, collection, obtains as-spun fibre;It carries out being placed in crosslinked fluid after hot-drawn extends to 10 times of original length under 180 degrees Celsius In (11.48 gram of 98% concentrated sulfuric acid, 3.5 grams of sodium sulphate, 4.16 gram of 50% glutaraldehyde water solution, 50 milliliters of aqueous solutions that constant volume obtains) 10 minutes.Washing, dry, collection, obtain class spider silk fiber.The main diameter of gained fiber be 17 microns, spindle pitch diameter to Height is 55~90 microns, and axial length is 80~350 microns, and spindle internode spacing is 100~2500 microns.
Embodiment 5
By 7 grams of polyvinyl alcohol (PVA 1788, Aladdin, the degree of polymerization 1700, alcoholysis degree 88%), 1.05 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 300~400 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%), be scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 75 degrees Celsius lower heating stirring 2 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times after, be placed in crosslinked fluid (11.48 gram of 98% concentrated sulfuric acid, 3.5 grams of sodium sulphate, 4.16 gram of 50% glutaraldehyde water solution, constant volume 50 milliliters of aqueous solutions) in 10 minutes.Washing, dry, collection, obtain class spider silk fiber.The main diameter of gained fiber Be 27 microns, spindle section radial height be 40~80 microns, axial length be 80~350 microns, spindle internode spacing be 100~ 2500 microns.
Embodiment 6
By 7 grams of polyvinyl alcohol (PVA 1788, Aladdin, the degree of polymerization 1700, alcoholysis degree 88%), 1.75 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 300~400 mesh, 40~70 angstroms of aperture, porosity be 40~ 60%), be scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 85 degrees Celsius lower heating stirring 3 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times after, obtain class spider silk fiber.The main diameter of gained fiber is 27 microns, and spindle section radial height is 40~80 micro- Rice, axial length are 90~370 microns, and spindle internode spacing is 100~1500 microns.
Embodiment 7
By 8 grams of polyvinyl alcohol (PVA 2499, Aladdin, the degree of polymerization 2400, alcoholysis degree 99%), 0.8 gram of column chromatography Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 100~200 mesh, 80~100 angstroms of aperture, porosity be 40~ 60%), be scattered in 42 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 90 degrees Celsius lower heating stirring 4 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 22G (diameter is 410 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 52 microns, and spindle section radial height is 80~180 micro- Rice, axial length are 170~500 microns, and spindle internode spacing is 110~3000 microns.
Embodiment 8
By 8 grams of polyvinyl alcohol (PVA 2499, Aladdin, the degree of polymerization 2400, alcoholysis degree 99%), 1.6 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 100~200 mesh, 80~100 angstroms of aperture, porosity be 40~ 60%), be scattered in 42 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 90 degrees Celsius lower heating stirring 4 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 22G (diameter is 410 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 53 microns, and spindle section radial height is 80~185 micro- Rice, axial length are 165~510 microns, and spindle internode spacing is 105~1800 microns.
Embodiment 9
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 0.7 gram of column chromatography Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of water, at 80 degrees celsius heating stirring 2 hours, obtains uniform spinning solution.In room temperature condition Under, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning: practical rate of extrusion in aqueous sodium persulfate solution (420 gram per liters) 0.02 milliliter per minute, and spinning head model 25G (diameter is 260 microns), receiving silk rate is 0.1 meter per minute, and fiber is solidifying Gu at least 5 minutes in bath;By sufficiently dry, collection, as-spun fibre is obtained;Progress hot-drawn extends to original under 165 degrees Celsius 8 times of length obtain class spider silk fiber.The main diameter of gained fiber is 30 microns, and spindle section radial height is 60~120 Micron, axial length are 90~400 microns, and spindle internode spacing is 150~4000 microns.
Embodiment 10
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 1.4 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 300~400 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of water, at 80 degrees celsius heating stirring 2 hours, obtains uniform spinning solution.In room temperature condition Under, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning: practical rate of extrusion in aqueous sodium persulfate solution (420 gram per liters) 0.02 milliliter per minute, and spinning head model 25G (diameter is 260 microns), receiving silk rate is 0.4 meter per minute, and fiber is solidifying Gu at least 5 minutes in bath;By sufficiently dry, collection, as-spun fibre is obtained;Progress hot-drawn extends to original under 165 degrees Celsius 6 times of length obtain class spider silk fiber.The main diameter of gained fiber is 18 microns, and spindle section radial height is 40~80 Micron, axial length are 70~350 microns, and spindle internode spacing is 120~2500 microns.
Embodiment 11
10 grams of polyacrylonitrile (are purchased from Sigma-Aldrich Sigma-Aldrich (Shanghai) trade Co., Ltd, weight is equal Molecular weight be 150000), 1.5 grams of column chromatography silica gels are (purchased from Qingdao base hundred million up to silica gel reagent Co., Ltd, 200~300 mesh, hole 40~70 angstroms of diameter, porosity be 40~60%), be scattered in 40 grams of n,N-Dimethylformamide (DMF), at 50 c plus Thermal agitation 3 hours, obtain uniform spinning solution.At room temperature, above-mentioned spinning solution is squeezed into solidification by peristaltic pump Spinning: practical rate of extrusion 0.02 is carried out in bath (mixed solution of water and DMF, based on 100 parts by weight of water, DMF80 parts by weight) Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn, which is carried out, in 95 DEG C waters extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 25 microns, and spindle section radial height is 55~100 microns, Axial length is 100~450 microns, and spindle internode spacing is 70~2500 microns.
It is observed through contact angle measurement, the fiber is in high humility, fiber surface formation droplet random first, Subsequent drop is to displacement at central protuberance, forming big drop around fusellal fabric.
Embodiment 12
By 8 grams of polyvinyl alcohol (PVA 1788, Aladdin, the degree of polymerization 1700, alcoholysis degree 88%), 0.8 gram of column chromatography Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 300~400 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%), be scattered in 42 grams of Isosorbide-5-Nitrae-dioxane (DMSO), 75 degrees Celsius lower heating stirring 2 hours, obtain uniform spinning Stoste.At room temperature, above-mentioned spinning solution is squeezed into coagulating bath by peristaltic pump (mixed solution of methanol and DMSO, is pressed 100 parts by weight meter of methanol, DMSO20 parts by weight) carry out spinning: 0.02 milliliter of practical rate of extrusion per minute, spinning head model 25G (diameter is 260 microns), receiving silk rate is 0.4 meter per minute, and fiber is at least 5 minutes in coagulating bath;By sufficiently dry Dry, collection, obtains as-spun fibre;It carries out being placed in crosslinked fluid after hot-drawn extends to 10 times of original length under 170 degrees Celsius In (11.48 gram of 98% concentrated sulfuric acid, 3.5 grams of sodium sulphate, 4.16 gram of 50% glutaraldehyde water solution, 50 milliliters of aqueous solutions that constant volume obtains) 10 minutes.Washing, dry, collection, obtain class spider silk fiber.The main diameter of gained fiber be 20 microns, spindle pitch diameter to Height is 38~80 microns, and axial length is 100~300 microns, and spindle internode spacing is 100~3000 microns.
Embodiment 13
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 0.35 gram of column chromatography Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 200~300 mesh, 20~30 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), heating stirring 2 hours, obtain uniform spinning at 80 degrees celsius Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 27 microns, and spindle section radial height is 52~110 micro- Rice, axial length are 80~430 microns, and spindle internode spacing is 100~3800 microns.
Embodiment 14
By 7 grams of polyvinyl alcohol (PVA 1799, Aladdin, the degree of polymerization 1700, alcoholysis degree 99%), 2.8 grams of column chromatographies Silica gel (purchased from Qingdao base hundred million reach silica gel reagent Co., Ltd, 300~400 mesh, 40~70 angstroms of aperture, porosity be 40~ 60%) it, is scattered in 43 grams of Isosorbide-5-Nitrae-dioxane (DMSO), heating stirring 2 hours, obtain uniform spinning at 80 degrees celsius Stoste.At room temperature, above-mentioned spinning solution is squeezed by peristaltic pump and carries out spinning in methanol: practical rate of extrusion 0.02 Per minute, spinning head model 25G (diameter is 260 microns), per minute for 0.1 meter, fiber is in coagulating bath for receipts silk rate for milliliter In at least 5 minutes;By sufficiently dry, collection, as-spun fibre is obtained;Hot-drawn is carried out under 180 degrees Celsius extends to original length 8 times, obtain class spider silk fiber.The main diameter of gained fiber is 25 microns, and spindle section radial height is 42~90 microns, Axial length is 80~630 microns, and spindle internode spacing is 80~900 microns.
Embodiment 15
By 5 grams of polyurethanes (being purchased from ShanDong DongChen Engineering Plastic Co., Ltd.), 1 gram of column chromatography silica gel (purchased from blueness Island base hundred million reaches silica gel reagent Co., Ltd, and 300~400 mesh, 40~70 angstroms of aperture, porosity is 40~60%), it is scattered in 15 grams In n,N-Dimethylformamide (DMF), heating stirring 2 hours at 80 DEG C obtain uniform spinning solution.In room temperature condition Under, by above-mentioned spinning solution by peristaltic pump squeeze into coagulating bath (mixed solution of water and DMF, based on 100 parts by weight of water, DMF40 Parts by weight) in carry out spinning: 0.01 milliliter of practical rate of extrusion per minute, spinning head model 25G (diameter is 260 microns), Receiving silk rate is 0.5 meter per minute, and fiber is at least 5 minutes in coagulating bath.By sufficiently dry, collection, as-spun fibre is obtained; 8 times that are stretched to original length are carried out, the polymerization described in class spider silk fiber with the bionical spider silk for characteristic of catchmenting is obtained Fibres.The main diameter of gained fiber be 24 microns, spindle section radial height be 38~79 microns, axial length be 78~ 520 microns, spindle internode spacing is 150~2300 microns.

Claims (19)

1. a kind of class spider silk polymer fiber based on column chromatography silica gel, it is characterised in that its monofilament of polymer fiber tool Have spindle section structure unit interval be distributed class spider silk microstructure, the spindle section structure unit radial height be 10~ 300 microns, preferably 20~200 microns, more preferably 30~150 microns;The axial length of the spindle section structure unit is 10~1000 microns, preferably 20~700 microns, more preferably 100~300 microns;The spacing of the spindle section structure unit It is 10~5000 microns, preferably 50~3000 microns, more preferably 100~1000 microns;
The polymer fiber includes following components based on parts by weight:
A. 100 parts of fibrous matrix polymer;
B. 1~44 parts by weight of column chromatography silica gel, preferably 3~40 parts, more preferably 5~30 parts by weight, most preferably 5~25 Parts by weight;
The average particle size of the column chromatography silica gel is 60~400 mesh, preferably 60~300 mesh, more preferably 80~300 Mesh;
The porosity of the column chromatography silica gel is 10~80%;
The aperture of the column chromatography silica gel is 0.1~200 nanometer.
2. a kind of class spider silk polymer fiber based on column chromatography silica gel according to claim 1, it is characterised in that:
The porosity of the column chromatography silica gel is 20~60%, preferably 20~50%.
3. a kind of class spider silk polymer fiber based on column chromatography silica gel according to claim 1, it is characterised in that:
The aperture of the column chromatography silica gel is 0.5~150 nanometer, more preferably 1~50 nanometer.
4. a kind of class spider silk polymer fiber based on column chromatography silica gel according to claim 1, it is characterised in that:
The polymer fiber main diameter is 5~250 microns, preferably 10~150 microns, more preferably 20~50 microns.
5. a kind of class spider silk polymer fiber based on column chromatography silica gel according to claim 1, it is characterised in that:
The fibrous matrix polymer is selected from polyacrylonitrile, polyurethanes, polyvinyl alcohol, viscose fiber, nylon, cellulose Sulphonic acid ester, cellulose acetate, polyvinyl chloride, poly- isophtalamide, poly, poly- paraphenylene terephthalamide At least one of p-phenylenediamine;Preferably polyacrylonitrile, polyurethanes, polyvinyl alcohol, viscose fiber, poly- isophthalic diformazan At least one of acyl m-phenylene diamine (MPD), poly(p-phenylene terephthalamide), polyvinyl chloride, more preferably polyacrylonitrile, poly- amino At least one of formic acid esters, polyvinyl alcohol.
6. a kind of class spider silk polymer fiber based on column chromatography silica gel according to claim 1, it is characterised in that:
The fibrous matrix polymer is selected from polyvinyl alcohol;The degree of polymerization of the polyvinyl alcohol is 400~4000, preferably 500 ~3000, more preferably 1000~2500;Alcoholysis degree is 55%~99%, preferably 88%~99%.
7. described in any item a kind of class spider silk polymer fibers based on column chromatography silica gel according to claim 1~6, by Method comprising the following steps are prepared:
(1) it disperses the fibrous matrix polymer and column chromatography silica gel additive in solvent by the dosage, heating, stirring It is dissolved in solvent to fibrous matrix polymer, column chromatography silica gel is evenly dispersed in the solution, obtains uniform spinning solution;
(2) corresponding coagulating bath is prepared;
(3) spinning solution is squeezed into coagulating bath, through supersolidification, drying, collection obtains as-spun fibre;
(4) by stretching as-spun fibre, the polymer fiber of the class spider silk with the spindle section structure being spaced apart is obtained.
8. a kind of system of the class spider silk polymer fibers based on column chromatography silica gel described in any item according to claim 1~7 Preparation Method, it is characterised in that the following steps are included:
(1) it disperses the fibrous matrix polymer and column chromatography silica gel in solvent by the dosage, heating is stirred to fiber Matrix polymer is dissolved in solvent, and column chromatography silica gel is evenly dispersed in the solution, obtains spinning solution;
(2) corresponding coagulating bath is prepared;
(3) spinning solution is squeezed into coagulating bath, through supersolidification, drying, collects, obtain as-spun fibre;
(4) by stretching as-spun fibre, the polymer fiber of the class spider silk with the spindle section structure being spaced apart is obtained.
9. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
It is in terms of 100 parts by weight of solvent in the step (1), the dosage of the fibrous matrix polymer is 5~50 parts by weight, Preferably 10~40 parts, more preferably 10~25 parts.
10. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
In the step (1), the solvent is selected from Isosorbide-5-Nitrae-dioxane, n,N-Dimethylformamide, tetrahydrofuran, water, sulfuric acid At least one of, more preferably at least one of n,N-Dimethylformamide, Isosorbide-5-Nitrae-dioxane.
11. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
In the step (1), the heating temperature is 30~95 degrees Celsius, preferably 50~95 degrees Celsius, more preferably 70~95 Degree Celsius.
12. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
In the step (2), the coagulating bath is selected from aqueous sodium persulfate solution, methanol, ethyl acetate, water, Isosorbide-5-Nitrae-dioxane, N, At least one of dinethylformamide or mixed solvent, preferably sulfuric acid sodium water solution, methanol, water, Isosorbide-5-Nitrae-dioxane, N, At least one of dinethylformamide or mixed solvent;The concentration of the aqueous sodium persulfate solution is 300~500g/L, preferably For 350~450g/L.
13. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
The fibrous matrix polymer is polyvinyl alcohol, and the solvent is Isosorbide-5-Nitrae-dioxane, and the coagulating bath is selected from methanol, second Acetoacetic ester, methanol and Isosorbide-5-Nitrae-dioxane composition at least one of binary solution;Preferably methanol or methanol and Isosorbide-5-Nitrae- The binary solution of dioxane composition;More preferably methanol, wherein the methanol and Isosorbide-5-Nitrae-dioxane composition binary solution In, it is that the parts by weight of the Isosorbide-5-Nitrae-dioxane are 0.1~50 part in terms of 100 parts by methanol weight, preferably 5~40 parts, more Preferably 10~30 parts.
14. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
When carrying out spinning using the spinning solution, the spinneret orifice internal diameter is 10~1000 microns, and preferably 50~500 is micro- Rice, more preferably 50~300 microns.
15. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
When carrying out spinning using the spinning solution, receiving silk rate is 0.01~100 meter per minute, and preferably 0.05~10 meter every Minute, more preferable 0.1~1 meter is per minute.
16. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 8, It is characterized in that:
In the step (4), the fibrous matrix polymer is polyvinyl alcohol, and draft temperature is 100~220 degrees Celsius, preferably 120~200 degrees Celsius, more preferably 150~180 degrees Celsius.
17. according to a kind of described in any item class spider silk polymer fibers based on column chromatography silica gel of claim 8~16 Preparation method, it is characterised in that it is further comprising the steps of:
Fiber obtained by step (4) is placed in crosslinked fluid and is impregnated, through washing, drying, collection to get.
18. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 17, It is characterized by:
The fibrous matrix polymer is polyvinyl alcohol, and the crosslinked fluid is acids and aldehydes and/or sodium sulphate, molten with water Liquid;The acids is inorganic acid, preferably at least one of hydrochloric acid, sulfuric acid, more preferably sulfuric acid;The aldehydes is selected from first At least one of aldehyde, glutaraldehyde.
19. a kind of preparation method of class spider silk polymer fiber based on column chromatography silica gel according to claim 18, It is characterized by:
Acids is selected from sulfuric acid in the crosslinked fluid, and aldehydes is selected from glutaraldehyde and formaldehyde;Wherein:
The concentration of the sulfuric acid is 100~500 gram per liters, preferably 200~350 gram per liters;
The concentration of the glutaraldehyde is 1~80 gram per liter, preferably 30~60 gram per liters;
The concentration of the formaldehyde is 1~50 gram per liter, preferably 20~35 gram per liters;
The concentration of the sodium sulphate is 0~350 gram per liter, preferably 50~200 gram per liters.
CN201710528437.6A 2017-07-01 2017-07-01 Spider silk-like polymer fiber based on column chromatography silica gel and preparation method thereof Active CN109208102B (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
CN201710528437.6A CN109208102B (en) 2017-07-01 2017-07-01 Spider silk-like polymer fiber based on column chromatography silica gel and preparation method thereof
PCT/CN2018/092645 WO2019007217A1 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fiber, preparation method therefor and use thereof
CN201880043553.1A CN110914488B (en) 2017-07-01 2018-06-25 Spider silk-like polymer fibers, method for producing same, and use thereof
US16/627,929 US11572638B2 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fiber, preparation method therefor and use thereof
CA3068755A CA3068755A1 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fiber, preparation method therefor and use thereof
JP2020500159A JP7353262B2 (en) 2017-07-01 2018-06-25 Spider-like polymer fibers, their production methods and their uses
EP18828449.1A EP3650587A4 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fiber, preparation method therefor and use thereof
KR1020207002521A KR102538295B1 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fibers, methods for their preparation and uses thereof
AU2018296341A AU2018296341B2 (en) 2017-07-01 2018-06-25 Spider-silk-like polymer fiber, preparation method therefor and use thereof
TW107122475A TWI786144B (en) 2017-07-01 2018-06-29 Spider silk-like polymer fiber, its preparation method and its use

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710528437.6A CN109208102B (en) 2017-07-01 2017-07-01 Spider silk-like polymer fiber based on column chromatography silica gel and preparation method thereof

Publications (2)

Publication Number Publication Date
CN109208102A true CN109208102A (en) 2019-01-15
CN109208102B CN109208102B (en) 2020-06-09

Family

ID=64991840

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710528437.6A Active CN109208102B (en) 2017-07-01 2017-07-01 Spider silk-like polymer fiber based on column chromatography silica gel and preparation method thereof

Country Status (1)

Country Link
CN (1) CN109208102B (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102776785A (en) * 2011-05-13 2012-11-14 中国科学院化学研究所 Water-collecting polymer filament imitating spider silk structure and preparation method thereof
CN103643337A (en) * 2013-12-02 2014-03-19 北京化工大学 Preparation method of beaded nanofiber
CN103952783A (en) * 2014-04-04 2014-07-30 苏州大学 Bead-like porous PLA (Poly Lactic Acid) nano fiber as well as preparation method and application thereof
CN105239206A (en) * 2015-11-03 2016-01-13 华侨大学 Polycaprolactone / polyethylene glycol (PCL / PEG) composite beaded fiber and preparation method thereof
CN105544091A (en) * 2016-01-21 2016-05-04 苏州大学 Antibacterial type nanofiber composite material and preparation method thereof
CN106012291A (en) * 2016-07-22 2016-10-12 中国石油大学(华东) Oil-water separation fiber membrane with excellent anti-pollution capability and preparation method thereof

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102776785A (en) * 2011-05-13 2012-11-14 中国科学院化学研究所 Water-collecting polymer filament imitating spider silk structure and preparation method thereof
CN103643337A (en) * 2013-12-02 2014-03-19 北京化工大学 Preparation method of beaded nanofiber
CN103952783A (en) * 2014-04-04 2014-07-30 苏州大学 Bead-like porous PLA (Poly Lactic Acid) nano fiber as well as preparation method and application thereof
CN105239206A (en) * 2015-11-03 2016-01-13 华侨大学 Polycaprolactone / polyethylene glycol (PCL / PEG) composite beaded fiber and preparation method thereof
CN105544091A (en) * 2016-01-21 2016-05-04 苏州大学 Antibacterial type nanofiber composite material and preparation method thereof
CN106012291A (en) * 2016-07-22 2016-10-12 中国石油大学(华东) Oil-water separation fiber membrane with excellent anti-pollution capability and preparation method thereof

Also Published As

Publication number Publication date
CN109208102B (en) 2020-06-09

Similar Documents

Publication Publication Date Title
CN110914488B (en) Spider silk-like polymer fibers, method for producing same, and use thereof
CN109208108A (en) A kind of class spider silk polymer fiber and preparation method thereof based on porous silica microballoon
CN106987922B (en) The cellulose nano-fibrous electrostatic spinning preparation method of hollow porous structure
CN105543995B (en) A kind of polyacrylonitrile organic aerogel fibrous material and its preparation method and application
CN104630923A (en) Method for preparing carbon nano tube modified polyacrylonitrile fibers with solution in-situ polymerization technology
CN106929929B (en) A kind of preparation method of the cellulose spin dope for electrostatic spinning
Wang et al. Nano-fiber/net structured PVA membrane: effects of formic acid as solvent and crosslinking agent on solution properties and membrane morphological structures
CN100422404C (en) Anti-wear polyvinyl alcohol aldehyde acetal fiber and its preparing method and use
CN109208109A (en) The polymer fiber and preparation method thereof of one type spider silk
CN106400305B (en) A kind of preparation method of macropore electrostatic spinning nano fiber film
CN109012638B (en) Preparation method of carboxylated hierarchical porous cellulose adsorption balls
CN109208100A (en) A kind of class spider silk polymer fiber and preparation method thereof based on polystyrene porous microballoon
Yin et al. High-throughput free surface electrospinning using solution reservoirs with different depths and its preparation mechanism study
CN105603543B (en) The silk spraying method of polyacrylonitrile solution
CN109208110A (en) A kind of class spider silk polymer fiber and preparation method thereof based on aspherical small porous particle
CN105126633B (en) Method for preparing anion-exchange membrane by electrospinning
CN109208101A (en) A kind of class spider silk polymer fiber and preparation method thereof based on spherical porous particle
CN102352537B (en) Coagulation-bath-free spinning method of polyacrylonitrile-based carbon fiber protofilament
CN109208102A (en) A kind of class spider silk polymer fiber and preparation method thereof based on column chromatography silica gel
CN109321990A (en) A kind of preparation method of super-hydrophobic Lyocell fibers
CN111235659A (en) Lyocell fiber with heat storage and insulation functions and preparation method thereof
Yang et al. Control of the morphology of micro/nanostructures of polycarbonate via electrospinning
CN110747521A (en) Three-dimensional electrostatic spinning micro-fiber scaffold with surface nano-structure and preparation method and application thereof
CN108677265A (en) A kind of filament shape fibrous material and preparation method thereof containing macrocyclic compounds
CN104195666B (en) Method for preparing polyimide fibers based on imidization of o-methyl aryl amide

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant