CN106567285A - High-strength ceramic fiber filter filter-paper - Google Patents
High-strength ceramic fiber filter filter-paper Download PDFInfo
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- CN106567285A CN106567285A CN201610996795.5A CN201610996795A CN106567285A CN 106567285 A CN106567285 A CN 106567285A CN 201610996795 A CN201610996795 A CN 201610996795A CN 106567285 A CN106567285 A CN 106567285A
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/08—Filter paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/36—Explosive disintegration by sudden pressure reduction
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/12—Pulp from non-woody plants or crops, e.g. cotton, flax, straw, bagasse
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/02—Synthetic cellulose fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/46—Non-siliceous fibres, e.g. from metal oxides
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H15/00—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
- D21H15/02—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
- D21H15/10—Composite fibres
- D21H15/12—Composite fibres partly organic, partly inorganic
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/71—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes
- D21H17/74—Mixtures of material ; Pulp or paper comprising several different materials not incorporated by special processes of organic and inorganic material
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H19/00—Coated paper; Coating material
- D21H19/10—Coatings without pigments
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/34—Ignifugeants
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/36—Biocidal agents, e.g. fungicidal, bactericidal, insecticidal agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/32—Addition to the formed paper by contacting paper with an excess of material, e.g. from a reservoir or in a manner necessitating removal of applied excess material from the paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/04—Physical treatment, e.g. heating, irradiating
- D21H25/06—Physical treatment, e.g. heating, irradiating of impregnated or coated paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/08—Rearranging applied substances, e.g. metering, smoothing; Removing excess material
Abstract
The invention discloses high-strength ceramic fiber filter filter-paper. The high-strength ceramic fiber filter filter-paper is prepared from, by weight, 60-80 parts of straw pulp, 1-2 parts of ceramic fibers, 8-10 parts of aluminum silicate fibers, 1-2 parts of sodium tripolyphosphate, 1-2 parts of an antioxidant DSTP, 0.2-0.8 part of erucyl amide, 0.5-0.6 part of zinc borate, 10-18 parts of tencel fibers, 1-2 parts of polyvinyl acetate emulsion adhesive, 1-2 parts of sodium hexametaphosphate, 1-2 parts of folium artemisiae argyi, 1-2 parts of folium isatidis, 0.1-0.2 part of melamine, 15-20 parts of styrene-acrylic emulsion, 2-4 parts of orange peels, 4-8 parts of durian shells, 5-6 parts of sugarcane peels, 1-2 parts of coconut fibers, 3-5 parts of sawdust, 0.02-0.05 part of citric acid, 0.1-0.2 part of zinc nitrate and 0.2-0.5 part of silver nitrate.
Description
Technical field
The present invention relates to cleaner technical field, more particularly to a kind of high-strength ceramic fiber filter paper of filter.
Background technology
Electromotor has air, machine oil, three kinds of cleaners of fuel oil, commonly referred to as " three filters ".They undertake electromotor respectively and enter
The filtration of medium in gas system, lubricating system and combustion system.The pattern of air filter has two kinds, i.e. dry type and wet type.It is dry
Formula air filter is by a dry type filter element, the cleaner that the impurity in air is separated by (such as paper filter element).
Air filter used by Light-duty Vehicle (contain car, minicar) is generally single-stage, and filtering material is filter paper or non-knits
Make cloth.Under nominal air volume flow, the filtration efficiency of filter element should be not less than 99.5%.Heavy goods vehicles are due to working environment
Badly, its air filter must be multistage.The first order is spiral-flow type prefilter (such as blade ring, cyclone pipe etc.), is used for
Big particle impurity is filtered, more than 80%, second level fine filtering is micropore paper filter element (filter element of commonly referred to as deciding) to filter efficiency, its
Filter efficiency is up to more than 99.5%.
Filter element is made using the filter paper of low price, because its filter paper aperture is big, lack of homogeneity, filter efficiency it is low, it is impossible to will be right
Harmful impurity is effectively filtered out, and is endangered healthy.
Ceramic fibre is a kind of fibrous light refractory material, with lightweight, high temperature resistant, heat stability be good, thermal conductivity
The advantages of low, specific heat is little and mechanical resistant shakes, thus in the industry such as machinery, metallurgy, chemical industry, oil, ceramics, glass, electronics all
It is widely used.Rising steadily due to global energy price in recent years, energy-conservation have become China national strategy, at this
Under the background of sample, obtain more in China up to the ceramic fibre of 10-30% than traditional resistance to material energy-conservations such as insulating brick and pouring materials
More wider array of application, development prospect are very good..
The content of the invention
The object of the invention is exactly for the defect for making up prior art, there is provided a kind of high-strength ceramic fiber filter
Paper.
The present invention is achieved by the following technical solutions:
A kind of high-strength ceramic fiber filter paper of filter, which is obtained by the raw material of following weight parts:Straw pulp 60-80, ceramics are fine
Dimension 1-2, alumina silicate fibre 8-10, sodium tripolyphosphate 1-2, antioxidant DSTP1-2, erucyl amide 0.2-0.8, Firebrake ZB 0.5-
0.6th, tencel fiber 10-18, Polyvinylacetate Emulsion Adhesive 1-2, sodium hexameta phosphate 1-2, Folium Artemisiae Argyi 1-2, Folium Isatidiss 1-2, three
Poly cyanamid 0.1-0.2, styrene-acrylic emulsion 15-20, orange peel 2-4, durian shell 4-8, Cortex Sacchari sinensis 5-6, coconut fibre 1-2, wood sawdust 3-5,
Citric acid 0.02-0.05, zinc nitrate 0.1-0.2, silver nitrate 0.2-0.5.
A kind of described high-strength ceramic fiber filter paper of filter, preparation method are comprised the following steps:
(1)After orange peel, durian shell, Cortex Sacchari sinensis are mixed, add water equivalent to the water of 0.6-1 times of above-mentioned raw materials, after mixing, anaerobism
After ferment 1-2 days, clean, air-dry, dry, pulverize to particle size range between 500-1000um, then after ultraviolet irradiation 30-60min,
Obtain biological powder standby;Radiating ultraviolet light wavelength is 254nm, and radiation dose is 0.5-2kJ/m2, irradiates 2-3 minutes;
(2)Citric acid adds suitable quantity of water, after being configured to the citric acid solution that concentration is 2-5%, adds biological powder, stirs at 40-60 DEG C
After mixing 0.5-1h, zinc nitrate, silver nitrate are added, after stirring, filter, use distilled water wash filtering residue, to filtrate in neutrality,
Filtering residue is added in sodium bicarbonate solution of the concentration for 2-3%, 0.5-3h is stirred at 30-50 DEG C, filtered, use distilled water wash
Filtering residue, to filtrate in neutrality, after filtering residue is dried at 50-70 DEG C, obtains final product biological load antibacterial powder standby;
(3)After styrene-acrylic emulsion is mixed with tripolycyanamide, after adding the mixing of biological load antibacterial powder, impregnation liquid is obtained standby;
(4)After Folium Artemisiae Argyi, Folium Isatidiss mix, steam explosion is carried out, explosion water vapour pressure is 0.05-0.3Mpa, blasting time is
1-3s, produces thing and is dried Jing after processed, obtain xeraphium standby;
(5)Mixed straw, tencel fiber and xeraphium by weight;Pulper size degradation is then placed in, add water suitable quantity of water, consolidate
Content is the slurry of 4-6%, adds other surplus stocks in addition to impregnation liquid, stirs and continue size degradation and obtain mixed slurry, and Jing is discongested
After machine is discongested, then defibrination, after defibrination, gained slurry is sized mixing through adding water, and copies according to conventional paper technology to solid content 3-5%
Paper, molding squeezing, to be drying to obtain forming paper standby;
(6)Forming paper is placed in impregnation liquid and impregnates 2-3h, then removes excessive impregnation liquid with pressure roll;It is permanent at 160-200 DEG C
Temperature drying Final finishing, obtains final product.
It is an advantage of the invention that:(1)Rationally, intensity is high for inventive formulation, and fire resistant flame retardant is safe, is hardly damaged, adds
Ceramic fibre is added, has been effectively increased the intensity of the present invention, ceramic fibre has been a kind of fibrous light refractory material, with weight
Gently, the advantages of high temperature resistant, heat stability be good, low thermal conductivity, specific heat are little and mechanical resistant shakes.
(2)The present invention uses impregnation liquid, serves the effect of multistage filtering, compensate for some perforations aperture between filter paper fibre
Larger defect, improves the uniformity in hole aperture between filter paper fibre, enhances sieving effect.Add biological load simultaneously
Antibacterial can be loaded by antibacterial powder, bio-carrier, slow to discharge, and antibacterial action is strong, lasting effect is good, tool broad spectrum activity and with processing
The compatible good advantage of product, various antibacterials, mycete is all had and kill well inhibitory action, to environment without any pollution.Profit
With orange peel, durian shell, Cortex Sacchari sinensis as bio-carrier, turn waste into wealth.
(3)The present invention adopts steam explosion technology, and the fiber in plant cell is bondd by lignin, steams with high temperature, high pressure
Under vapour effect, cellulose crystallity is improved, and the degree of polymerization declines, hemicellulose fraction degraded, and lignin softens, under horizontal strength of connection
Drop, when the material sudden pressure reduction full of steam, the acute expansion of the gas in hole produces " explosion " effect, raw material is torn
For fiber fines, obtained fiber slurrying has high yield pulp1, free of contamination feature..
Specific embodiment
A kind of high-strength ceramic fiber filter paper of filter, which is obtained by the raw material of following weight parts:Straw pulp 60, ceramics are fine
Dimension 1, alumina silicate fibre 8, sodium tripolyphosphate 1, antioxidant DSTP1, erucyl amide 0.2, Firebrake ZB 0.5, tencel fiber 10, poly-vinegar
Sour vac emulsion adhesive 1, sodium hexameta phosphate 1, Folium Artemisiae Argyi 1, Folium Isatidiss 1, tripolycyanamide 0.1, styrene-acrylic emulsion 15, orange peel 2, pomegranate
Lotus shell 4, Cortex Sacchari sinensis 5, coconut fibre 1, wood sawdust 3, citric acid 0.02, zinc nitrate 0.1, silver nitrate 0.2.
A kind of described high-strength ceramic fiber filter paper of filter, preparation method are comprised the following steps:
(1)After orange peel, durian shell, Cortex Sacchari sinensis are mixed, add water equivalent to the water of 0.6 times of above-mentioned raw materials, after mixing, anaerobic fermentation
After 1 day, clean, air-dry, dry, pulverize to particle size range between 500um, then after ultraviolet irradiation 30min, obtain biological powder standby
With;Radiating ultraviolet light wavelength is 254nm, and radiation dose is 0.5kJ/m2, is irradiated 2 minutes;
(2)Citric acid adds suitable quantity of water, after being configured to the citric acid solution that concentration is 2%, adds biological powder, stirs at 40 DEG C
After 0.5h, zinc nitrate, silver nitrate are added, after stirring, filter, use distilled water wash filtering residue, to filtrate in neutrality, will filter
During slag adds concentration to be 2% sodium bicarbonate solution, 0.5h is stirred at 30 DEG C, filter, use distilled water wash filtering residue, to filtrate
In neutrality, after filtering residue is dried at 50 DEG C, biological load antibacterial powder is obtained final product standby;
(3)After styrene-acrylic emulsion is mixed with tripolycyanamide, after adding the mixing of biological load antibacterial powder, impregnation liquid is obtained standby;
(4)After Folium Artemisiae Argyi, Folium Isatidiss mix, steam explosion is carried out, explosion water vapour pressure is 0.05Mpa, and blasting time is 1s, quick-fried
Go out thing to be dried Jing after processed, obtain xeraphium standby;
(5)Mixed straw, tencel fiber and xeraphium by weight;Pulper size degradation is then placed in, add water suitable quantity of water, consolidate
Content is 4% slurry, adds other surplus stocks in addition to impregnation liquid, stirs and continues size degradation and obtain mixed slurry, Jing fluffers
After discongesting, then defibrination, after defibrination, gained slurry is sized mixing through adding water, to solid content 3% according to conventional paper technology copy paper, into
Type squeezing, to be drying to obtain forming paper standby;
(6)Forming paper is placed in impregnation liquid and impregnates 2h, then removes excessive impregnation liquid with pressure roll;The constant temperature drying at 160 DEG C
Final finishing, obtains final product.
Obtained in above-described embodiment, performance of filter paper data are as follows:
Filter paper into paper air permeability in 50-60L/m2.S between, 55-60 μm of maximum diameter of hole, average pore size 35-40 μm, wet elongation
Rate≤1.8%, wet bursting strength >=350KPa, tensile strength is 16.58kNm, 11 μm of filtering accuracy <, removal of impurity >
99.0%。
Claims (2)
1. a kind of high-strength ceramic fiber filter paper of filter, it is characterised in that:Which is obtained by the raw material of following weight parts:Straw pulp
60-80, ceramic fibre 1-2, alumina silicate fibre 8-10, sodium tripolyphosphate 1-2, antioxidant DSTP1-2, erucyl amide 0.2-0.8,
Firebrake ZB 0.5-0.6, tencel fiber 10-18, Polyvinylacetate Emulsion Adhesive 1-2 are sodium hexameta phosphate 1-2, Folium Artemisiae Argyi 1-2, big
Folium Isatidis 1-2, tripolycyanamide 0.1-0.2, styrene-acrylic emulsion 15-20, orange peel 2-4, durian shell 4-8, Cortex Sacchari sinensis 5-6, coconut fibre 1-2,
Wood sawdust 3-5, citric acid 0.02-0.05, zinc nitrate 0.1-0.2, silver nitrate 0.2-0.5.
2. a kind of high-strength ceramic fiber filter paper of filter according to claim 1, it is characterised in that:Preparation method includes
Following steps:
(1)After orange peel, durian shell, Cortex Sacchari sinensis are mixed, add water equivalent to the water of 0.6-1 times of above-mentioned raw materials, after mixing, anaerobism
After ferment 1-2 days, clean, air-dry, dry, pulverize to particle size range between 500-1000um, then after ultraviolet irradiation 30-60min,
Obtain biological powder standby;Radiating ultraviolet light wavelength is 254nm, and radiation dose is 0.5-2kJ/m2, irradiates 2-3 minutes;
(2)Citric acid adds suitable quantity of water, after being configured to the citric acid solution that concentration is 2-5%, adds biological powder, stirs at 40-60 DEG C
After mixing 0.5-1h, zinc nitrate, silver nitrate are added, after stirring, filter, use distilled water wash filtering residue, to filtrate in neutrality,
Filtering residue is added in sodium bicarbonate solution of the concentration for 2-3%, 0.5-3h is stirred at 30-50 DEG C, filtered, use distilled water wash
Filtering residue, to filtrate in neutrality, after filtering residue is dried at 50-70 DEG C, obtains final product biological load antibacterial powder standby;
(3)After styrene-acrylic emulsion is mixed with tripolycyanamide, after adding the mixing of biological load antibacterial powder, impregnation liquid is obtained standby;
(4)After Folium Artemisiae Argyi, Folium Isatidiss mix, steam explosion is carried out, explosion water vapour pressure is 0.05-0.3Mpa, blasting time is
1-3s, produces thing and is dried Jing after processed, obtain xeraphium standby;
(5)Mixed straw, tencel fiber and xeraphium by weight;Pulper size degradation is then placed in, add water suitable quantity of water, consolidate
Content is the slurry of 4-6%, adds other surplus stocks in addition to impregnation liquid, stirs and continue size degradation and obtain mixed slurry, and Jing is discongested
After machine is discongested, then defibrination, after defibrination, gained slurry is sized mixing through adding water, and copies according to conventional paper technology to solid content 3-5%
Paper, molding squeezing, to be drying to obtain forming paper standby;
(6)Forming paper is placed in impregnation liquid and impregnates 2-3h, then removes excessive impregnation liquid with pressure roll;It is permanent at 160-200 DEG C
Temperature drying Final finishing, obtains final product.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113969517A (en) * | 2020-07-23 | 2022-01-25 | 杭州特种纸业有限公司 | Diesel oil filter paper and preparation method thereof |
CN114573878A (en) * | 2022-03-18 | 2022-06-03 | 潍坊潍森纤维新材料有限公司 | Preparation method and application of food-medicine grade biological cellulose transparent material |
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