CN109371742A - A kind of coaster paper and preparation method thereof - Google Patents

A kind of coaster paper and preparation method thereof Download PDF

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Publication number
CN109371742A
CN109371742A CN201811301880.0A CN201811301880A CN109371742A CN 109371742 A CN109371742 A CN 109371742A CN 201811301880 A CN201811301880 A CN 201811301880A CN 109371742 A CN109371742 A CN 109371742A
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Prior art keywords
polyethylene
paper
graphene
coaster
parts
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CN201811301880.0A
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CN109371742B (en
Inventor
王建业
吴琼华
吴安波
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Hangzhou Special Paper Industry Co Ltd
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Hangzhou Special Paper Industry Co Ltd
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • 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
    • 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
    • D01F6/46Monocomponent 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 polyolefins
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M10/00Physical treatment of fibres, threads, yarns, fabrics, or fibrous goods made from such materials, e.g. ultrasonic, corona discharge, irradiation, electric currents, or magnetic fields; Physical treatment combined with treatment with chemical compounds or elements
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/50Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with organometallic compounds; with organic compounds containing boron, silicon, selenium or tellurium atoms
    • D06M13/51Compounds with at least one carbon-metal or carbon-boron, carbon-silicon, carbon-selenium, or carbon-tellurium bond
    • D06M13/513Compounds with at least one carbon-metal or carbon-boron, carbon-silicon, carbon-selenium, or carbon-tellurium bond with at least one carbon-silicon bond
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H13/00Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
    • D21H13/10Organic non-cellulose fibres
    • D21H13/12Organic non-cellulose fibres from macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H13/14Polyalkenes, e.g. polystyrene polyethylene
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/46Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47Condensation polymers of aldehydes or ketones
    • D21H17/49Condensation polymers of aldehydes or ketones with compounds containing hydrogen bound to nitrogen
    • D21H17/50Acyclic compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/18Synthetic fibres consisting of macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/20Polyalkenes, polymers or copolymers of compounds with alkenyl groups bonded to aromatic groups

Abstract

The present invention relates to a kind of paper more particularly to a kind of coaster paper and preparation method thereof.The present invention is mainly made by following parts by weight of component: 20-30 parts of softwood pulp fiber, 20-30 parts of bamboo fibre, 30-50 parts of polyethylene particle, 0.05-0.5 parts of graphene, 5-10 parts of acrylic latex, wherein polyethylene particle and graphene melt blending, spinning, and carry out modified obtain with preferable hydrophilic dispersed and carbon dioxide adsorption polyethylene/graphene composite fibre, then with softwood pulp fiber, body paper is obtained after bamboo fibre combination copy paper, body paper is subjected to blown with carbon dioxide, make to form tiny abscess in polyethylene/graphene composite fibre, considerably increase the heat-proof quality of paper obtained, and effectively reduce the weight of paper, material is saved.

Description

A kind of coaster paper and preparation method thereof
Technical field
The present invention relates to a kind of paper more particularly to a kind of coaster paper and preparation method thereof.
Background technique
Coaster has become a kind of people's essential daily necessity in daily life, in daily life, in order to pacify Entirely and practicability, coaster needs are lightly, durable, and want in the prior art in order to reach above with excellent heat-proof quality It asks, the material for manufacturing coaster is also classified into several classes, such as wooden coaster, metal coaster, plastic cup mat and papery coaster etc., however The preparation method very complicated that above-mentioned coaster has, some then not economical environment-protective, especially papery coaster, since plain paper does not have There is thermal insulation, and intensity is not high, it is frangible to meet water, therefore papery coaster is usually disposable, and heat-insulated effect It is poor.
For example, one kind disclosed " coaster body paper and its production method ", notification number in Chinese patent literature CN104018388B, it discloses a kind of coaster body paper and its production methods.Its coaster body paper is made of surface layer, sandwich layer, bottom, The raw material slurry of each layer is two kinds of paper pulp raw materials in softwood pulp, hardwood pulp and mechanical pulp, and spray pattern shape is arranged in interlayer At stratum granulosum to improve the bond strength of layer and interlayer;The softwood pulp is bleached sulphate method softwood pulp, leaf wood Slurry is bleached sulphate method hardwood pulp, mechanical pulp is chemical bleaching thermomechanical pulp.The coaster body paper be divided into surface layer, sandwich layer, Bottom, preparation method is complex, and heat-proof quality not with higher.
Summary of the invention
In order to overcome the above problem, the present invention is prepared for a kind of dixie cup pad with good heat insulation.
To achieve the goals above, the invention adopts the following technical scheme:
A kind of coaster paper, is made by following parts by weight of component: 20-30 parts of softwood pulp fiber, 20-30 parts of bamboo fibre, and polyethylene 30-50 parts of particle, 0.05-0.5 parts of graphene, 5-10 parts of acrylic latex.
The preparation method of coaster paper the following steps are included:
(1) polyethylene particle is placed in vacuum drying oven vacuum drying, then, is melted at 140-190 DEG C with graphene Mixing, spinning obtain polyethylene/graphene composite fibre;
(2) it regard the infiltration of polyethylene/graphene complex fiber material as anode in the ammonium sulfate of 5wt%-15wt%, with Carbon-point is passed through the electric current of 1-2A/g as cathode, and 5-10min is handled at 50-75 DEG C, is then cleaned using deionized water, dries It is dry to obtain the polyethylene/graphene complex fiber material after oxidation processes;
(3) it disperses the polyethylene/graphene composite fibre after oxidation processes in ethanol solution, three second of 3- aminopropyl is added Oxysilane, flow back 12-18h at 75-90 DEG C, then washs polyethylene/graphene composite fibre using dehydrated alcohol, obtains The modified polyethylene/graphene composite fibre of 3-aminopropyltriethoxysilane;
(4) the compound fibre of polyethylene/graphene for being modified softwood pulp fiber, bamboo fibre and 3-aminopropyltriethoxysilane Dimension, which is put into 80-95 DEG C of water, impregnates 10-15h, is subsequently placed into fiberizer and carries out defibrination, refining pressure 3-5N/mm is then put Enter in beater and is beaten;
(5) acrylic latex is added in the slurry obtained by step (4), is uniformly mixed, obtains mixed slurry;
(6) mixed slurry is put into paper machine, carries out copy paper, squeezing and drying, obtains body paper;
(7) body paper is put into carbon dioxide environment, adsorbs 10-15h under the conditions of 20-40 DEG C, 10-15MPa;
(8) body paper of carbon dioxide adsorption is foamed, is cut after Temperature fall, obtain coaster paper.
The present invention mainly manufactures paper with pulp using wood pulp cellulose, bamboo fibre and polyethylene/graphene composite fibre as primary raw material together At body paper, inventor has found when inventing creation, due to not having hydrophilic radical, pure polyethylene on pure polyethylene fibre segment The hydrophily of fiber is poor, causes its dispersibility in mashing in softwood pulp fiber and bamboo fibre poor, therefore, this hair It is bright to use polyethylene particle as spinning after raw material, with a certain amount of graphene melting mixing first, obtain polyethylene/graphene Composite fibre is mixed with graphene on polyethylene/graphene composite fibre with two benefits, firstly, composite fibre can infiltrate Anode is used as in electrolyte ammonium sulfate, then using carbon-point as cathode, after being passed through electric current, on the graphene of polyethylene surface Oxygen-containing group can be adsorbed, secondly, graphene is mixed into the foaming for being conducive to later period fiber, this is because titanium dioxide before foaming During carbon adsorption, the adsorptivity of carbon dioxide can be increased by being mixed into graphene, also, graphene can also the conduct in foaming Heterogeneous nucleation point, advantageously forms abscess, when then to polyethylene/graphene composite fibre into electrochemicial oxidation, uses Ammonium sulfate as electrolyte, be due to ammonium sulfate be neutral electrolyte, if electrolyte be acidity, poly- second can be corroded Alkene/graphene composite fibre, and when electrolyte is alkalinity, it can be adsorbed with polyethylene/graphene composite fiber surface oxygen-containing Group reaction, reduces degree of oxidation, also, current density has a larger impact to the adsorbance of oxygen-containing group, when energization, if electric When current density is less than 1A/g, the electrochemical reaction of polyethylene/graphene composite fiber surface is excessively slow, and adsorbance is less, and When current density is less than 2A/g, reaction is excessively acutely to be difficult to control degree of oxidation.The compound fibre of subsequent polyethylene/graphene Dimension carries out the modification of 3-aminopropyltriethoxysilane, is not only able to improve its dispersibility in copy paper, moreover, being grafted on Amino on polyethylene/graphene composite fibre can increase the carbon dioxide adsorption of polyethylene/graphene composite fibre, have Conducive to subsequent foaming process.After polyethylene/graphene composite fibre and wood pulp cellulose and bamboo fibre are mixed with beating, it is added Acrylic latex can be improved the retention force of fiber, this is because itself just not having binding force between fiber, increase acrylic acid After latex, the surface that there is acrylic latex certain cohesive force to be adsorbed onto fiber forms condensation product, so that between fiber mutually In conjunction with effectively improving the tensile index of paper.By mixed slurry by manufacturing paper with pulp, after squeezing and being dried to obtain body paper, body paper is put Enter in carbon dioxide environment, the absorption for making surface that there is the polyethylene/graphene composite fibre of amino group to carry out carbon dioxide, It then foams, the inside of polyethylene/graphene composite fibre can generate small abscess, greatly increase the heat-insulated of coaster paper Performance obtains the coaster paper of required shape most afterwards after cooling, cutting.
Preferably, the mass fraction of graphene is in polyethylene/graphene complex fiber material described in step (1) 1 ‰ -2%.
Preferably, 3-aminopropyltriethoxysilane described in step (3) is the 2%-5% of ethyl alcohol quality.
Preferably, softwood pulp fiber described in step (4), bamboo fibre and 3-aminopropyltriethoxysilane are modified Polyethylene/graphene composite fibre mass ratio be 1:0.8-1.2:1-2.
Since polyethylene/graphene composite fibre can dramatically increase the thermal insulation of body paper after expanding, but polyethylene/stone Black alkene composite fibre is excessive or increases the production cost of body paper, and polyethylene/graphene composite fibre is in the quality in composition of raw materials Thermal insulation than lower body paper just reaches necessary requirement, and lower production costs, and commercial interest is maximized.
Preferably, beater revolving speed 20-30HZ described in step (4), the solid content of slurry is 2wt%-4wt%.
It is beaten under this condition, polyethylene/graphene composite fibre can preferably disperse in the slurry, the body paper of manufacture It can be preferably.
Preferably, the quality that acrylic latex is added described in step (5) is the 6%- relative to slurry solid content 10%.
If the quality of acrylic latex is very few, so that acrylic latex does not have enough amounts to be adsorbed on fiber, so that Binding force between fiber is inadequate, and the tensile index of body paper is unable to reach demand, the knot with the increase of acrylic acid, between fiber Resultant force increases, and tensile index can also increase therewith, but when the quality of acrylic latex is excessive, acrylic latex can be adhered to The surface of fiber generates wadding and gathers, so very big that hinder the dispersion of fiber, and tensile index is caused to decline, therefore, anti-by inventor Multiple experimental verification, it is determined that the mass range of required acrylic latex.
Preferably, the solid content of the acrylic latex is 35-45%.
Preferably, foaming condition is to carry out hot-pressing and foaming under the conditions of 70-90 DEG C, 1-3MPa in the step (8).
Body paper carries out the absorption of carbon dioxide first at 20-40 DEG C of low temperature, then at 70-90 DEG C of higher temperature, The carbon dioxide of absorption can escape, to generate abscess, and the pressure of 1-3MPa be given in foaming, this is because when foaming Body paper can expand, and pressure cannot be excessive with too small, pressure mistake when needing certain pressure to guarantee the planarization of paper, but foaming Hour, it not can guarantee the smooth of paper, when pressure is excessive, abscess can be flattened due to bearing excessive pressure, cause abscess can not Molding.
Therefore, the invention has the following beneficial effects: polyethylene particles and graphene melt blending, spinning, and are changed Property after obtain the polyethylene/graphene composite fibre with preferable hydrophilic dispersibility and carbon dioxide adsorption, then and needle Leaf wood pulp cellulose obtains body paper after bamboo fibre combination copy paper, body paper is carried out blown with carbon dioxide, answers polyethylene/graphene Tiny abscess is formed in condensating fiber, considerably increases the heat-proof quality of paper obtained, and effectively reduces the weight of paper Amount, has saved material.
Specific embodiment
The present invention program is more clearly and completely described below in conjunction with specific embodiment, it is clear that described implementation Example is only a part of the embodiment of the present invention, rather than whole embodiments.Based on the embodiments of the present invention, ordinary skill Personnel's every other embodiment obtained without making creative work, belongs to protection scope of the present invention.
Embodiment 1: the preparation of coaster paper the following steps are included:
(1) 100g polyethylene particle is placed in vacuum drying oven vacuum drying, then, is carried out at 150 DEG C with 0.5g graphene Melting mixing, spinning obtain polyethylene/graphene composite fibre;
(2) infiltration of polyethylene/graphene composite fibre is regard as anode in the ammonium sulfate of 5wt%, using carbon-point as yin Pole is passed through the electric current of 1A/g, and 7.5min is handled at 50 DEG C, is then cleaned using deionized water, after drying obtains oxidation processes Polyethylene/graphene composite fibre;
(3) it takes 50g to be scattered in 200ml ethanol solution the polyethylene/graphene composite fibre after oxidation processes, 4.2g is added 3-aminopropyltriethoxysilane, flow back 13h at 80 DEG C, then multiple using dehydrated alcohol washing polyethylene/graphene Condensating fiber 3 times, obtain the modified polyethylene/graphene composite fibre of 3-aminopropyltriethoxysilane;
(4) polyethylene/stone for being modified 25g softwood pulp fiber, 25g bamboo fibre and 40g3- aminopropyltriethoxywerene werene Black alkene composite fibre is put into the water of 2kg, in 80 DEG C of immersion 11h, is subsequently placed into fiberizer and is carried out defibrination, refining pressure is It is put into beater and is beaten after 3.5N/mm, defibrination 10min, beater revolving speed 21HZ;
(5) acrylic latex that 6.3g solid content is 37wt% is added in the slurry obtained by step (4), is uniformly mixed, is mixed Close slurry;
(6) mixed slurry is put into paper machine, carries out copy paper, squeezing and drying, obtains body paper;
(7) body paper is put into carbon dioxide environment, adsorbs 10h under the conditions of 23 DEG C, 11MPa;
(8) body paper of carbon dioxide adsorption is foamed under 72 DEG C, 1.3MPa, is cut after Temperature fall, obtain coaster paper.
Embodiment 2: the preparation of coaster paper the following steps are included:
(1) 100g polyethylene particle is placed in vacuum drying oven vacuum drying, then, is carried out at 190 DEG C with 0.3g graphene Melting mixing, spinning obtain polyethylene/graphene composite fibre;
(2) polyethylene/carbon fiber composite fibre infiltration is regard as anode in the ammonium sulfate of 12wt%, using carbon-point as yin Pole is passed through the electric current of 1.6A/g, and 5min is handled at 55 DEG C, is then cleaned using deionized water, after drying obtains oxidation processes Polyethylene/graphene composite fibre;
(3) it takes 50g to be scattered in 200ml ethanol solution the polyethylene/graphene composite fibre after oxidation processes, 5.8g is added 3-aminopropyltriethoxysilane, flow back 15h at 82 DEG C, then multiple using dehydrated alcohol washing polyethylene/graphene Condensating fiber 3 times, obtain the modified polyethylene/graphene composite fibre of 3-aminopropyltriethoxysilane;
(4) polyethylene/stone for being modified 23g softwood pulp fiber, 22g bamboo fibre and 45g3- aminopropyltriethoxywerene werene Black alkene composite fibre is put into the water of 2.3kg, in 93 DEG C of immersion 12h, is subsequently placed into fiberizer and is carried out defibrination, refining pressure is It is put into beater and is beaten after 4N/mm, defibrination 15min, beater revolving speed 23HZ;
(5) acrylic latex that 7.8g solid content is 41wt% is added in the slurry obtained by step (4), is uniformly mixed, is mixed Close slurry;
(6) mixed slurry is put into paper machine, carries out copy paper, squeezing and drying, obtains body paper;
(7) body paper is put into carbon dioxide environment, adsorbs 12h under the conditions of 30 DEG C, 12MPa;
(8) body paper of carbon dioxide adsorption is foamed under 83 DEG C, 1.8MPa, is cut after Temperature fall, obtain coaster paper.
Embodiment 3: the preparation of coaster paper the following steps are included:
(1) 100g polyethylene particle is placed in vacuum drying oven vacuum drying, then, is carried out at 180 DEG C with 0.8g graphene Melting mixing, spinning obtain polyethylene/graphene composite fibre;
(2) polyethylene/carbon fiber composite fibre infiltration is regard as anode in the ammonium sulfate of 14wt%, using carbon-point as yin Pole is passed through the electric current of 2A/g, and 9min is handled at 75 DEG C, is then cleaned using deionized water, after drying obtains oxidation processes Polyethylene/graphene composite fibre;
(3) it takes 50g to be scattered in 200ml ethanol solution the polyethylene/graphene composite fibre after oxidation processes, 8.7g is added 3-aminopropyltriethoxysilane, flow back 18h at 90 DEG C, then multiple using dehydrated alcohol washing polyethylene/graphene Condensating fiber 3 times, obtain the modified polyethylene/graphene composite fibre of 3-aminopropyltriethoxysilane;
(4) polyethylene/stone for being modified 20g softwood pulp fiber, 18g bamboo fibre and 39g3- aminopropyltriethoxywerene werene Black alkene composite fibre is put into the water of 2.5kg, in 95 DEG C of immersion 14h, is subsequently placed into fiberizer and is carried out defibrination, refining pressure is It is put into beater and is beaten after 4.5N/mm, defibrination 20min, beater revolving speed 28HZ;
(5) acrylic latex that 9.1g solid content is 45wt% is added in the slurry obtained by step (4), is uniformly mixed, is mixed Close slurry;
(6) mixed slurry is put into paper machine, carries out copy paper, squeezing and drying, obtains body paper;
(7) body paper is put into carbon dioxide environment, adsorbs 15h under the conditions of 35 DEG C, 14.3MPa;
(8) body paper of carbon dioxide adsorption is foamed under 90 DEG C, 2.8MPa, is cut after Temperature fall, obtain coaster paper.
Comparative example 1: the difference from embodiment 1 is that, it is put into paper machine in mixed slurry, carries out copy paper, squeezing and do It is dry, after obtaining body paper, without blown with carbon dioxide, coaster paper is obtained after being directly over cutting.
Then, different embodiments and comparative example 1 are carried out with the measurement of thermal coefficient using hot plate method, measurement data is as follows.
By upper table data it is found that in comparative example 1 relative to the comparative example not foamed, after foaming in embodiment 1 Paper thermal coefficient is decreased obviously, and is illustrated that heat-proof quality has and is significantly promoted.
Comparative example 2: the difference from embodiment 1 is that, when polyethylene/graphene composite fibre oxidation processes, the electricity of energization Current density is 0.3A/g.
Comparative example 3: the difference from embodiment 1 is that, when polyethylene/graphene composite fibre oxidation processes, the electricity of energization Current density is 1.5A/g.
Current density is different when oxidation processes, and the hydrophily of polyethylene/graphene composite fibre is different, to coaster paper Tensile index has large effect, as a result as shown in the table.
Tensile index (Nm/g)
Embodiment 1 20.3
Comparative example 2 14.5
Comparative example 3 15.3
By upper table data it is found that current density is excessive and too small, the tensile index of paper can be declined.
Comparative example 4: the difference from embodiment 1 is that, the pressure to foam in step (8) is 0.5Mpa.
Comparative example 5: the difference from embodiment 1 is that, the pressure to foam in step (8) is 5Mpa.
The pressure of foaming will affect coaster paper foaming degree and planarization, to influence the thermal insulation of coaster paper, use heat Plate method carries out the measurement of thermal coefficient, and measurement data is as follows.
Thermal coefficient (W/mk) Planarization
Embodiment 1 0.048 Out-of-flatness
Comparative example 4 0.53 It is smooth
Comparative example 5 0.94 It is smooth
By upper table data it is found that pressure is too small, the planarization of coaster paper is poor, but when pressure is excessive, coaster paper it is heat-insulated Property can be declined.

Claims (9)

1. a kind of coaster paper, which is characterized in that be made by following parts by weight of component: 20-30 parts of softwood pulp fiber, bamboo fibre 20-30 parts, 30-50 parts of polyethylene particle, 0.05-0.5 parts of graphene, 5-10 parts of acrylic latex.
2. a kind of preparation method of coaster paper described in claim 1, which comprises the following steps:
(1) polyethylene particle is placed in vacuum drying oven vacuum drying, then, is melted at 140-190 DEG C with graphene Mixing, spinning obtain polyethylene/graphene composite fibre;
(2) infiltration of polyethylene/graphene complex fiber material is regard as anode in the ammonium sulfate of 5wt%-15wt%, with carbon Stick is passed through the electric current of 1-2A/g as cathode, and 5-10min is handled at 50-75 DEG C, is then cleaned using deionized water, drying Polyethylene/graphene complex fiber material after obtaining oxidation processes;
(3) it disperses the polyethylene/graphene composite fibre after oxidation processes in ethanol solution, three second of 3- aminopropyl is added Oxysilane, flow back 12-18h at 75-90 DEG C, then washs polyethylene/graphene composite fibre using dehydrated alcohol, obtains The modified polyethylene/graphene composite fibre of 3-aminopropyltriethoxysilane;
(4) the compound fibre of polyethylene/graphene for being modified softwood pulp fiber, bamboo fibre and 3-aminopropyltriethoxysilane Dimension, which is put into 80-95 DEG C of water, impregnates 10-15h, is subsequently placed into fiberizer and carries out defibrination, refining pressure 3-5N/mm is then put Enter in beater and is beaten;
(5) acrylic latex is added in the slurry obtained by step (4), is uniformly mixed, obtains mixed slurry;
(6) mixed slurry is put into paper machine, carries out copy paper, squeezing and drying, obtains body paper;
(7) body paper is put into carbon dioxide environment, adsorbs 10-15h under the conditions of 20-40 DEG C, 10-15MPa;
(8) by the body paper of carbon dioxide adsorption: foaming, cut after Temperature fall, obtain coaster paper.
3. the preparation method of coaster paper according to claim 2, which is characterized in that polyethylene/graphene described in step (1) The mass fraction of graphene is 1 ‰ -2% in complex fiber material.
4. the preparation method of coaster paper according to claim 2, which is characterized in that 3- aminopropyl three described in step (3) Ethoxysilane is the 2%-5% of ethanol solution quality.
5. the preparation method of coaster paper according to claim 2, which is characterized in that softwood pulp fiber described in step (4), The mass ratio for the polyethylene/graphene composite fibre that bamboo fibre and 3-aminopropyltriethoxysilane are modified is 1:0.8-1.2: 1-1.4。
6. the preparation method of coaster paper according to claim 2, which is characterized in that beater revolving speed 20- described in step (4) 30HZ, the solid content of slurry are 2wt%-4wt%.
7. the preparation method of coaster paper according to claim 2, which is characterized in that acrylate glue is added described in (5) in step The quality of cream is the 6%-10% relative to slurry solid content.
8. the preparation method of coaster paper according to claim 7, which is characterized in that the solid content of the acrylic latex is 35wt%-45wt%。
9. the preparation method of coaster paper according to claim 2, which is characterized in that foaming is in 70-90 in the step (8) DEG C, hot-pressing and foaming is carried out under the conditions of 1-3MPa.
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