CN108842519A - A kind of method of environmentally protective manufacture high-quality air filter paper - Google Patents

A kind of method of environmentally protective manufacture high-quality air filter paper Download PDF

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Publication number
CN108842519A
CN108842519A CN201810701761.8A CN201810701761A CN108842519A CN 108842519 A CN108842519 A CN 108842519A CN 201810701761 A CN201810701761 A CN 201810701761A CN 108842519 A CN108842519 A CN 108842519A
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China
Prior art keywords
weight
filter paper
paper
preparation
air filter
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CN201810701761.8A
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Chinese (zh)
Inventor
高云
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Jingxian County Dao Wang Environmental Protection Technology Co Ltd
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Jingxian County Dao Wang Environmental Protection Technology Co Ltd
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Priority to CN201810701761.8A priority Critical patent/CN108842519A/en
Publication of CN108842519A publication Critical patent/CN108842519A/en
Withdrawn legal-status Critical Current

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    • 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
    • D21H27/08Filter paper
    • 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
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • 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
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/12Pulp from non-woody plants or crops, e.g. cotton, flax, straw, bagasse
    • 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
    • D21H11/00Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/14Secondary fibres
    • 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
    • D21H13/02Synthetic cellulose fibres
    • 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
    • D21H13/36Inorganic fibres or flakes
    • D21H13/38Inorganic fibres or flakes siliceous
    • D21H13/40Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
    • 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
    • D21H15/00Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
    • D21H15/02Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
    • D21H15/10Composite fibres
    • D21H15/12Composite fibres partly organic, partly inorganic
    • 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
    • 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
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/25Cellulose
    • D21H17/26Ethers thereof
    • 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
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/30Alginic acid or alginates
    • 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
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/675Oxides, hydroxides or carbonates
    • 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
    • D21H17/63Inorganic compounds
    • D21H17/67Water-insoluble compounds, e.g. fillers, pigments
    • D21H17/68Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays
    • 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/20Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/24Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/16Sizing or water-repelling agents
    • 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/18Reinforcing agents
    • 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/36Biocidal agents, e.g. fungicidal, bactericidal, insecticidal agents
    • 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
    • D21H21/00Non-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
    • D21H21/14Non-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
    • D21H21/38Corrosion-inhibiting agents or anti-oxidants
    • 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
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22Addition to the formed paper
    • D21H23/70Multistep processes; Apparatus for adding one or several substances in portions or in various ways to the paper, not covered by another single group of this main group
    • 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
    • D21H25/00After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/04Physical treatment, e.g. heating, irradiating
    • D21H25/06Physical treatment, e.g. heating, irradiating of impregnated or coated paper

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Pest Control & Pesticides (AREA)
  • Paper (AREA)

Abstract

The invention discloses a kind of methods of environmentally protective manufacture high-quality air filter paper, include the following steps:Step 1: the preparation of reaction mixture, Step 2: the preparation of mixed serum, Step 3: composite fibre slurry is produced, Step 4: the preparation of mixed-powder, Step 5: mixing paste preparation, Step 6: paper tire tentatively produce and Step 7: paper tire coating be dried to obtain final air filter paper.Air filter paper air permeability prepared by the present invention is preferable; it is lower to gas-flow resistance; filter efficiency is excellent; filter paper has the function of the plant fragrance of a flower, antimycotic antiseptic, effective mosquito expelling, while the resistance to deformation of filter paper, resistance to compression difference ability and bursting strength have preferable performance, furthermore uses a large amount of wastes; it reduces costs; environment is protected, resource, practical value with higher and good application prospect have been saved.

Description

A kind of method of environmentally protective manufacture high-quality air filter paper
Technical field
The present invention relates to technical field of air purification, and in particular to a kind of side of environmentally protective manufacture high-quality air filter paper Method.
Background technique
Air conditioner filter element is most common component in each vehicle, and air outside vehicle is sent into car by filtering, is played The effect of improvement in-car air quality, and main component of the air filter paper as air conditioner filter element, decide high efficiency particulate air filter Filter efficiency.The fibre diameter of air filter paper is smaller, removes the partial size of particle in air with regard to smaller, filter efficiency is also got over Height, but opposite windage is bigger, the rate of filtration is slower, and dust containing capacity reduces, and traditional single filter paper filter effect is bad, It is easy that raw bacterium is mouldy, and filter paper mechanical strength and durability are bad, can no longer meet people and the air environment of high-quality is wanted It asks, therefore a kind of filter efficiency of demand is high, the air filter paper of the big composite highly effective of dust containing capacity.
Summary of the invention
In view of the drawbacks of the prior art, the object of the present invention is to provide a kind of environmentally protective manufacture high-quality air filter papers The air filter paper of method, this method preparation has the function of that the plant fragrance of a flower, antimycotic antiseptic, effective mosquito expelling, paper are smooth It is flexible, be not easy to wrinkle, tensile strength it is higher, furthermore use a large amount of agricultural wastes, reduce costs, protect environment, Resource, ecological, environmental protective function with higher are saved, while preparation method of the invention, raw material are easy to get, cost is relatively low, work Skill is simple, practical value with higher and good application prospect.
The present invention solves technical problem and adopts the following technical scheme that:
The present invention provides a kind of method of environmentally protective manufacture high-quality air filter paper, following steps:
Step 1: by polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and polyether polyol According to weight ratio 4:6:1:It is heated to 74-80 DEG C in 3 addition reactors, while with gentle nitrogen purge and with speed of agitator It is stirred 20-30% minutes under 300-400r/min, obtains reaction mixture, 55-60 DEG C of water-bath heat preservation is spare;
Step 2: waste paper, which is sent into pulper, carries out size degradation, then mashing deinking is carried out to waste paper, the paper pulp after being beaten deinking flows into Stock tank obtains secondary stock stoste, is added into secondary stock stoste and accounts for stoste weight 6%-8% viscose rayon, and is carried out with stirring rod Stirring, prevents fiber from precipitating, it is spare to obtain mixed serum;
Step 3: according to weight ratio 3:Wood pulp cellulose and straw pulp fiber are put into blender, stirring to pulp 7-9min by 1, so that planting Fibres are uniformly dispersed in water, and wherein wood pulp cellulose is by softwood pulp fiber and hardwood pulp fiber according to weight ratio 1:4 Composition, then the plant fiber for having broken slurry and step 2 are prepared into mixed serum and injected in charging basket after evenly mixing, it is fine to obtain mixing Slurry is tieed up, is stirred at low speed spare;
Step 4: by shell powder, bentonite, mica stone powder and attapulgite according to 3:2:1:2 are mixed and in pH value are Acid water washing is carried out under conditions of 5.2-5.4, then with clear water foam washing, using spray drying, then by the mixture after drying Preliminary crushing is calcined at 680-700 DEG C, then is sequentially added into mixture and accounted for the nano-titanium dioxide of its weight 1% and account for The graphene of its weight 0.5% is put into ball mill the ball milling at revolving speed 300-400r/min and obtains nanometer grade powder, to nanoscale The four acicular type zinc oxide crystal whisker for accounting for its weight 4% is added in powder, then is added into mixture and accounts for the nano oxidized of its weight 1% It is spare to be uniformly mixing to obtain mixed-powder for zinc;
Step 5: by tapioca, quaternary ammonium starch ethers, cycloheptaamylose according to weight ratio 8:1:1 is uniformly mixing to obtain mixture, Add the tricresyl phosphate of alkyl glycosides, 3% for being equivalent to its weight 5%, the deionized water of 70-80% and 20-30% Organic solvent, be stirred until homogeneous, it is to react 40min in 200W ultrasonic wave that power is placed at being 50 DEG C in temperature, is mixed Paste;
Step 6: by the mixing of the mixed serum of step 2 preparation, the composite fibre slurry of step 3 preparation and step 4 preparation Powder is according to weight ratio 4:9:2 addition stirrer for mixing are uniform, the slurry injection wet-laying equipment after uniform mixing, After being shaken up and down using stripper plate, timely quickly exclusion moisture, the fiber networking on forming net in the presence of hydraulic pressure, then will examination Sample be pressed further by removed from forming net after moisture standing and drying obtain water content be lower than 10% paper tire;
Step 7: by the reaction mixture of step 1 preparation and the mixing paste of step 5 preparation according to weight ratio 5:3 are added In blender, it is uniformly mixing to obtain dipping just liquid at being 50 DEG C in temperature, adds the plant sterilization for accounting for and impregnating just liquid weight 5% Flavouring extracting solution continues stirring 20-30 minutes, obtains maceration extract;
The plant sterilization flavouring extracts liquid and preparation method thereof:By weight by 0.1 part of deinsectization polyester, 1.5 parts of matrine, cloves 5 parts of extracting solution 5 parts of fish pelargonium extracting solution, 10 parts of ethyl alcohol, in 16 parts of feeding blenders of 6 parts of bracketplant leaching liquid and water, is in temperature 40 DEG C, speed of agitator is to stir 30 minutes under 250r/min;
Step 8: the gluten fortifier solution for being first 5% by paper tire two sides brushing quality score, uses the side of print roll coating again after drying in the shade Maceration extract is coated on the paper tire two sides of step 6 preparation by formula, then by the paper tire after coating temperature be at 90-98 DEG C it is dry, i.e., ?.
Preferably, mixture further includes the chitosan for accounting for its weight 10% in the step 5.
Preferably, mixture further includes the mixed rare earth chlorides for accounting for its weight 5% in the step 5.
Preferably, also added with the sodium alginate for accounting for its weight 0.2% respectively in the composite fibre slurry in the step 3 With 0.5% sodium carboxymethylcellulose.
Preferably, the step 3 medium-height grass pulp fibres are by discarded rice straw, straw and reed according to weight ratio 4:3:2 Composition.
Preferably, stirring to pulp uses medium consistency refining mode in the step 3.
Preferably, mixed serum is obtained in the step 2 be also added with the glass fibre for accounting for its weight 4%.
Compared with prior art, the present invention has following beneficial effect:
(1)The method of environmentally protective manufacture high-quality air filter paper of the invention is by wood pulp cellulose and straw pulp fiber and viscose rayon And the secondary stock slurry mixing in waste paper, eliminate original microdefect of single fiber raw material, a variety of thicknesses are different, The different fiber synergistic effect of toughness, while the four acicular type zinc oxide crystal whisker increased fiber interaction area and interface knot used With joint efforts, it so that filter paper has preferable mechanical strength and endurance, while being formed after being squeezed by wet-laying web-forming equipment Preliminary paper tire, so that paper structure is stablized, clearance rate is ideal between fiber, and air penetrability is preferable, at the same add by conch meal End, bentonite, mica stone powder and attapulgite form mixed-powder, on the one hand promote paper molding, improve paper On the other hand intensity also improves the strainability of filter paper, mixed-powder has preferable absorption property, can be in air Dust, pollution gas have preferable suction-operated, and furthermore there are also preferable bactericidal effects for shell powder.
(2)The method of the environmentally protective manufacture high-quality air filter paper of one kind of the invention uses the maceration extract of preparation Polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and a variety of chemical substances of polyether polyol and Tapioca, quaternary ammonium starch ethers, cycloheptaamylose are primary raw material, and the maceration extract modest viscosity of formation can effectively improve filter The tensile strength of paper, the synergistic effect of a variety of chemical substances effectively improve the mechanical property of paper, enhance its tensile property starch Introducing improve the peel strength of maceration extract, its antioxygenic property can be improved in cycloheptaamylose, so that maceration extract has been not easy Bubble, while stability is also greatly improved, period of storage also greatly improves.
(3)The paper tire of preparation is coated by the method for the environmentally protective manufacture high-quality air filter paper of one kind of the invention again The maceration extract of preparation can effectively improve the physical performance index of filter paper, predominantly tensile strength, bursting strength and stiffness, energy Enough make to form discrete face connection between paper tire fiber, slight crosslinking occurs between fiber, so that the mechanical strength of paper increases Greatly, there are also preferable water resistances, and the amount of coating furthermore can be effectively controlled by the way of print roll coating, can reduce and be produced into Sheet and raising production efficiency.
(4)It is also added in the maceration extract of the method for the environmentally protective manufacture high-quality air filter paper of one kind of the invention and accounts for it On the one hand the plant sterilization flavouring extracting solution of weight 5% can allow the filter paper paper prepared to have certain sterilization, expelling parasite desinsection energy On the other hand power makes it have certain plant fragrance of a flower, is effectively improved indoor air.
(5)It is used in the maceration extract that the method for the environmentally protective manufacture high-quality air filter paper of one kind of the invention uses useless The composition of paper and certain straw pulp, wood pulp, reduces costs, and takes full advantage of waste, has saved resource, reduces tree The excessive felling of wood, bamboo, has achieved the effect that ecological, environmental protective.
(6)The air filter paper air permeability of preparation of the invention is preferable, and lower to gas-flow resistance, filter efficiency is excellent, filter Paper has the function of the plant fragrance of a flower, antimycotic antiseptic, effective mosquito expelling, while the resistance to deformation of filter paper, resistance to compression difference ability and resistance to Broken degree has preferable performance, furthermore uses a large amount of wastes, reduces costs, protect environment, saved resource, have Higher practical value and good application prospect.
Specific embodiment
Combined with specific embodiments below, technical scheme in the embodiment of the invention is clearly and completely described, shows So, described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.Based on the reality in the present invention Example is applied, every other embodiment obtained by those of ordinary skill in the art without making creative efforts all belongs to In the scope of protection of the invention.
Embodiment 1.
A kind of method of environmentally protective manufacture high-quality air filter paper, includes the following steps:
Step 1: by polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and polyether polyol According to weight ratio 4:6:1:74 DEG C are heated in 3 addition reactors, while with gentle nitrogen purge and with speed of agitator It is stirred 20 minutes under 300r/min, obtains reaction mixture, 55 DEG C of water-bath heat preservations are spare;
Step 2: waste paper, which is sent into pulper, carries out size degradation, then mashing deinking is carried out to waste paper, the paper pulp after being beaten deinking flows into Stock tank obtains secondary stock stoste, is added into secondary stock stoste and accounts for 6% viscose rayon of stoste weight, and is stirred with stirring rod It mixes, prevents fiber from precipitating, it is spare to obtain mixed serum;
Step 3: according to weight ratio 3:Wood pulp cellulose and straw pulp fiber are put into blender, stirring to pulp 7min, so that plant by 1 Fiber is uniformly dispersed in water, and wherein wood pulp cellulose is by softwood pulp fiber and hardwood pulp fiber according to weight ratio 1:4 groups At, then the plant fiber for having broken slurry and step 2 are prepared into mixed serum and injected in charging basket after evenly mixing, obtain composite fibre Slurry stirs at low speed spare;
Step 4: by shell powder, bentonite, mica stone powder and attapulgite according to 3:2:1:2 are mixed and in pH value are Acid water washing is carried out under conditions of 5.2, then with clear water foam washing, using spray drying, then by the mixture after drying 680 Calcined at DEG C it is preliminary crush, then sequentially add into mixture and to account for the nano-titanium dioxide of its weight 1% and account for its weight 0.5% Graphene be put into ball mill the ball milling at revolving speed 300r/min and obtain nanometer grade powder, be added into nanometer grade powder and account for it The four acicular type zinc oxide crystal whisker of weight 4%, then the nano zine oxide for accounting for its weight 1% is added into mixture, it is uniformly mixing to obtain Mixed-powder is spare;
Step 5: by tapioca, quaternary ammonium starch ethers, cycloheptaamylose according to weight ratio 8:1:1 is uniformly mixing to obtain mixture, Add the tricresyl phosphate of alkyl glycosides, 3% for being equivalent to its weight 5%, 70% deionized water and 20% it is organic Solvent is stirred until homogeneous, and it is to react 40min in 200W ultrasonic wave that power is placed at being 50 DEG C in temperature, obtains mixing paste Object;
Step 6: by the mixing of the mixed serum of step 2 preparation, the composite fibre slurry of step 3 preparation and step 4 preparation Powder is according to weight ratio 4:9:2 addition stirrer for mixing are uniform, the slurry injection wet-laying equipment after uniform mixing, After being shaken up and down using stripper plate, timely quickly exclusion moisture, the fiber networking on forming net in the presence of hydraulic pressure, then will examination Sample be pressed further by removed from forming net after moisture standing and drying obtain water content be lower than 10% paper tire;
Step 7: by the reaction mixture of step 1 preparation and the mixing paste of step 5 preparation according to weight ratio 5:3 are added In blender, it is uniformly mixing to obtain dipping just liquid at being 50 DEG C in temperature, adds the plant sterilization for accounting for and impregnating just liquid weight 5% Flavouring extracting solution continues stirring 20 minutes, obtains maceration extract;
The plant sterilization flavouring extracts liquid and preparation method thereof:By weight by 0.1 part of deinsectization polyester, 1.5 parts of matrine, cloves 5 parts of extracting solution 5 parts of fish pelargonium extracting solution, 10 parts of ethyl alcohol, in 16 parts of feeding blenders of 6 parts of bracketplant leaching liquid and water, is in temperature 40 DEG C, speed of agitator is to stir 30 minutes under 250r/min;
Step 8: the gluten fortifier solution for being first 5% by paper tire two sides brushing quality score, uses the side of print roll coating again after drying in the shade Formula by maceration extract be coated on step 6 preparation paper tire two sides, then by the paper tire after coating temperature be 90 DEG C at dry to get. Mixture further includes the chitosan for accounting for its weight 10% in step five in the present embodiment.
Mixture further includes the mixed rare earth chlorides for accounting for its weight 5% in step five in the present embodiment.
Also added with the alginic acid for accounting for its weight 0.2% respectively in composite fibre slurry in step three in the present embodiment Sodium and 0.5% sodium carboxymethylcellulose.
Step three medium-height grass pulp fibres in the present embodiment are by discarded rice straw, straw and reed according to weight ratio 4:3: 2 compositions.
Stirring to pulp uses medium consistency refining mode in step three in the present embodiment.
Mixed serum is obtained in step two in the present embodiment is also added with the glass fibre for accounting for its weight 4%.
Embodiment 2.
A kind of method of environmentally protective manufacture high-quality air filter paper, includes the following steps:
Step 1: by polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and polyether polyol According to weight ratio 4:6:1:80 DEG C are heated in 3 addition reactors, while with gentle nitrogen purge and with speed of agitator It is stirred 30% minute under 400r/min, obtains reaction mixture, 60 DEG C of water-bath heat preservations are spare;
Step 2: waste paper, which is sent into pulper, carries out size degradation, then mashing deinking is carried out to waste paper, the paper pulp after being beaten deinking flows into Stock tank obtains secondary stock stoste, is added into secondary stock stoste and accounts for 8% viscose rayon of stoste weight, and is stirred with stirring rod It mixes, prevents fiber from precipitating, it is spare to obtain mixed serum;
Step 3: according to weight ratio 3:Wood pulp cellulose and straw pulp fiber are put into blender, stirring to pulp 9min, so that plant by 1 Fiber is uniformly dispersed in water, and wherein wood pulp cellulose is by softwood pulp fiber and hardwood pulp fiber according to weight ratio 1:4 groups At, then the plant fiber for having broken slurry and step 2 are prepared into mixed serum and injected in charging basket after evenly mixing, obtain composite fibre Slurry stirs at low speed spare;
Step 4: by shell powder, bentonite, mica stone powder and attapulgite according to 3:2:1:2 are mixed and in pH value are Acid water washing is carried out under conditions of 5.4, then with clear water foam washing, using spray drying, then by the mixture after drying 700 Calcined at DEG C it is preliminary crush, then sequentially add into mixture and to account for the nano-titanium dioxide of its weight 1% and account for its weight 0.5% Graphene be put into ball mill the ball milling at revolving speed 400r/min and obtain nanometer grade powder, be added into nanometer grade powder and account for it The four acicular type zinc oxide crystal whisker of weight 4%, then the nano zine oxide for accounting for its weight 1% is added into mixture, it is uniformly mixing to obtain Mixed-powder is spare;
Step 5: by tapioca, quaternary ammonium starch ethers, cycloheptaamylose according to weight ratio 8:1:1 is uniformly mixing to obtain mixture, Add the tricresyl phosphate of alkyl glycosides, 3% for being equivalent to its weight 5%, 80% deionized water and 30% it is organic Solvent is stirred until homogeneous, and it is to react 40min in 200W ultrasonic wave that power is placed at being 50 DEG C in temperature, obtains mixing paste Object;
Step 6: by the mixing of the mixed serum of step 2 preparation, the composite fibre slurry of step 3 preparation and step 4 preparation Powder is according to weight ratio 4:9:2 addition stirrer for mixing are uniform, the slurry injection wet-laying equipment after uniform mixing, After being shaken up and down using stripper plate, timely quickly exclusion moisture, the fiber networking on forming net in the presence of hydraulic pressure, then will examination Sample be pressed further by removed from forming net after moisture standing and drying obtain water content be lower than 10% paper tire;
Step 7: by the reaction mixture of step 1 preparation and the mixing paste of step 5 preparation according to weight ratio 5:3 are added In blender, it is uniformly mixing to obtain dipping just liquid at being 50 DEG C in temperature, adds the plant sterilization for accounting for and impregnating just liquid weight 5% Flavouring extracting solution continues stirring 30 minutes, obtains maceration extract;
The plant sterilization flavouring extracts liquid and preparation method thereof:By weight by 0.1 part of deinsectization polyester, 1.5 parts of matrine, cloves 5 parts of extracting solution 5 parts of fish pelargonium extracting solution, 10 parts of ethyl alcohol, in 16 parts of feeding blenders of 6 parts of bracketplant leaching liquid and water, is in temperature 40 DEG C, speed of agitator is to stir 30 minutes under 250r/min;
Step 8: the gluten fortifier solution for being first 5% by paper tire two sides brushing quality score, uses the side of print roll coating again after drying in the shade Formula by maceration extract be coated on step 6 preparation paper tire two sides, then by the paper tire after coating temperature be 98 DEG C at dry to get.
The increasing muscle that paper tire is also before the coating 5% in paper tire two sides brushing quality score in step seven in the present embodiment Agent solution.
Also added with the nano zine oxide for accounting for its weight 1% in mixed-powder in step four in the present embodiment.
Mixture further includes the chitosan for accounting for its weight 10% in step five in the present embodiment.
Mixture further includes the mixed rare earth chlorides for accounting for its weight 5% in step five in the present embodiment.
Also added with the alginic acid for accounting for its weight 0.2% respectively in composite fibre slurry in step three in the present embodiment Sodium and 0.5% sodium carboxymethylcellulose.
Step three medium-height grass pulp fibres in the present embodiment are by discarded rice straw, straw and reed according to weight ratio 4:3: 2 compositions.
Stirring to pulp uses medium consistency refining mode in step three in the present embodiment.
Mixed serum is obtained in step two in the present embodiment is also added with the glass fibre for accounting for its weight 4%.
Embodiment 3.
A kind of method of environmentally protective manufacture high-quality air filter paper, includes the following steps:
Step 1: by polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and polyether polyol According to weight ratio 4:6:1:77 DEG C are heated in 3 addition reactors, while with gentle nitrogen purge and with speed of agitator It is stirred 25% minute under 350r/min, obtains reaction mixture, 57 DEG C of water-bath heat preservations are spare;
Step 2: waste paper, which is sent into pulper, carries out size degradation, then mashing deinking is carried out to waste paper, the paper pulp after being beaten deinking flows into Stock tank obtains secondary stock stoste, is added into secondary stock stoste and accounts for 7% viscose rayon of stoste weight, and is stirred with stirring rod It mixes, prevents fiber from precipitating, it is spare to obtain mixed serum;
Step 3: according to weight ratio 3:Wood pulp cellulose and straw pulp fiber are put into blender, stirring to pulp 8min, so that plant by 1 Fiber is uniformly dispersed in water, and wherein wood pulp cellulose is by softwood pulp fiber and hardwood pulp fiber according to weight ratio 1:4 groups At, then the plant fiber for having broken slurry and step 2 are prepared into mixed serum and injected in charging basket after evenly mixing, obtain composite fibre Slurry stirs at low speed spare;
Step 4: by shell powder, bentonite, mica stone powder and attapulgite according to 3:2:1:2 are mixed and in pH value are Acid water washing is carried out under conditions of 5.3, then with clear water foam washing, using spray drying, then by the mixture after drying 690 Calcined at DEG C it is preliminary crush, then sequentially add into mixture and to account for the nano-titanium dioxide of its weight 1% and account for its weight 0.5% Graphene be put into ball mill the ball milling at revolving speed 350r/min and obtain nanometer grade powder, be added into nanometer grade powder and account for it The four acicular type zinc oxide crystal whisker of weight 4%, then the nano zine oxide for accounting for its weight 1% is added into mixture, it is uniformly mixing to obtain Mixed-powder is spare;
Step 5: by tapioca, quaternary ammonium starch ethers, cycloheptaamylose according to weight ratio 8:1:1 is uniformly mixing to obtain mixture, Add the tricresyl phosphate of alkyl glycosides, 3% for being equivalent to its weight 5%, 75% deionized water and 25% it is organic Solvent is stirred until homogeneous, and it is to react 40min in 200W ultrasonic wave that power is placed at being 50 DEG C in temperature, obtains mixing paste Object;
Step 6: by the mixing of the mixed serum of step 2 preparation, the composite fibre slurry of step 3 preparation and step 4 preparation Powder is according to weight ratio 4:9:2 addition stirrer for mixing are uniform, the slurry injection wet-laying equipment after uniform mixing, After being shaken up and down using stripper plate, timely quickly exclusion moisture, the fiber networking on forming net in the presence of hydraulic pressure, then will examination Sample be pressed further by removed from forming net after moisture standing and drying obtain water content be lower than 10% paper tire;
Step 7: by the reaction mixture of step 1 preparation and the mixing paste of step 5 preparation according to weight ratio 5:3 are added In blender, it is uniformly mixing to obtain dipping just liquid at being 50 DEG C in temperature, adds the plant sterilization for accounting for and impregnating just liquid weight 5% Flavouring extracting solution continues stirring 25 minutes, obtains maceration extract;
The plant sterilization flavouring extracts liquid and preparation method thereof:By weight by 0.1 part of deinsectization polyester, 1.5 parts of matrine, cloves 5 parts of extracting solution 5 parts of fish pelargonium extracting solution, 10 parts of ethyl alcohol, in 16 parts of feeding blenders of 6 parts of bracketplant leaching liquid and water, is in temperature 40 DEG C, speed of agitator is to stir 30 minutes under 250r/min;
Step 8: the gluten fortifier solution for being first 5% by paper tire two sides brushing quality score, uses the side of print roll coating again after drying in the shade Formula by maceration extract be coated on step 6 preparation paper tire two sides, then by the paper tire after coating temperature be 94 DEG C at dry to get.
Mixture further includes the chitosan for accounting for its weight 10% in step five in the present embodiment.
Mixture further includes the mixed rare earth chlorides for accounting for its weight 5% in step five in the present embodiment.
Also added with the alginic acid for accounting for its weight 0.2% respectively in composite fibre slurry in step three in the present embodiment Sodium and 0.5% sodium carboxymethylcellulose.
Step three medium-height grass pulp fibres in the present embodiment are by discarded rice straw, straw and reed according to weight ratio 4:3: 2 compositions.
Stirring to pulp uses medium consistency refining mode in step three in the present embodiment.
Mixed serum is obtained in step two in the present embodiment is also added with the glass fibre for accounting for its weight 4%.
Implementation result:
In order to verify implementation result of the invention, air filter paper prepared by three embodiments of the invention with it is common on the market Air filter paper carry out the test comparison of following index:
1. quantitative:The weight of every square metre of filter paper, unit g/m2
2. gas-flow resistance:The resistance that filter paper flows air, uses 100cm2Filter paper is resulting by 85 lift-off gas in one minute Pressure drop numerical value indicates, unit Pa;
3. air permeability:In particular area and vacuum degree, per unit time in pass through the air capacity of filter paper, unit l/ m2·s;
4. bursting strength:The maximum pressure that can bear on Filter Paper Units area, unit K pa;
5. stiffness:Filter paper deformability, unit mg;
6. tensile strength:Unit kNm;
7. water resistance:Unit s.
Following table is the index test result of each embodiment and comparative example:
Performance indicator Embodiment 1 Embodiment 2 Embodiment 3 The prior art
Quantitative g/m2 129.4 130.8 132.5 136.5
Gas-flow resistance Pa 17.4 18.2 17.1 27.1
Air permeability l/ m2·min 2634 2657 2745 2300
Bursting strength Kpa 589.8 601.2 567.9 440.3
Stiffness mg 2178 2256 2134 1943
Tensile strength kNm 3.83 3.98 3.86 3.4
Water resistance s 102 109 98 67
The filter paper that the properties of the filter paper of 1-3 of embodiment of the present invention preparation produce compared with prior art as seen from the above table has aobvious The progress of work, wherein a quantitative index at most reduces 5.2% relative to comparative example, and gas-flow resistance at most reduces 36.9%, breathes freely Degree highest improves 19.3%, and bursting strength highest improves 36.5%, and stiffness highest improves 16.1%, and tensile strength highest is promoted 17.1%, water resistance at most improves 62.6%.
Reason is analyzed, and the present invention is used by first preparing paper tire, then the maceration extract of preparation is coated with using coating method, can With the fiber that effectively prevent in filter process and other components, there is a phenomenon where movements, under differential pressure, the more difficult hair of the structure of filter core Change shape, is not susceptible to collapsing phenomenon, and is able to maintain filter paper pre-existent pore to keep good strainability, simultaneously The present invention is also creative in the preparation of maceration extract to have used polyvinyl acetate, N- octyl (methyl) acrylamide, uncle Raw material based on carboxylic acid vinyl ester and a variety of chemical substances of polyether polyol, auxiliary mixing tapioca, quaternary ammonium starch ethers, β- The mixing paste that cyclodextrine and alkyl glycosides, tricresyl phosphate are constituted, the maceration extract modest viscosity of formation can be effective The tensile strength of filter paper is improved, the synergistic effect of a variety of chemical substances effectively improves the mechanical property of paper, enhances its draftability Can, the introducing of starch improves the peel strength of maceration extract, its antioxygenic property can be improved in cycloheptaamylose, thus maceration extract It is not easy to foaming, while stability is also greatly improved, period of storage also greatly improves, the side that the maceration extract of configuration passes through coating Formula can effectively control the amount of coating, can reduce production cost and improve production efficiency, additionally it is possible to can effectively improve filter paper Physical performance index, predominantly tensile strength, bursting strength and stiffness can make to form discrete face between paper tire fiber It connects, slight crosslinking occurs between fiber, so that the mechanical strength of paper increases, moreover it is possible to realize the protrusion technology effect of barrier performance Fruit reduces paper to the wet performance of water, has reached preferable water resistance.
The present invention mixes wood pulp cellulose and straw pulp fiber with the secondary stock slurry in viscose rayon and waste paper, eliminates Original microdefect of single fiber raw material, the fiber synergistic effect that a variety of thicknesses are different, toughness is different, while using Four acicular type zinc oxide crystal whisker increased fiber interacts area and interface binding power so that filter paper have preferable mechanical strength and Endurance, while forming preliminary paper tire after squeezing by wet-laying web-forming equipment so that paper structure is stablized, between fiber between Gap rate is ideal, and air penetrability is preferable, while that adds is made of shell powder, bentonite, mica stone powder and attapulgite On the one hand mixed-powder promotes paper molding, improves the intensity of paper, on the other hand also improve the filterability of filter paper Can, mixed-powder has preferable absorption property, there can be preferable suction-operated for dust, the pollution gas in air, Furthermore there are also preferable bactericidal effects for shell powder, while the titanium dioxide added can be improved the ageing-resistant line of filter paper, addition Zinc oxide can be improved the bactericidal property of filter paper.
The plant sterilization flavouring extracting solution added in maceration extract in the preferred embodiment of the present invention simultaneously, on the one hand can allow The filter paper paper prepared has certain sterilization, on the other hand expelling parasite killing ability makes it have certain plant fragrance of a flower, effectively Improve indoor air, while vegetalitas sterilizes non-toxic to humans, safety and environmental protection, special standby suitable this kind of confined space of vehicle It uses.
The mixed rare earth chlorides of its weight 5% also are accounted in mixture addition in the preferred embodiment of the present invention, cooperate starch The phenomenon that using, the paper in later period can effectively be avoided to turn to be yellow, the chitosan of addition, which to mix, more uniform is distributed in fiber Plain surface and there are apparent retention, filtrating aid function preparing paper tire process.
The glass fibre added in mixed serum in the preferred embodiment of the present invention can effectively improve the porosity of paper tire, 4% selection is that inventor's repetition test can reach effect without making the quantitative criterion of filter paper hairiness thorn stick.
Medium consistency refining mode is used in the preferred embodiment of the present invention, so that the length of fiber, rugosity, kink and crimp index Achieve the effect that best, this is that inventor is serendipitous in repetition test during invention.
The index effect of comprehensive upper table simultaneously, the indices of embodiment 1-3 are although better than comparative example, embodiment Also difference between 1-3, it is seen that the selection of the content and preparation method parameter of component also have to final performance it is most important, therefore And the innovative content selection aspect for being also embodied in each component simultaneously of the invention, certain remaining component selection of the present invention and content Selection is obviously also non-obvious, and those skilled in the art combine the prior art that can readily occur in absolutely not.
The filter paper air permeability that the method for the environmentally protective manufacture high-quality air filter paper of one kind provided by the invention is prepared compared with Good, lower to gas-flow resistance, filter efficiency is excellent, and filter paper has the function of the plant fragrance of a flower, antimycotic antiseptic, effective mosquito expelling, Resistance to deformation, resistance to compression difference ability and the bursting strength of filter paper have preferable performance simultaneously, furthermore use a large amount of wastes, reduce Cost, protects environment, has saved resource, practical value with higher and good application prospect.
It is obvious to a person skilled in the art that invention is not limited to the details of the above exemplary embodiments, Er Qie In the case where without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter From the point of view of which point, the present embodiments are to be considered as illustrative and not restrictive, and the scope of the present invention is by appended power Benefit requires rather than above description limits, it is intended that all by what is fallen within the meaning and scope of the equivalent elements of the claims Variation is included within the present invention.
In addition, it should be understood that although this specification is described in terms of embodiments, but not each embodiment is only wrapped Containing an independent technical solution, this description of the specification is merely for the sake of clarity, and those skilled in the art should It considers the specification as a whole, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art The other embodiments being understood that.

Claims (7)

1. a kind of method of environmentally protective manufacture high-quality air filter paper, which is characterized in that include the following steps:
Step 1: by polyvinyl acetate, N- octyl (methyl) acrylamide, versatic acid vinyl esters and polyether polyol According to weight ratio 4:6:1:It is heated to 74-80 DEG C in 3 addition reactors, while with gentle nitrogen purge and with speed of agitator It is stirred 20-30% minutes under 300-400r/min, obtains reaction mixture, 55-60 DEG C of water-bath heat preservation is spare;
Step 2: waste paper, which is sent into pulper, carries out size degradation, then mashing deinking is carried out to waste paper, the paper pulp after being beaten deinking flows into Stock tank obtains secondary stock stoste, is added into secondary stock stoste and accounts for stoste weight 6%-8% viscose rayon, and is carried out with stirring rod Stirring, prevents fiber from precipitating, it is spare to obtain mixed serum;
Step 3: according to weight ratio 3:Wood pulp cellulose and straw pulp fiber are put into blender, stirring to pulp 7-9min by 1, so that planting Fibres are uniformly dispersed in water, and wherein wood pulp cellulose is by softwood pulp fiber and hardwood pulp fiber according to weight ratio 1:4 Composition, then the plant fiber for having broken slurry and step 2 are prepared into mixed serum and injected in charging basket after evenly mixing, it is fine to obtain mixing Slurry is tieed up, is stirred at low speed spare;
Step 4: by shell powder, bentonite, mica stone powder and attapulgite according to 3:2:1:2 are mixed and in pH value are Acid water washing is carried out under conditions of 5.2-5.4, then with clear water foam washing, using spray drying, then by the mixture after drying Preliminary crushing is calcined at 680-700 DEG C, then is sequentially added into mixture and accounted for the nano-titanium dioxide of its weight 1% and account for The graphene of its weight 0.5% is put into ball mill the ball milling at revolving speed 300-400r/min and obtains nanometer grade powder, to nanoscale The four acicular type zinc oxide crystal whisker for accounting for its weight 4% is added in powder, then is added into mixture and accounts for the nano oxidized of its weight 1% It is spare to be uniformly mixing to obtain mixed-powder for zinc;
Step 5: by tapioca, quaternary ammonium starch ethers, cycloheptaamylose according to weight ratio 8:1:1 is uniformly mixing to obtain mixture, Add the tricresyl phosphate of alkyl glycosides, 3% for being equivalent to its weight 5%, the deionized water of 70-80% and 20-30% Organic solvent, be stirred until homogeneous, it is to react 40min in 200W ultrasonic wave that power is placed at being 50 DEG C in temperature, is mixed Paste;
Step 6: by the mixing of the mixed serum of step 2 preparation, the composite fibre slurry of step 3 preparation and step 4 preparation Powder is according to weight ratio 4:9:2 addition stirrer for mixing are uniform, the slurry injection wet-laying equipment after uniform mixing, After being shaken up and down using stripper plate, timely quickly exclusion moisture, the fiber networking on forming net in the presence of hydraulic pressure, then will examination Sample be pressed further by removed from forming net after moisture standing and drying obtain water content be lower than 10% paper tire;
Step 7: by the reaction mixture of step 1 preparation and the mixing paste of step 5 preparation according to weight ratio 5:3 are added In blender, it is uniformly mixing to obtain dipping just liquid at being 50 DEG C in temperature, adds the plant sterilization for accounting for and impregnating just liquid weight 5% Flavouring extracting solution continues stirring 20-30 minutes, obtains maceration extract;
The plant sterilization flavouring extracts liquid and preparation method thereof:By weight by 0.1 part of deinsectization polyester, 1.5 parts of matrine, cloves 5 parts of extracting solution 5 parts of fish pelargonium extracting solution, 10 parts of ethyl alcohol, in 16 parts of feeding blenders of 6 parts of bracketplant leaching liquid and water, is in temperature 40 DEG C, speed of agitator is to stir 30 minutes under 250r/min;
Step 8: the gluten fortifier solution for being first 5% by paper tire two sides brushing quality score, uses the side of print roll coating again after drying in the shade Maceration extract is coated on the paper tire two sides of step 6 preparation by formula, then by the paper tire after coating temperature be at 90-98 DEG C it is dry, i.e., Obtain air filter paper of the invention.
2. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Mixture further includes the chitosan for accounting for its weight 10% in step 5.
3. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Mixture further includes the mixed rare earth chlorides for accounting for its weight 5% in step 5.
4. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Also added with the sodium alginate and 0.5% carboxymethyl cellulose for accounting for its weight 0.2% respectively in composite fibre slurry in step 3 Sodium.
5. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Step 3 medium-height grass pulp fibres are by discarded rice straw, straw and reed according to weight ratio 4:3:2 compositions.
6. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Stirring to pulp uses medium consistency refining mode in step 3.
7. the method for the environmentally protective manufacture high-quality air filter paper of one kind according to claim 1, which is characterized in that described Mixed serum is obtained in step 2 is also added with the glass fibre for accounting for its weight 4%.
CN201810701761.8A 2018-06-30 2018-06-30 A kind of method of environmentally protective manufacture high-quality air filter paper Withdrawn CN108842519A (en)

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CN102444048A (en) * 2011-10-22 2012-05-09 富阳市金源纸业有限公司 Writing and painting paper capable of preventing water, breakage, oxidation and moth eating
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