CN109056420A - A kind of preparation method of Deinking Pulp fruit paper bag - Google Patents

A kind of preparation method of Deinking Pulp fruit paper bag Download PDF

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Publication number
CN109056420A
CN109056420A CN201810763105.0A CN201810763105A CN109056420A CN 109056420 A CN109056420 A CN 109056420A CN 201810763105 A CN201810763105 A CN 201810763105A CN 109056420 A CN109056420 A CN 109056420A
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CN
China
Prior art keywords
slurry
deinking
slurries
pulper
needle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
CN201810763105.0A
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Chinese (zh)
Inventor
华克烈
甘木林
何县香
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINJIANG YOULANFA PAPER INDUSTRY Co Ltd
Original Assignee
JINJIANG YOULANFA PAPER INDUSTRY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JINJIANG YOULANFA PAPER INDUSTRY Co Ltd filed Critical JINJIANG YOULANFA PAPER INDUSTRY Co Ltd
Priority to CN201810763105.0A priority Critical patent/CN109056420A/en
Publication of CN109056420A publication Critical patent/CN109056420A/en
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • D21H27/10Packing paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21BFIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00Fibrous raw materials or their mechanical treatment
    • D21B1/04Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30Defibrating by other means
    • D21B1/34Kneading or mixing; Pulpers
    • D21B1/345Pulpers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/02Methods of beating; Beaters of the Hollander type
    • 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
    • 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
    • D21H21/06Paper forming aids
    • D21H21/12Defoamers
    • 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
    • D21H21/20Wet strength 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

Abstract

The present invention relates to pulp technology for making paper, provide a kind of preparation method of Deinking Pulp fruit paper bag, solve the problems, such as prior art high production cost, the following steps are included: pulping process, slurrying process, desanding, pulp flow and online process, paper making control process, paper postprocessing working procedures.

Description

A kind of preparation method of Deinking Pulp fruit paper bag
Technical field
The present invention relates to pulp technology for making paper more particularly to a kind of preparation methods of Deinking Pulp fruit paper bag.
Background technique
Fruit paper bag is a kind of top grade paper for being exclusively used in fruit internal liner package, and quality characteristic is mainly physics dry strength With wet strength height, transparency is good, fine and smooth Micron Technology, shows the aesthetics and comfort of fruit.But domestic manufacturer is produced at present Fruit paper bag is produced using the long fine slurry of 100% needlebush, through high concentration mashing.The fruit paper bag of the method production, production of units With wood pulp amount is big, electricity consumption is high, manufacturing cost is high, and client is difficult to receive such higher-priced fruit paper bag.Do not have at present yet It was found that, for this purpose, being suitble to meet customer need for production, expanding market with the document of Deinking Pulp production such use fruit paper bag and occupying Rate promotes product competitiveness, makes full use of and play the advantage that our company has production regeneration Deinking Pulp, and our company tissue researches and develops people Member mixes regeneration Deinking Pulp production fruit paper bag in fruit paper bag production, and improves prior art technology and wet end furnish, to reach To the production cost for reducing fruit paper bag.
Summary of the invention
Therefore, for the above content, the present invention provides a kind of preparation method of Deinking Pulp fruit paper bag, solves the prior art The problem of high production cost.
A kind of preparation method of Deinking Pulp fruit paper bag, the following steps are included:
A, pulping process
By Deinking Pulp size degradation, the revolving speed of pulper is 300-400r/min, beating time 30-60min, in pulper The mass concentration of Deinking Pulp is maintained at 3-5%, and the slurry in pulper is removed impurity by aperture 3mm sieve, then uses disk Grinding machine is beaten, and beating degree control adjusts pH to 7 in 75-85 ° of SR, obtains storing after deinking slurries spare;By needle starch into Row size degradation, the revolving speed of pulper are 500-600r/min, beating time 30-60min, and the quality of the needle slurry in pulper is dense Degree is maintained at 3-5%, and the slurry in pulper is removed impurity by aperture 3mm sieve, is then beaten, is beaten with disc mill Degree of beating control adjusts pH to 7 in 75-85 ° of SR, obtains storing after needle slurries spare;
B, slurrying process
Deinking slurries and needle slurries difference weight percent 40-80%, 20-60% mixing for taking step A to obtain, to Cation guar gum is added in the mixed slurry, dosage is the 0.08-0.15% of oven dry stock weight, is uniformly mixed, is added and increases White dose;
C, desanding
Above-mentioned mixing slurry is successively copied to forebay, header box, intermediate pool, removes sand pump and desander desanding;In the high position The PAE wet strength agent (calculating by 100% content) of oven dry stock weight 3-4% is added in the case stage;
D, pulp flow and online process
The obtained slurry of step C is streamed, during the streaming, the concentration of slurry is diluted to mass fraction It is 0.5~0.9%, while removes the weight impurity of the slurry;Be added account for oven dry stock weight 0.5-1% cationic starch, Preservative and pigment is added in the paraffin wax emulsions of the emulsion acrylic resin of 20-30%, 10-15%, defoaming agent 0.01-0.15%, Then online process is completed;
E, paper making controls process
Slurry in step D is sent into after machine chest and is diluted by plain boiled water, flow box dehydration, drying, top sizing, finally It is formed by soft calendaring ornamenting;The top sizing agents useful for same is grouped as by each group of following parts by weight: phosphate ester starch 80- 90 parts, 10-20 parts of sodium carboxymethylcellulose, 0.5-1 parts of defoaming agent, 0.1-0.3 parts of preservative;
F, paper postprocessing working procedures
Sheet paper or roll web, finished product are processed into the paper bowl cutting that step E is obtained.
A further improvement is that: the acrylic emulsion solid content 35%.
A further improvement is that: the paraffin wax emulsions solid content 30%.
A further improvement is that: the proportion of the deinking slurries and needle slurries is 5:5.
A further improvement is that: the dosage of the PEA wet strength agent is the 3.5% of oven dry stock.
By using preceding solution, the beneficial effects of the present invention are:
1. the present invention is reduced the long fine slurry dosage of needle, is increased regeneration Deinking Pulp dosage, save and use by optimization wet end furnish Electricity.
2. adding retention agent cation guar gum in the slurry, the loss of fiber fines is reduced, reduces unit usage of sizing agent.
3. fruit paper bag wet strength and tearability are effectively improved, with propylene within the scope of experimentally determined PAE wet strengthening agent Acid resin replaces filler kaolin in the prior art etc., and finished product transparency is high, paraffin wax emulsions is added, finished product is fine and smooth, moisture retention Good, whole finished product physics dry strength and wet strength are high, and transparency is good, fine and smooth Micron Technology, can show the aesthetics of fruit and comfortable Sense.
Specific embodiment
Carry out the embodiment that the present invention will be described in detail below with reference to specific embodiment, how skill is applied to the present invention whereby Art means solve technical problem, and the realization process for reaching technical effect can fully understand and implement.
Unless otherwise specified, the conventional hand that technological means employed in embodiment is well known to those skilled in the art Section, used reagent and product are also available commercial.The source of agents useful for same, trade name and it is necessary to list it Constituent person is indicated on the first occurrence.
Embodiment one
A, pulping process
By Deinking Pulp size degradation, the revolving speed of pulper is 300r/min, beating time 30min, the Deinking Pulp in pulper Mass concentration be maintained at 3%, by the slurry in pulper by aperture 3mm sieve remove impurity, then carried out with disc mill Mashing, beating degree control adjust pH to 7 in 75 ° of SR, obtain storing after deinking slurries spare;Needle is starched and carries out size degradation, pulping The revolving speed of machine is 500r/min, beating time 30min, and the mass concentration of the needle slurry in pulper is maintained at 3%, by pulping Slurry in machine removes impurity by aperture 3mm sieve, is then beaten with disc mill, and beating degree control is adjusted in 75SR PH to 7 obtains storing after needle slurries spare;
B, slurrying process
Deinking slurries and needle slurries the difference weight percent 40%, 60% for taking step A to obtain mix, and mix to described It closes and cation guar gum is added in slurry, dosage is the 0.08% of oven dry stock weight, is uniformly mixed, and fluorescent brightener CBS is added (stilbene biphenyl sodium disulfonate), dosage are the 0.01% of oven dry stock weight;
C, desanding: above-mentioned mixing slurry is successively copied to forebay, header box, intermediate pool, removes sand pump and desander desanding;In institute State the PAE wet strength agent (calculating by 100% content) of header box stage addition oven dry stock weight 3%;
D, pulp flow and online process
The obtained slurry of step C is streamed, during the streaming, the concentration of slurry is diluted to mass fraction It is 0.5%, while removes the weight impurity of the slurry;It is added the third of the cationic starch, 20% that account for oven dry stock weight 0.5% Olefin(e) acid resin emulsion, 10% paraffin wax emulsions, defoaming agent 0.01% is added preservative and pigment, then completes online process;
E, paper making controls process
Slurry in step D is sent into after machine chest and is diluted by plain boiled water, flow box dehydration, drying, top sizing, finally It is formed by soft calendaring ornamenting;The top sizing agents useful for same is grouped as by each group of following parts by weight: phosphate ester starch 80 Part, 20 parts of sodium carboxymethylcellulose, 0.5 part of defoaming agent, 0.1 part of preservative;
F, paper postprocessing working procedures
Sheet paper or roll web, finished product are processed into the paper bowl cutting that step E is obtained.
Embodiment two
A, pulping process
By Deinking Pulp size degradation, the revolving speed of pulper is 350r/min, beating time 40min, the Deinking Pulp in pulper Mass concentration be maintained at 4%, by the slurry in pulper by aperture 3mm sieve remove impurity, then carried out with disc mill Mashing, beating degree control adjust pH to 7 in 80 ° of SR, obtain storing after deinking slurries spare;Needle is starched and carries out size degradation, pulping The revolving speed of machine is 550r/min, beating time 50min, and the mass concentration of the needle slurry in pulper is maintained at 4%, by pulping Slurry in machine removes impurity by aperture 3mm sieve, is then beaten with disc mill, and beating degree control is adjusted in 80 ° of SR PH to 7 obtains storing after needle slurries spare;
B, slurrying process
Deinking slurries and needle slurries the difference weight percent 50%, 50% for taking step A to obtain mix, and mix to described It closes and cation guar gum is added in slurry, dosage is the 0.1% of oven dry stock weight, is uniformly mixed, and fluorescent brightener CBS is added (stilbene biphenyl sodium disulfonate), dosage are the 0.02% of oven dry stock weight;
C, desanding: above-mentioned mixing slurry is successively copied to forebay, header box, intermediate pool, removes sand pump and desander desanding;In institute State the PAE wet strength agent (calculating by 100% content) of header box stage addition oven dry stock weight 3.5%;
D, pulp flow and online process
The obtained slurry of step C is streamed, during the streaming, the concentration of slurry is diluted to mass fraction It is 0.7%, while removes the weight impurity of the slurry;It is added the third of the cationic starch, 25% that account for oven dry stock weight 0.7% Olefin(e) acid resin emulsion, 12% paraffin wax emulsions, defoaming agent 0.1% is added preservative and pigment, then completes online process;Institute State acrylic emulsion solid content 35%, the paraffin wax emulsions solid content 30%.
E, paper making controls process
Slurry in step D is sent into after machine chest and is diluted by plain boiled water, flow box dehydration, drying, top sizing, finally It is formed by soft calendaring ornamenting;The top sizing agents useful for same is grouped as by each group of following parts by weight: phosphate ester starch 85 Part, 15 parts of sodium carboxymethylcellulose, 0.7 part of defoaming agent, 0.2 part of preservative;
F, paper postprocessing working procedures
Sheet paper or roll web, finished product are processed into the paper bowl cutting that step E is obtained.
Embodiment three
A, pulping process
By Deinking Pulp size degradation, the revolving speed of pulper is 400r/min, beating time 60min, the Deinking Pulp in pulper Mass concentration be maintained at 5%, by the slurry in pulper by aperture 3mm sieve remove impurity, then carried out with disc mill Mashing, beating degree control adjust pH to 7 in 85 ° of SR, obtain storing after deinking slurries spare;Needle is starched and carries out size degradation, pulping The revolving speed of machine is 600r/min, beating time 60min, and the mass concentration of the needle slurry in pulper is maintained at 5%, by pulping Slurry in machine removes impurity by aperture 3mm sieve, is then beaten with disc mill, and beating degree control is adjusted in 85 ° of SR PH to 7 obtains storing after needle slurries spare;
B, slurrying process
Deinking slurries and needle slurries the difference weight percent 80%, 20% for taking step A to obtain mix, and mix to described It closes and cation guar gum is added in slurry, dosage is the 0.15% of oven dry stock weight, is uniformly mixed, and fluorescent brightener CBS is added (stilbene biphenyl sodium disulfonate), dosage are the 0.03% of oven dry stock weight;
C, desanding: above-mentioned mixing slurry is successively copied to forebay, header box, intermediate pool, removes sand pump and desander desanding;In institute State the PAE wet strength agent (calculating by 100% content) of header box stage addition oven dry stock weight 4%;PAE, i.e. daiamid epoxy chlorine Propane resin, is water solubility, cationic, thermosetting resin, have efficiently, be suitable for Neutral Papermaking, to broken or waste paper time The features such as receipts are easier to, are nontoxic.
D, pulp flow and online process
The obtained slurry of step C is streamed, during the streaming, the concentration of slurry is diluted to mass fraction It is 0.9%, while removes the weight impurity of the slurry;It is added the third of the cationic starch, 25% that account for oven dry stock weight 0.7% Olefin(e) acid resin emulsion, 12% paraffin wax emulsions, defoaming agent 1% is added preservative and pigment, then completes online process;It is described Acrylic emulsion solid content 35%, the paraffin wax emulsions solid content 30%.
E, paper making controls process
Slurry in step D is sent into after machine chest and is diluted by plain boiled water, flow box dehydration, drying, top sizing, finally It is formed by soft calendaring ornamenting;The top sizing agents useful for same is grouped as by each group of following parts by weight: phosphate ester starch 90 Part, 10 parts of sodium carboxymethylcellulose, 1 part of defoaming agent, 0.3 part of preservative;
F, paper postprocessing working procedures
Sheet paper or roll web, finished product are processed into the paper bowl cutting that step E is obtained.
In above-described embodiment, the preservative uses the lf-231 preservative of Foshan City Lan Feng auxiliary agent Co., Ltd production.
The foregoing descriptions are merely the embodiment using this origination techniques content, any those skilled in the art use this wound Make done modifications and changes, all belong to the scope of the patents of this creation opinion, and is not limited to those disclosed embodiments.

Claims (5)

1. a kind of preparation method of Deinking Pulp fruit paper bag, it is characterised in that: the following steps are included:
A, pulping process: by Deinking Pulp size degradation, the revolving speed of pulper is 300-400r/min, beating time 30-60min, broken The mass concentration of Deinking Pulp in pulp grinder is maintained at 3-5%, and the slurry in pulper is removed impurity by aperture 3mm sieve, Then it is beaten with disc mill, beating degree control adjusts pH to 7 in 75-85 ° of SR, obtains storing after deinking slurries spare;It will Needle slurry carries out size degradation, and the revolving speed of pulper is 500-600r/min, beating time 30-60min, the needle slurry in pulper Mass concentration be maintained at 3-5%, by the slurry in pulper by aperture 3mm sieve remove impurity, then with disc mill into Row mashing, beating degree control adjust pH to 7 in 75-85 ° of SR, obtain storing after needle slurries spare;
B, slurrying process: deinking slurries and needle slurries difference weight percent 40-80%, the 20-60% for taking step A to obtain Cation guar gum is added into the mixed slurry for mixing, and dosage is the 0.08-0.15% of oven dry stock weight, is uniformly mixed, Brightening agent is added;
C, desanding: above-mentioned mixing slurry is successively copied to forebay, header box, intermediate pool, removes sand pump and desander desanding;In the height The PAE wet strength agent of oven dry stock weight 3-4% is added in the position case stage, and the PAE wet strength agent is calculated by 100% content;
D, pulp flow and online process: the obtained slurry of step C is streamed, during the streaming, slurry it is dense It is 0.5~0.9% that degree, which is diluted to mass fraction, while removing the weight impurity of the slurry;Addition accounts for oven dry stock weight The cationic starch of 0.5-1%, the emulsion acrylic resin of 20-30%, 10-15% paraffin wax emulsions, defoaming agent 0.01- 0.15%, preservative and pigment is added, then completes online process;
E, paper making controls process: the slurry in step D being sent into after machine chest and is diluted by plain boiled water, flow box dehydration is dried Dry, top sizing is finally formed by soft calendaring ornamenting;The top sizing agents useful for same is grouped by each group of following parts by weight At: 80-90 parts of phosphate ester starch, 10-20 parts of sodium carboxymethylcellulose, 0.5-1 parts of defoaming agent, 0.1-0.3 parts of preservative;
F, sheet paper or roll web, finished product paper postprocessing working procedures: are processed into the paper bowl cutting that step E is obtained.
2. a kind of preparation method of Deinking Pulp fruit paper bag according to claim 1, it is characterised in that: the acrylic emulsion Solid content 35%.
3. a kind of preparation method of Deinking Pulp fruit paper bag according to claim 1, it is characterised in that: the paraffin wax emulsions are solid Content 30%.
4. a kind of preparation method of Deinking Pulp fruit paper bag according to claim 1, it is characterised in that: the deinking slurries and The proportion of needle slurries is 5:5.
5. a kind of preparation method of Deinking Pulp fruit paper bag according to claim 1, it is characterised in that: the PEA wet strength agent Dosage be oven dry stock 3.5%.
CN201810763105.0A 2018-07-12 2018-07-12 A kind of preparation method of Deinking Pulp fruit paper bag Withdrawn CN109056420A (en)

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Application Number Priority Date Filing Date Title
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109468886A (en) * 2018-12-27 2019-03-15 东莞市江高包装材料有限公司 A kind of production technology of wrapping paper
CN113832775A (en) * 2021-07-23 2021-12-24 广州造纸股份有限公司 Environment-friendly orange bubble bag envelope paper and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101748643A (en) * 2008-12-02 2010-06-23 福建省晋江优兰发纸业有限公司 Production process of ultra-low quantitative tissue paper
CN101806016A (en) * 2010-03-22 2010-08-18 浙江科技学院 Fruit fresh-keeping paperboard and preparation method thereof
CN102517988A (en) * 2011-10-20 2012-06-27 陕西科技大学 Method for producing fruit breeding bag paper with high water resistance
CN104313947A (en) * 2014-10-22 2015-01-28 浙江华川实业集团有限公司 Preparation method of breathable and waterproof fruit cultivating bag paper
CN106120459A (en) * 2016-06-29 2016-11-16 福建希源纸业有限公司 A kind of preparation method of ultra-low quantitative hydrophobicity tissue paper

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101748643A (en) * 2008-12-02 2010-06-23 福建省晋江优兰发纸业有限公司 Production process of ultra-low quantitative tissue paper
CN101806016A (en) * 2010-03-22 2010-08-18 浙江科技学院 Fruit fresh-keeping paperboard and preparation method thereof
CN102517988A (en) * 2011-10-20 2012-06-27 陕西科技大学 Method for producing fruit breeding bag paper with high water resistance
CN104313947A (en) * 2014-10-22 2015-01-28 浙江华川实业集团有限公司 Preparation method of breathable and waterproof fruit cultivating bag paper
CN106120459A (en) * 2016-06-29 2016-11-16 福建希源纸业有限公司 A kind of preparation method of ultra-low quantitative hydrophobicity tissue paper

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109468886A (en) * 2018-12-27 2019-03-15 东莞市江高包装材料有限公司 A kind of production technology of wrapping paper
CN113832775A (en) * 2021-07-23 2021-12-24 广州造纸股份有限公司 Environment-friendly orange bubble bag envelope paper and preparation method thereof

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Application publication date: 20181221