CN108316045A - A kind of true qualities base paper for excursion press mark production method - Google Patents
A kind of true qualities base paper for excursion press mark production method Download PDFInfo
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- CN108316045A CN108316045A CN201711457512.0A CN201711457512A CN108316045A CN 108316045 A CN108316045 A CN 108316045A CN 201711457512 A CN201711457512 A CN 201711457512A CN 108316045 A CN108316045 A CN 108316045A
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- true qualities
- slurry
- base paper
- press mark
- production method
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Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
- D21H17/29—Starch cationic
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/62—Rosin; Derivatives thereof
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
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Abstract
The object of the present invention is to provide a kind of true qualities base paper for excursion press mark production methods.A kind of true qualities base paper for excursion press mark production method, including：（1）True qualities needle slurry first carries out defibrination；（2）The bleaching broad-leaved slurry that true qualities needle slurry and accounting after the defibrination for being 10 40% by accounting are 60 90%, mixes defibrination, the degree of beating：30 60oSR, 1.5 3.5g of weight in wet base；（3）Degasser, glue, gum rosin, filler, aluminum sulfate in slurry are added in the slurry, concentration of surfing the Internet：0.3‑0.8%；（4）Paper pulp is surfed the Internet and is dried by one to three big drying cylinder after squeezing；（5）One to three road soft calendaring is carried out to page.The true qualities base paper for excursion press mark of true qualities base paper for excursion press mark production method production, machine direction tensile strength：>=1.6KN/m, whiteness：25 40%, ash content：≤5%；Positive smoothness：≥500s；Water imbibition：15‑25g/m2；Transversal stretching rate：≤2.0%；It will not lose powder, will not adsorb dyestuff makes transfer printing stable quality.
Description
Technical field
The present invention relates to field of papermaking, especially a kind of true qualities base paper for excursion press mark production method.
Background technology
Transfer printing is one of printing in textiles method；First dyestuff is imprinted on paper when stamp, it then will with hot pressing mode
Decorative pattern is transferred on fabric.When base paper for excursion press mark produces, needle is starched and bleached broad-leaved slurry mixing defibrination and forms mixing slurry, by
It is longer in the fiber of needle slurry, to make the degree of beating of mixing slurry reach setting value, the longer mixing defibrination time is needed, causes to produce
Base paper for excursion press mark exist be easy to picking influence transfer printing quality deficiency；Cotton pulp, needle slurry and bleaching broad-leaved slurry is mixed
Defibrination is closed, though picking can be reduced, exist makes transfer printing unstable quality, and cost since cotton pulp can adsorb dyestuff on a small quantity
Higher deficiency；Therefore, design one kind will not lose powder, and will not adsorb dyestuff makes the true qualities transfer printing of transfer printing stable quality
Base paper production method becomes urgent problem to be solved.
Invention content
When the purpose of the invention is to overcome current base paper for excursion press mark to produce, it is mixed that needle is starched and is bleached broad-leaved slurry
It closes defibrination and forms mixing slurry, since the fiber of needle slurry is longer, to make the degree of beating of mixing slurry reach setting value, need longer mixed
The defibrination time is closed, the base paper for excursion press mark of production is caused to there is the deficiency for being easy to picking influence transfer printing quality；By cotton pulp, needle
Leaf is starched and bleaching broad-leaved slurry mixing defibrination, though picking can be reduced, exist makes transfer print since cotton pulp can adsorb dyestuff on a small quantity
Flower unstable quality, and the higher deficiency of cost；There is provided one kind will not lose powder, and will not adsorb dyestuff makes transfer printing stable quality
True qualities base paper for excursion press mark production method.
The specific technical solution of the present invention is：
A kind of true qualities base paper for excursion press mark production method, including：（1）True qualities needle slurry first carries out defibrination；（2）It is 10- by accounting
True qualities needle slurry and accounting after 40% defibrination are starched for the bleaching broad-leaved of 60-90%, mix defibrination, the degree of beating：30-60oSR, weight in wet base
1.5-3.5g；（3）Degasser, glue, gum rosin, filler, aluminum sulfate in slurry are added in the slurry, concentration of surfing the Internet：0.3-0.8%；
（4）Paper pulp surfs the Internet to form page；（5）Page after press dewatering is dried by one to three big drying cylinder；（6）To page
Carry out one to three road soft calendaring；The true qualities base paper for excursion press mark of the true qualities base paper for excursion press mark production method：It is quantitative：25-45g/
m2；Machine direction tensile strength：>=1.6KN/m, whiteness：25-40%, ash content：≤5%；Positive smoothness：≥500s；Moisture：4-7%,
Water imbibition：15-25g/m2；Transversal stretching rate：≤2.0%.
The true qualities base paper for excursion press mark production method, slurry include that the true qualities needle that accounting is 10-40% is starched, drop
The whiteness of low true qualities base paper for excursion press mark levels off to needle slurry true qualities, is conducive to the true qualities that transfer printing keeps dyestuff；First to fibre
It ties up after longer true qualities needle slurry first carries out defibrination, the true qualities needle slurry that accounting is 10-40% and the bleaching that accounting is 60-90% are wealthy
Leaf is starched, and defibrination is mixed, and is shortened the defibrination time of the shorter bleaching broad-leaved slurry of fiber, is not fallen conducive to true qualities base paper for excursion press mark
Powder；Addition gum rosin, which can improve, in the slurry prevents picking performance；It is dried by one to three big drying cylinder, improves paper
The positive smoothness of page；One to three road soft calendaring is carried out to page, improves the tightness of page, improve the smoothness of page reverse side and
Further increase the positive smoothness of page；Mixing defibrination can reduce energy consumption；The true qualities base paper for excursion press mark production method produces
True qualities base paper for excursion press mark, machine direction tensile strength：>=1.6KN/m, whiteness：25-40%, ash content：≤5%；Positive smoothness：≥
500s；Water imbibition：15-25g/m2；Transversal stretching rate：≤2.0%；It will not lose powder, will not adsorb dyestuff keeps transfer printing quality steady
It is fixed.
Preferably, the degasser ton paper dosage is 0.5-1.5kg；Glue selects cationic starch, ton paper to use in slurry
Amount is in 5-10kg；Gum rosin selects anion gum rosin, and ton paper dosage is in 20-30kg；Filler selects talcum powder, ton paper dosage to exist
50-100kg；Aluminum sulfate ton paper dosage is in 5-10kg.True qualities base paper for excursion press mark is set not lose powder, will not adsorb dyestuff makes transfer
Printing quality is stablized, and effect is preferable.
Preferably, there are two the big drying cylinders, 4-5m of the first big drying cylinder diameter, temperature：It is 140-160 DEG C, second largest
3-4m of drying cylinder diameter, temperature：120-140℃.Drying efficiency height and good drying effect；The diameter of the second largest drying cylinder is less than first
Big drying cylinder diameter, the temperature of the second largest drying cylinder are less than the first big dryer temperature, are conducive to gentle dry, improve the intensity, tight of page
Degree, page front smoothness.
Preferably, the soft calendaring is carried out by soft roll and steel rider cooperation, the line pressure of soft roll：60-
100KN/m；Soft calendaring steel rider uses heat-conducting oil heating, soft calendaring steel rider roll surface temperature：100-200℃.The line pressure of soft roll
Power：60-100KN/m, soft calendaring steel rider use heat-conducting oil heating, soft calendaring steel rider roll surface temperature：100-200 DEG C, it is conducive to improve
Tightness and paper smoothness.
Compared with prior art, the beneficial effects of the invention are as follows：The true qualities base paper for excursion press mark production method, slurry
Include accounting be 10-40% true qualities needle starch, reduce true qualities base paper for excursion press mark whiteness level off to needle slurry true qualities,
The true qualities of dyestuff are kept conducive to transfer printing；After first first carrying out defibrination to fiber longer true qualities needle slurry, accounting 10-40%
True qualities needle slurry and accounting be 60-90% bleaching broad-leaved starch, mix defibrination, shorten fiber it is shorter bleaching broad-leaved slurry
The defibrination time does not lose powder conducive to true qualities base paper for excursion press mark；Addition gum rosin, which can improve, in the slurry prevents picking performance；Pass through
One to three big drying cylinder is dried, and improves the positive smoothness of page；One to three road soft calendaring is carried out to page, is improved
The tightness of page improves the smoothness of page reverse side and further increases the positive smoothness of page；Mixing defibrination can reduce energy
Consumption；The true qualities base paper for excursion press mark of true qualities base paper for excursion press mark production method production, machine direction tensile strength：>=1.6KN/m, in vain
Degree：25-40%, ash content：≤5%；Positive smoothness：≥500s；Water imbibition：15-25g/m2；Transversal stretching rate：≤2.0%；It will not
Picking, will not adsorb dyestuff makes transfer printing stable quality.Degasser ton paper dosage is 0.5-1.5kg；Slurry in glue select sun from
Sub- starch, ton paper dosage is in 5-10kg；Gum rosin selects anion gum rosin, and ton paper dosage is in 20-30kg；Filler selects talcum
Powder, ton paper dosage is in 50-100kg；Aluminum sulfate ton paper dosage is in 5-10kg；True qualities base paper for excursion press mark is set not lose powder, it will not
Absorption dyestuff keeps transfer printing stable quality, effect preferable.Drying efficiency height and good drying effect；The diameter of the second largest drying cylinder is small
It is less than the first big dryer temperature in the temperature of the first big drying cylinder diameter, the second largest drying cylinder, is conducive to gentle drying, improves the strong of page
Degree, tightness, page front smoothness.The line pressure of soft roll：60-100KN/m, soft roll uses heat-conducting oil heating, soft
Felt wrapped roll roll surface temperature：100-200 DEG C, it is conducive to improve tightness and paper smoothness.
Specific implementation mode
A kind of true qualities base paper for excursion press mark production method, including：（1）True qualities needle slurry first carries out defibrination；（2）It is by accounting
The bleaching broad-leaved that 30% true qualities needle slurry and accounting is 70% is starched, and defibrination, the degree of beating are mixed：45oSR, weight in wet base 2.5g；（3）In slurry
Glue, gum rosin, filler, aluminum sulfate in middle addition degasser, slurry, concentration of surfing the Internet：0.6%；（4）Paper pulp surfs the Internet to form page；（5）
Page after press dewatering is dried by one to three big drying cylinder；（6）One to three road soft calendaring is carried out to page；This
The true qualities base paper for excursion press mark of color base paper for excursion press mark production method：It is quantitative：25-45g/m2；Machine direction tensile strength：≥1.6KN/
M, whiteness：25-40%, ash content：≤5%；Positive smoothness：≥500s；Moisture：4-7%, water imbibition：15-25g/m2；Transversal stretching
Rate：≤2.0%.
The degasser ton paper dosage is 1kg；Glue selects cationic starch in slurry, and ton paper dosage is in 7kg；Gum rosin selects
With anion gum rosin, ton paper dosage is in 25kg；Filler selects talcum powder, and ton paper dosage is in 70kg；Aluminum sulfate ton paper dosage exists
6kg。
In the present embodiment, there are two the big drying cylinders, 4 .5m of the first big drying cylinder diameter, temperature：150 DEG C, the second largest baking
Cylinder diameter 3.5m, temperature：130℃.
The soft calendaring is coordinated by soft roll and bachelor to carry out, the line pressure of soft roll：80KN/m；Soft calendaring
Roller uses heat-conducting oil heating, soft roll roll surface temperature：150℃.
The beneficial effects of the invention are as follows：The true qualities base paper for excursion press mark production method, slurry include that accounting is 10-
40% true qualities needle slurry, reduce true qualities base paper for excursion press mark whiteness level off to needle slurry true qualities, be conducive to transfer printing keep
The true qualities of dyestuff；After first first carrying out defibrination to fiber longer true qualities needle slurry, true qualities needle slurry and account for that accounting is 10-40%
Than the bleaching broad-leaved slurry for 60-90%, defibrination is mixed, the defibrination time of the shorter bleaching broad-leaved slurry of fiber is shortened, is conducive to true qualities
Base paper for excursion press mark does not lose powder；Addition gum rosin, which can improve, in the slurry prevents picking performance；Pass through one to three big drying cylinder
It is dried, improves the positive smoothness of page；One to three road soft calendaring is carried out to page, improves the tightness of page, is improved
The smoothness of page reverse side and further increase the positive smoothness of page；Mixing defibrination can reduce energy consumption；True qualities transfer print
The true qualities base paper for excursion press mark of flower base paper production method production, machine direction tensile strength：>=1.6KN/m, whiteness：25-40%, ash content：
≤5%；Positive smoothness：≥500s；Water imbibition：15-25g/m2；Transversal stretching rate：≤2.0%；It will not lose powder, dye will not be adsorbed
Material makes transfer printing stable quality.Degasser ton paper dosage is 1kg；Glue selects cationic starch in slurry, and ton paper dosage is in 7kg；
Gum rosin selects anion gum rosin, and ton paper dosage is in 25kg；Filler selects talcum powder, and ton paper dosage is in 70kg；Aluminum sulfate ton
Paper dosage is in 6kg；So that true qualities base paper for excursion press mark is not lost powder, will not adsorb dyestuff makes transfer printing stable quality, effect compared with
It is good.Drying efficiency height and good drying effect；The diameter of the second largest drying cylinder is less than the first big drying cylinder diameter, the temperature of the second largest drying cylinder
Less than the first big dryer temperature, it is conducive to gentle drying, improves the intensity, tightness, page front smoothness of page.Soft roll
Line pressure：80KN/m, soft calendaring steel rider use heat-conducting oil heating, soft calendaring steel rider roll surface temperature：150 DEG C, it is conducive to improve tightness
And paper smoothness.
The present invention can be changed apparent to one skilled in the art for various ways, and such change is not considered as
It departs from the scope of the present invention.The technical staff in the field is obviously changed as all, is included within this right
Within the scope of it is required that.
Claims (4)
1. a kind of true qualities base paper for excursion press mark production method, characterized in that including：（1）True qualities needle slurry first carries out defibrination；（2）
The bleaching broad-leaved slurry that true qualities needle slurry and accounting after the defibrination for being 10-40% by accounting are 60-90%, mixes defibrination, the degree of beating：
30-60oSR, weight in wet base 1.5-3.5g；（3）Degasser, glue, gum rosin, filler, aluminum sulfate in slurry are added in the slurry, and online is dense
Degree：0.3-0.8%；（4）Paper pulp surfs the Internet to form page；（5）Page after press dewatering is done by one to three big drying cylinder
It is dry；（6）One to three road soft calendaring is carried out to page；The true qualities base paper for excursion press mark of the true qualities base paper for excursion press mark production method：
It is quantitative：25-45g/m2；Machine direction tensile strength：>=1.6KN/m, whiteness：25-40%, ash content：≤5%；Positive smoothness：≥
500s；Moisture：4-7%, water imbibition：15-25g/m2；Transversal stretching rate：≤2.0%.
2. true qualities base paper for excursion press mark production method according to claim 1, it is characterized in that：The degasser ton paper is used
Amount is 0.5-1.5kg；Glue selects cationic starch in slurry, and ton paper dosage is in 5-10kg；Gum rosin selects anion gum rosin, ton
Paper dosage is in 20-30kg；Filler selects talcum powder, and ton paper dosage is in 50-100kg；Aluminum sulfate ton paper dosage is in 5-10kg.
3. true qualities base paper for excursion press mark production method according to claim 1, it is characterized in that：The big drying cylinder has two
It is a, 4-5m of the first big drying cylinder diameter, temperature：140-160 DEG C, 3-4m of the second largest drying cylinder diameter, temperature：120-140℃.
4. true qualities base paper for excursion press mark production method according to claim 1, it is characterized in that：The soft calendaring passes through soft
Felt wrapped roll and steel rider cooperation carry out, the line pressure of soft roll：60-100KN/m；Soft calendaring steel rider uses heat-conducting oil heating, soft
Press polish steel rider roll surface temperature：100-200℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711457512.0A CN108316045B (en) | 2017-12-28 | 2017-12-28 | Natural color transfer printing base paper production method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711457512.0A CN108316045B (en) | 2017-12-28 | 2017-12-28 | Natural color transfer printing base paper production method |
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| Publication Number | Publication Date |
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| CN108316045A true CN108316045A (en) | 2018-07-24 |
| CN108316045B CN108316045B (en) | 2020-02-28 |
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| CN201711457512.0A Active CN108316045B (en) | 2017-12-28 | 2017-12-28 | Natural color transfer printing base paper production method |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110318298A (en) * | 2019-06-26 | 2019-10-11 | 深圳市铭诚生活科技有限公司 | A kind of multilayer paper for kitchen containing compound glue application solution |
| CN110644286A (en) * | 2019-09-19 | 2020-01-03 | 山东华泰纸业股份有限公司 | High-heat-conduction anti-static thermal sublimation transfer printing paper |
| CN111593608A (en) * | 2020-04-13 | 2020-08-28 | 仙鹤股份有限公司 | Preparation method of natural-color furniture protection paper |
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| CN111593608A (en) * | 2020-04-13 | 2020-08-28 | 仙鹤股份有限公司 | Preparation method of natural-color furniture protection paper |
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| CN108316045B (en) | 2020-02-28 |
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