CN107059463A - A kind of production technology of uncoated heat sublimation transfer printing paper - Google Patents
A kind of production technology of uncoated heat sublimation transfer printing paper Download PDFInfo
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- CN107059463A CN107059463A CN201710310394.4A CN201710310394A CN107059463A CN 107059463 A CN107059463 A CN 107059463A CN 201710310394 A CN201710310394 A CN 201710310394A CN 107059463 A CN107059463 A CN 107059463A
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21D—TREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
- D21D1/00—Methods of beating or refining; Beaters of the Hollander type
- D21D1/02—Methods of beating; Beaters of the Hollander type
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F3/00—Press section of machines for making continuous webs of paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
- D21F5/00—Dryer section of machines for making continuous webs of paper
- D21F5/02—Drying on cylinders
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21G—CALENDERS; ACCESSORIES FOR PAPER-MAKING MACHINES
- D21G1/00—Calenders; Smoothing apparatus
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/06—Paper forming aids
- D21H21/10—Retention agents or drainage improvers
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/16—Sizing or water-repelling agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Paper (AREA)
Abstract
The present invention relates to field of papermaking, particularly a kind of production technology of uncoated heat sublimation transfer printing paper, the technique is adjusted to slurry feedstock, dissolving pulp has been used first, and change traditional handicraft by sizing material by surface coating be transferred to slurry in add, realize same printing effect and transfer effect by the effect of the higher dissolving pulp of content of cellulose.By coordinating auxiliary material mix and then being manufactured paper with pulp into uncoated transfer printing paper the slurry in a variety of sources, the grammes per square metre of paper is substantially reduced using this technique, in the market is met to low grammes per square metre, efficient requirement, coating production technology is reduced, greatly reduces production cost.This production technology can make finished product using conventional paper machine, it is not necessary to which sizing applicator is glued, it is not required that coating machine is coated with paper surface, and equipment is simple, and production efficiency is high.
Description
Technical field
The present invention relates to field of papermaking, it is related to a kind of production technology of uncoated heat sublimation transfer printing paper.
Background technology
Thermal dye sublimation transfer printing is that the picture and text such as portrait, landscape, word are used into the ink-jet printer equipped with thermal dye sublimation transfer printing ink
It is printed upon with mirror image posture on thermal dye sublimation transfer printing paper, then 200 DEG C or so is heated to by thermal transfer equipment, is made on heat sublimation paper
Thermal transfer ink distillation penetrates into stock, and the quality of wherein thermal dye sublimation transfer printing paper directly influences the result of said process.
The consumption of current thermal sublimation digit transfer printing paper is continuously increased, and digital printing speed is also increasingly faster, logarithmic code
In the case that the requirement of paper is developed from original high grammes per square metre to low grammes per square metre, but paper grammes per square metre is low, easily break paper in coating process；It is another
The transfer printing paper of aspect, originally coating is stronger due to the moisture pick-up properties of coating, and causing will to the humidity of use environment
Ask comparison high, the easy adhesion of high humidity, therefore how to solve the above problems as one of this area urgent problem to be solved.
The content of the invention
There is provided a kind of life of uncoated heat sublimation transfer printing paper for problems of the invention for prior art presence
Production. art, the technique is adjusted to slurry feedstock, coordinates auxiliary material mix and then copied in the slurry in a variety of sources
Make, the grammes per square metre of paper is substantially reduced using this technique, meet in the market to low grammes per square metre, efficient requirement, reduce coating
Production technology, greatly reduces production cost.This production technology can make finished product using conventional paper machine, it is not necessary to apply
Glue machine is glued, it is not required that coating machine is coated with paper surface, and equipment is simple, and production efficiency is high.
Technical scheme is as follows：
A kind of production technology of uncoated heat sublimation transfer printing paper：Its slurry feedstock composition is calculated as by weight：Dissolving
40-60 parts of wood pulp, 20-30 parts of broad-leaved chemical pulp, 20-30 parts of needle chemical pulp；
Concretely comprise the following steps：
Above-mentioned slurry feedstock is beaten respectively in proportion, wherein needle or broad-leaved dissolving pulp is beaten to 28-32 °
SR, broad-leaved chemical pulp are beaten to 33-35 ° of SR, needle chemical pulp and are beaten to 30-33 ° of SR, then press the slurry after above-mentioned mashing
Parts by weight are delivered to slurry pond and mixed in proportion, while adding the filler that parts by weight are 5-15 parts；
Backward slurry pond in add turning property of filler reinforcing agent and sizing agent and sodium carboxymethylcellulose or sodium alginate
In one kind or mixture, and be well mixed；
By it is above-mentioned be sufficiently mixed uniform slurry and be pumped into destroy forebay, add retention agent, filter aid, then entered by head box
Enter that wet end dehydration, press section are further dehydrated, cylinder dried, calender press polish obtain finished product.
Above-mentioned dissolving pulp is the abbreviation of " dissolving grade chemical wood pulp ", described dissolving pulp for needle dissolving pulp or
Broad-leaved dissolving pulp, content of cellulose more than 90%, cellulosic degree of polymerization is highly homogeneous, and this is one of inventive point of the present invention；
The wood pulp is that in the market is directly bought with broad-leaved chemical pulp and needle chemical pulp；
The calico paper prepared using above-mentioned technique, quantitative 38-65g/m2, longitudinal wet tensile index be more than or equal to 7N.m/g,
Surface absorption weight 20-40g/m2, transversal stretching rate 1-3%, smoothness 20-70s, indices are same more than prior art
Class paper.
Substitution value >=0.6 of wherein described sodium carboxymethylcellulose, sodium alginate uses the sodium alginate of medium-high viscosity,
Viscosity of its 2wt% aqueous solution at 25 DEG C is 50-100cp；Its consumption is the 1-5% of slurry feedstock gross mass, is added above-mentioned
After the tie substance of consumption, a kind of comprehensive crosslinking is formed between each fiber and other components of slurry, by drying
This crosslinking is in paper afterwards and surface forms a kind of film, and this film can guarantee that the ink for carrying printer and be shifted after heated
Go out, so as to realize uncoated transfer printing, this is another difference of the present invention and prior art.
Described filler is the one or more that particle diameter is less than in 50nm calcium carbonate, bentonite, attapulgite；
Described turning property of filler reinforcing agent is that cationic thermosetting resin or cation superpolymer or polymer-modified silicon are molten
Effective content is more than 12wt% in liquid, solution；Its consumption is the 0.5-1% of slurry feedstock gross mass；It, which is acted on, mainly wraps up
Firmly with the mineral filler and fiber fines of fiber binding ability difference, then produced by the tissue such as the group of itself and other fibers
It is raw to be cross-linked to form adhesion, improve bond strength.
Described sizing agent be dispersion rosin size or alkenyl succinic anhydride (ASA) or alkyl ketene dimer (AKD) or
Its mixture；Its consumption is the 1-2% of slurry feedstock gross mass, and its effect can assign paper suitable water absorbing capacity, can be by table
Face absorbs Weight control within the scope of certain, and consumption of the invention can control the parameter to be 20-40g/m2；
In addition, retention agent, filter aid employed in above-mentioned technique of the invention is all high polymer polyacrylamide,
Retention agent unlike unique is dry powder-shaped, and filter aid is emulsion form, and the molecular weight of the two is different, and the former molecular weight is 5,000,000
Left and right, the latter is typically below 1,000,000, as retention agent may be selected from BASF Percol182, and filter aid may be selected from BASF
Percol740, can directly buy from the market, add wherein the addition of described retention agent is over dry slurry feedstock per ton
0.2~0.5kg；The addition of described filter aid is that over dry slurry feedstock per ton adds 0.7~1.0kg；
Compared with prior art, can one the method have the characteristics that dissolving pulp and sodium carboxymethylcellulose or sodium alginate
It is secondary that calico paper is just directly obtained by copy paper technique, it is not necessary to pass through body paper+coating twice production process.Wherein, dissolving pulp has
There is the features such as fiber height is homogeneous, content of cellulose is high, add the film forming of sodium carboxymethylcellulose or sodium alginate, it is ensured that
The features such as surface is fine and smooth after into paper, film spreadability is good, possesses every feature that surface separately applies a coating.
Beneficial effects of the present invention：The grammes per square metre of paper is substantially reduced, in the market is met to low grammes per square metre, efficient requirement,
Coating production technology is reduced, production cost is greatly reduced.This production technology (includes wet end, pressure using conventional paper machine
Squeezing portion, drying portion, reeling end) finished product can be made, it is not necessary to and sizing applicator is glued, it is not required that coating machine is applied on paper surface
Cloth, equipment is simple, and production efficiency is high.
Embodiment
The present invention is further illustrated with reference to embodiment, can make those skilled in the art that this hair is more completely understood
It is bright, but do not limit the invention in any way.
Embodiment 1
A kind of production technology of uncoated heat sublimation transfer printing paper,
Its slurry feedstock composition is calculated as by weight：60 parts of dissolving pulp, 20 parts of broad-leaved chemical pulp, needle chemical pulp 20
Part；
Concretely comprise the following steps：
Above-mentioned slurry feedstock is beaten respectively in proportion, wherein needle or broad-leaved dissolving pulp is beaten to 28-32 °
SR, broad-leaved chemical pulp are beaten to 33-35 ° of SR, needle chemical pulp and are beaten to 30-33 ° of SR, then press the slurry after above-mentioned mashing
Parts by weight are delivered to slurry pond and mixed in proportion, while adding the filler that parts by weight are 15 parts；
Backward slurry pond in add turning property of filler reinforcing agent and sizing agent and sodium carboxymethylcellulose or sodium alginate
In one kind or mixture, and be well mixed；
By it is above-mentioned be sufficiently mixed uniform slurry and be pumped into destroy forebay, add retention agent filter aid, then entered by head box
Enter that wet end dehydration, press section are further dehydrated, cylinder dried, calender press polish obtain finished product.
The dissolving pulp is that in the market is directly bought with broad-leaved chemical pulp and needle chemical pulp, and wherein dissolving pulp is purchased
The broad-leaved dissolving pulp produced from Anhui Hua Tai Co., Ltds, uses external import star board broad-leaved chemical pulp and Pacific Ocean board needle
Chemical pulp；
The calico paper prepared using above-mentioned technique, quantitative 45g/m2, longitudinal wet tensile index 8.9N.m/g, Surface absorption weight
Measure 35g/m2, transversal stretching rate 1.8%, smoothness 45s；
The substitution value 0.62 of the sodium carboxymethylcellulose wherein used, the sodium alginate 2wt% aqueous solution is viscous at 25 DEG C
Spend for 92cp；Its consumption is the 2% of slurry feedstock gross mass；
Described filler is the calcium carbonate that particle diameter is less than 50nm；
Described turning property of filler reinforcing agent reaches purchased from Jiangyin perseverance, model ZQ-8, and effective content is 14wt% in solution；Its
Consumption is the 1% of slurry feedstock gross mass；
Described sizing agent is that alkyl ketene dimer (AKD) its consumption of Hua Tai Chemical Co., Ltd.s production is that slurry is former
Expect the 2% of gross mass,；
In addition, retention agent, filter aid employed in above-mentioned technique of the invention is all high polymer polyacrylamide,
Retention agent is selected from BASF Percol182, and filter aid is selected from BASF Percol740, wherein the addition of described retention agent
Add 0.5kg for over dry slurry feedstock per ton；The addition of described filter aid is that over dry slurry feedstock per ton adds 1.0kg..
Embodiment 2
A kind of production technology of uncoated heat sublimation transfer printing paper,
Raw material composition is calculated as by weight：40 parts of dissolving pulp, 30 parts of broad-leaved chemical pulp, 30 parts of needle chemical pulp；
Concretely comprise the following steps：
Above-mentioned slurry feedstock is beaten respectively in proportion, wherein needle or broad-leaved dissolving pulp is beaten to 28-32 °
SR, broad-leaved chemical pulp are beaten to 33-35 ° of SR, needle chemical pulp and are beaten to 30-33 ° of SR, then press the slurry after above-mentioned mashing
Parts by weight are delivered to slurry pond and mixed in proportion, while adding the filler that parts by weight are 6 parts；
Backward slurry pond in add turning property of filler reinforcing agent and sizing agent and sodium carboxymethylcellulose or sodium alginate
In one kind or mixture, and be well mixed；
By it is above-mentioned be sufficiently mixed uniform slurry and be pumped into destroy forebay, add retention agent filter aid, then entered by head box
Enter that wet end dehydration, press section are further dehydrated, cylinder dried, calender press polish obtain finished product.
The dissolving pulp is that in the market is directly bought with broad-leaved chemical pulp and needle chemical pulp, and wherein dissolving pulp is purchased
The broad-leaved dissolving pulp produced from Anhui Hua Tai Co., Ltds, uses external import star board broad-leaved chemical pulp and Pacific Ocean board needle
Chemical pulp；
The calico paper prepared using above-mentioned technique, quantitative 44.5g/m2, longitudinal wet tensile index 8.5N.m/g, Surface absorption
Weight 28g/m2, transversal stretching rate 2.2%, smoothness 40s；
The substitution value 0.62 of the sodium carboxymethylcellulose wherein used, the sodium alginate 2wt% aqueous solution is viscous at 25 DEG C
Spend for 92cp；Its consumption is the 5% of slurry feedstock gross mass
Described filler is the attapulgite that particle diameter is less than 50nm
Described turning property of filler reinforcing agent reaches purchased from Jiangyin perseverance, model ZQ-8, and effective content is 14wt% in solution；Its
Consumption is the 0.5% of slurry feedstock gross mass；
Described sizing agent is that alkyl ketene dimer (AKD) its consumption of Hua Tai Chemical Co., Ltd.s production is that slurry is former
Expect the 1% of gross mass；
In addition, retention agent, filter aid employed in above-mentioned technique of the invention is all high polymer polyacrylamide,
Retention agent is selected from BASF Percol182, and filter aid is selected from BASF Percol740, wherein the addition of described retention agent
Add 0.3kg for over dry slurry feedstock per ton；The addition of described filter aid is that over dry slurry feedstock per ton adds 0.7kg.
Comparative example
By gained finished product and the corresponding parameter experiment of conventional paper progress of the prior art, it see the table below：
Product quality is contrasted：
Contrast：Wet tensile index is more than 2 times of conventional paper, improves pulling force of the paper when great Mo amounts are soaked；Laterally stretch
Shrinkage significantly reduces, and reduces playing drum, rubbing shower nozzle phenomenon in print procedure；Pad-ink vividness and the rate of transform before transfer
It is slightly above routine paper；Rate of drying is higher than conventional paper, and more much lower than conventional paper into paper grammes per square metre, reduces and uses into
This.
Production cost：
Analysis：The species of two kinds of production method fibrous raw materials is different with proportioning, the fibrous raw material cost of uncoated transfer paper
It is higher than conventional coating paper but uncoated paper eliminates coating production process, it is comprehensive which reduces 1788 yuan of coating expense
Synthesize this 292 yuan/ton of paper lower than the transfer paper that conventional production process is obtained.And product quality is higher than conventional coating paper, because
Grammes per square metre belongs to ultralow gram weight, and use cost is far below conventional products.
Claims (5)
1. a kind of production technology of uncoated heat sublimation transfer printing paper, it is characterised in that：Its slurry feedstock is constituted by weight
It is calculated as：40-60 parts of dissolving pulp, 20-30 parts of broad-leaved chemical pulp, 20-30 parts of needle chemical pulp；
Production is concretely comprised the following steps：
Above-mentioned slurry feedstock is beaten respectively in proportion, wherein needle or broad-leaved dissolving pulp are beaten to 28-32 ° of SR, wealthy
Leaf chemical pulp is beaten to 33-35 ° of SR, needle chemical pulp and is beaten to 30-33 ° of SR, then by the slurry after above-mentioned mashing by weight
Part is delivered to slurry pond and mixed in proportion, while adding the filler that parts by weight are 5-15 parts；
Backward slurry pond in add in turning property of filler reinforcing agent and sizing agent and sodium carboxymethylcellulose or sodium alginate
A kind of or mixture, and be well mixed；
By it is above-mentioned be sufficiently mixed uniform slurry and be pumped into destroy forebay, add retention agent, filter aid, then enter to network by head box
Portion's dehydration, press section are further dehydrated, cylinder dried, calender press polish obtain finished product.
2. described technique according to claim 1, it is characterised in that：The substitution value of described sodium carboxymethylcellulose >=
0.6, sodium alginate uses the sodium alginate of medium-high viscosity, and viscosity of its 2wt% aqueous solution at 25 DEG C is 50-100cp；It is used
Measure as the 1-5% of slurry feedstock gross mass.
3. described technique according to claim 1, it is characterised in that：Described filler is the carbonic acid that particle diameter is less than 50nm
One or more in calcium, bentonite, attapulgite.
4. described technique according to claim 1, it is characterised in that：Described turning property of filler reinforcing agent is cation heat
Effective content is more than 12wt% in thermosetting resin or cation superpolymer or polymer-modified silicon solution, solution；Its consumption is slurry
Expect the 0.5-1% of raw material gross mass；Described sizing agent is dispersion rosin size or alkenyl succinic anhydride or alkyl ketene dimerization
Body or its mixture；Its consumption is the 1-2% of slurry feedstock gross mass.
5. described technique according to claim 1, it is characterised in that：Described retention agent, filter aid are all macromolecules
Polyacrylamide, wherein retention agent are dry powder-shapeds, and filter aid is emulsion form, and the addition of described retention agent is oven dry stock per ton
Material raw material adds 0.2~0.5kg；The addition of described filter aid is that over dry slurry feedstock per ton adds 0.7~1.0kg.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611253121 | 2016-12-30 | ||
| CN2016112531212 | 2016-12-30 |
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| Publication Number | Publication Date |
|---|---|
| CN107059463A true CN107059463A (en) | 2017-08-18 |
| CN107059463B CN107059463B (en) | 2018-05-18 |
Family
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| CN201710310394.4A Active CN107059463B (en) | 2016-12-30 | 2017-05-05 | A kind of production technology of uncoated heat sublimation transfer printing paper |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110093806A (en) * | 2019-05-06 | 2019-08-06 | 浙江科技学院 | A kind of uncoated digital ink-jet base paper for excursion press mark and its production method |
| CN110130142A (en) * | 2019-05-06 | 2019-08-16 | 浙江科技学院 | A kind of low grammes per square metre digital ink-jet base paper for excursion press mark and its production method |
| 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 |
| CN110884280A (en) * | 2018-09-10 | 2020-03-17 | 安徽江南春包装科技有限公司 | Production process of uncoated thermal sublimation transfer printing paper |
| CN111088723A (en) * | 2019-12-23 | 2020-05-01 | 山东华泰纸业股份有限公司 | Production process of simple transfer printing paper |
| CN111826992A (en) * | 2020-07-24 | 2020-10-27 | 淄博圣泉纸业有限公司 | Transfer printing base paper suitable for ink printing |
| CN114889223A (en) * | 2022-06-02 | 2022-08-12 | 重庆市渝北区中央公园小学校 | Automatic hydraulic forming device for pattern hand tissue |
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| CN102362031A (en) * | 2009-02-10 | 2012-02-22 | 鲍吉肥料公司 | Use of aluminum phosphate, polyphosphate and metaphosphate particles in paper coating applications |
| CN102864675A (en) * | 2011-06-07 | 2013-01-09 | 王子制纸株式会社 | Manufacturing method of coated paper for printing |
| CN103774469A (en) * | 2013-12-06 | 2014-05-07 | 苏州大学 | Dry-type transfer-printed textile and preparation method thereof |
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| CN101448999A (en) * | 2006-03-28 | 2009-06-03 | 环宇企业集团有限公司 | Transfer paper for dry transfer printing and method of dry transfer printing with the same |
| CN102362031A (en) * | 2009-02-10 | 2012-02-22 | 鲍吉肥料公司 | Use of aluminum phosphate, polyphosphate and metaphosphate particles in paper coating applications |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110884280A (en) * | 2018-09-10 | 2020-03-17 | 安徽江南春包装科技有限公司 | Production process of uncoated thermal sublimation transfer printing paper |
| CN110093806A (en) * | 2019-05-06 | 2019-08-06 | 浙江科技学院 | A kind of uncoated digital ink-jet base paper for excursion press mark and its production method |
| CN110130142A (en) * | 2019-05-06 | 2019-08-16 | 浙江科技学院 | A kind of low grammes per square metre digital ink-jet base paper for excursion press mark and its production method |
| CN110130142B (en) * | 2019-05-06 | 2022-04-05 | 浙江科技学院 | Low-gram-weight digital ink-jet transfer printing base paper and production method thereof |
| 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 |
| CN110644286B (en) * | 2019-09-19 | 2021-10-08 | 山东华泰纸业股份有限公司 | High-heat-conduction anti-static thermal sublimation transfer printing paper |
| CN111088723A (en) * | 2019-12-23 | 2020-05-01 | 山东华泰纸业股份有限公司 | Production process of simple transfer printing paper |
| CN111826992A (en) * | 2020-07-24 | 2020-10-27 | 淄博圣泉纸业有限公司 | Transfer printing base paper suitable for ink printing |
| CN114889223A (en) * | 2022-06-02 | 2022-08-12 | 重庆市渝北区中央公园小学校 | Automatic hydraulic forming device for pattern hand tissue |
| CN114889223B (en) * | 2022-06-02 | 2023-11-07 | 重庆市渝北区中央公园小学校 | Automatic pattern manual paper water pressure forming device |
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| Publication number | Publication date |
|---|---|
| CN107059463B (en) | 2018-05-18 |
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Denomination of invention: Production process of uncoated thermal sublimation transfer printing paper Effective date of registration: 20211223 Granted publication date: 20180518 Pledgee: Industrial and Commercial Bank of China Limited Guangrao sub branch Pledgor: SHANDONG HUATAI PAPER Co.,Ltd. Registration number: Y2021980015852 |