CN105040507B - A kind of film coated base paper and its production technology - Google Patents
A kind of film coated base paper and its production technology Download PDFInfo
- Publication number
- CN105040507B CN105040507B CN201510375310.6A CN201510375310A CN105040507B CN 105040507 B CN105040507 B CN 105040507B CN 201510375310 A CN201510375310 A CN 201510375310A CN 105040507 B CN105040507 B CN 105040507B
- Authority
- CN
- China
- Prior art keywords
- slurry
- parts
- concentration
- film coated
- base paper
- 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.)
- Active
Links
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
- D21H15/00—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution
- D21H15/02—Pulp or paper, comprising fibres or web-forming material characterised by features other than their chemical constitution characterised by configuration
- D21H15/10—Composite fibres
-
- 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
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/66—Salts, e.g. alums
-
- 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
- D21H21/20—Wet strength agents
Abstract
The present invention discloses a kind of film coated base paper and its production technology, and its shown technique is to obtain film coated base paper sandwich layer slurry with reducing rules, needle slurry, broad-leaved slurry and waste stuff proportioning；Surface layer slurry is obtained with needle slurry and broad-leaved slurry proportioning；And surface layer slurry bottom slurry is obtained with needle slurry and broad-leaved slurry proportioning；Three part sizes enter head box through constant displacement pump respectively, then compound into three layers of wet end via wet end, are got product then in turn through squeezing, dry, applying glue, dry, press polish.The present invention is on the premise of product quality is ensured, the improvement to the proportioning and technique of slurry adds waste stuff in original technical recipe, improves the consumption of reducing rules, reduces the consumption of hardwood pulp and softwood pulp, is especially the reduction of the consumption of import slurry.
Description
Technical field
The present invention relates to paper technology, and in particular to a kind of film coated base paper and its production technology.
Background technology
Film coated base paper is a kind of paperboard dedicated for film system cup, with high-stiffness and high water resistance, typically without
Coating.Film (and printing) is carried out on film coated base paper, is subsequently used for that leaching membrane paper is made, splendid attire and storage for liquid.Side
Just the paper bowl in face falls within the category of leaching membrane paper.Leaching membrane paper is one kind of flexible package punch paper, contains the time ratio used after liquid
Shorter, general dozens of minutes were by one week.According to the use requirement of film coated base paper, it is needed with water resistant, oil resistant, anti-lactic acid, anti-
The performances such as hydrogen peroxide.The requirement of its small edge penetration is more more than other flexible package punch paper.
With the raising and the enhancing of environmental consciousness of living standards of the people, pollution of the disposal plastic cup to environment is very tight
Weight, need to go up a century can just be decomposed, therefore film coated base paper development prospect is wide.
Domestic and international industrial film coated base paper is typically all matched somebody with somebody using softwood pulp, hardwood chemical pulp to be copied, industrial film coated base
Paper is during the manufacturing, and because slurry and wet end furnish are different, unstable to be easily caused paper surface strong for technical data
The quality problems such as degree, transversal stretching rate, water imbibition, the amount of being filled with, form and aspect.And leaf wood and pin in film coated base paper in the prior art
Leaf wood pulp material materials are larger, once added the production cost of product.
The content of the invention
In order to solve the deficiencies in the prior art, the invention provides a kind of film coated base paper and its production technology.
The technical scheme is that：A kind of film coated base paper production technology, it is characterised in that with reducing rules, needle slurry, it is wealthy
Leaf is starched and waste stuff proportioning obtains film coated base paper sandwich layer slurry；Surface layer slurry is obtained with needle slurry and broad-leaved slurry proportioning；And with needle
Slurry and broad-leaved slurry proportioning obtain surface layer slurry bottom slurry；Three part sizes enter head box through constant displacement pump respectively, then enter via wet end
Enter three layers of wet end to be combined, got product then in turn through squeezing, dry, applying glue, dry, press polish.
Further improvement of the present invention includes：
The concentration of surface layer slurry is that 2.5-3.0%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 3g；The sandwich layer
The concentration of slurry is that 2.5-3.0%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 3g；The concentration of the sandwich layer slurry is 2.5-
3.0%th, beating degree is 27-33 ° of SR, weight in wet base for not less than 2g.
Described surface layer slurry weight proportion is that 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleached sulphates are wealthy
Leaf wood pulp；Described bottom slurry weight proportion is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleached sulphate broad-leaveds
Wood pulp.
Described sandwich layer slurry weight proportion is 60-65 parts of APMPs, 30-35 parts of waste stuffs, 3 parts of bleachings
Kp softwood pulp, 0-5 parts of BRATSKs.
Described sandwich layer slurry weight proportion is 60-65 parts of APMPs, 15-20 parts of bleached chemi-mechanical mills
Wood pulp, 20-15 parts of waste stuffs, 3 parts of bleached sulphate softwood pulps, 0-5 parts of BRATSKs.
Prime cement consumption is 28-34g in every square metre of leaching membrane paper, and surface layer slurry consumption is 28-34g, and core slurry consumption is 90-
180g。
The beating consistency of the reducing rules is that 4.5-5%, beating degree are that 28-35 ° of SR, weight in wet base are not less than 1.5g；Needle is starched
Beating consistency be that 4.5-5%, beating degree are that 27-33 ° of SR, weight in wet base are 8-10g；Beating consistency between broad-leaved is 5-5.5%,
Beating degree is 27-33 ° of SR, weight in wet base not less than 2g；The beating consistency of waste stuff be 4.5-5%, beating degree be 27-33 ° of SR, it is wet
It is not less than 2g again.
The surface layer slurry also concentration including 2.8 mass parts is that 35% gum rosin, the concentration of 2.8 mass parts are 5% sulfuric acid
Aluminium, the concentration of 1 mass parts is 12.5% wet strength agent；The bottom slurry also concentration including 2.8 mass parts is 35% gum rosin,
The concentration of 2.8 mass parts is 5% aluminum sulfate, and the concentration of 1 mass parts is 12.5% wet strength agent；The sandwich layer slurry also includes 3.2 matter
It is 5% aluminum sulfate to measure the gum rosin, the concentration of 3.2 mass parts that part concentration is 35%, and the concentration of 1.1 mass parts is wet strong for 12.5%
Agent.
Another object of the present invention is to provide a kind of film coated base paper as made from weighing above-mentioned production technology.
The present invention is on the premise of product quality is ensured, to the improvement of the proportioning and technique of slurry in original technical recipe
In add waste stuff, improve the consumption of reducing rules, reduce the consumption of hardwood pulp and softwood pulp, be especially the reduction of import
The consumption of slurry.Reduce the production cost of product.Manufacturing process of the present invention is simple, manufacturing cost reduction, the industry pouring of production
Film paper roll is elastic consistent；Quantitative, thickness is homogeneous, and bursting strength is good；With preferable surface strength and suitable water imbibition.Deflection
Height, forming, while oozing, effect is good, and water resistant, anti-lactic acid exceed national standard, and comply fully with food grade hygienic.
It is produced by the present invention as shown in the table into paper physical index：
Table 1
Brief description of the drawings
Fig. 1 is present invention process schematic flow sheet.
Embodiment
The present invention is elaborated below in conjunction with the accompanying drawings.
As shown in figure 1, a kind of film coated base paper production technology of the invention, it is characterised in that with reducing rules, needle slurry, broad-leaved
Slurry and waste stuff proportioning obtain film coated base paper sandwich layer slurry；Surface layer slurry is obtained with needle slurry and broad-leaved slurry proportioning；And starched with needle
Surface layer slurry bottom slurry is obtained with broad-leaved slurry proportioning；Three part sizes enter head box through constant displacement pump respectively, then enter via wet end
Three layers of wet end is combined, and is got product then in turn through squeezing, dry, applying glue, dry, press polish.
Further improvement of the present invention includes：The concentration of surface layer slurry be 2.5-3.0%, beating degree be 27-33 ° of SR,
Weight in wet base is not less than 3g；The concentration of sandwich layer slurry is that 2.5-3.0%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 3g；Institute
The concentration for stating sandwich layer slurry is that 2.5-3.0%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 2g.
Described surface layer slurry weight proportion is that 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleached sulphates are wealthy
Leaf wood pulp；Described bottom slurry weight proportion is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleached sulphate broad-leaveds
Wood pulp.
Described sandwich layer slurry weight proportion is 60-65 parts of APMPs, 30-35 parts of waste stuffs, 3 parts of bleachings
Kp softwood pulp, 0-5 parts of BRATSKs.
Described sandwich layer slurry weight proportion is 60-65 parts of APMPs, 15-20 parts of bleached chemi-mechanical mills
Wood pulp, 20-15 parts of waste stuffs, 3 parts of bleached sulphate softwood pulps, 0-5 parts of BRATSKs.
Prime cement consumption is 28-34g in every square metre of leaching membrane paper, and surface layer slurry consumption is 28-34g, and core slurry consumption is 90-
180g。
The beating consistency of the reducing rules is that 4.5-5%, beating degree are that 28-35 ° of SR, weight in wet base are not less than 1.5g；Needle is starched
Beating consistency be that 4.5-5%, beating degree are that 27-33 ° of SR, weight in wet base are 8-10g；Beating consistency between broad-leaved is 5-5.5%,
Beating degree is 27-33 ° of SR, weight in wet base not less than 2g；The beating consistency of waste stuff be 4.5-5%, beating degree be 27-33 ° of SR, it is wet
It is not less than 2g again.
The surface layer slurry also concentration including 2.8 mass parts is that 35% gum rosin, the concentration of 2.8 mass parts are 5% sulfuric acid
Aluminium, the concentration of 1 mass parts is 12.5% wet strength agent；The bottom slurry also concentration including 2.8 mass parts is 35% gum rosin,
The concentration of 2.8 mass parts is 5% aluminum sulfate, and the concentration of 1 mass parts is 12.5% wet strength agent；The sandwich layer slurry also includes 3.2 matter
It is 5% aluminum sulfate to measure the gum rosin, the concentration of 3.2 mass parts that part concentration is 35%, and the concentration of 1.1 mass parts is wet strong for 12.5%
Agent.
Another object of the present invention is to provide a kind of film coated base paper as made from weighing above-mentioned production technology.
The present invention is on the premise of product quality is ensured, to the improvement of the proportioning and technique of slurry in original technical recipe
In add waste stuff, improve the consumption of reducing rules, reduce the consumption of hardwood pulp and softwood pulp, be especially the reduction of import
The consumption of slurry.Reduce the production cost of product.Manufacturing process of the present invention is simple, manufacturing cost reduction, the industry pouring of production
Film paper roll is elastic consistent；Quantitative, thickness is homogeneous, and bursting strength is good；With preferable surface strength and suitable water imbibition.Deflection
Height, forming, while oozing, effect is good, and water resistant, anti-lactic acid exceed national standard, and comply fully with food grade hygienic.
By taking 150-190g/ ㎡ film coated base paper as an example, the quantification of 30 ± 2g of surface layer slurry, bottom starches quantification of 30 ± 2g,
Sandwich layer starches quantification of 90-120g, ash content 9 ± 1%；Surface layer slurry proportioning is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts
BRATSK；Bottom slurry weight proportion is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleaching sulfuric acid
Salt hardwood pulp；Sandwich layer slurry proportioning is 60-65 parts of APMPs, 30-35 parts of waste stuffs, 3 parts of bleached sulphates
Softwood pulp；Or sandwich layer slurry proportioning is used for 60-70 parts of APMPs, and 15-20 parts of waste stuffs, 15-20 parts
Bleached chemi-mechanical ground wood pulp, 3 parts of bleached sulphate softwood pulps.
By taking 190-230g/ ㎡ leaching membrane paper as an example, the quantification of 30 ± 2g of surface layer slurry, bottom starches quantification of 30 ± 2g, core
The quantification of 130-170g of layer slurry, ash content 10 ± 1%；Surface layer slurry proportioning is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts
BRATSK；Bottom slurry weight proportion is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleaching sulfuric acid
Salt hardwood pulp；Sandwich layer slurry proportioning is 60-65 parts of APMPs, 30-35 parts of waste stuffs, 3 parts of bleached sulphates
Softwood pulp.3 parts of BRATSKs；Or sandwich layer slurry proportioning is used for 60-70 parts of APMPs,
15-20 parts of waste stuffs, 15-20 parts of bleached chemi-mechanical ground wood pulps, 3 parts of bleached sulphate softwood pulps, 3 parts of bleached sulphates
Hardwood pulp.
By taking more than 230g/ ㎡ film coated base paper as an example, the quantification of 32 ± 2g of surface layer slurry, bottom starches quantification of 32 ± 2g,
Sandwich layer slurry is quantification of to be not less than 180g, ash content 10 ± 1%；Surface layer slurry proportioning is 30-40 parts of bleached sulphate softwood pulps and 60-
70 parts of BRATSKs；Bottom slurry weight proportion is 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of bleachings
Sulfate hardwood pulp；Sandwich layer slurry proportioning is 60-65 parts of APMPs, 30-35 parts of waste stuffs, 3 parts of bleaching sulphur
Hydrochlorate softwood pulp, 5 parts of BRATSKs；Or sandwich layer slurry proportioning is used for 60-70 parts of alkaline hydrogen peroxide machines
Tool is starched, 15-20 parts of waste stuffs, 15-20 parts of bleached chemi-mechanical ground wood pulps, 3 parts of bleached sulphate softwood pulps, 5 parts of bleaching sulphur
Hydrochlorate hardwood pulp.
Auxiliary material and technique in production process is as follows：
The general principle and principal character and advantages of the present invention of the present invention has been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the simply explanation described in above-described embodiment and specification is originally
The principle of invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (7)
1. a kind of film coated base paper production technology, it is characterised in that obtained with reducing rules, needle slurry, broad-leaved slurry and waste stuff proportioning
Film coated base paper sandwich layer is starched, and described sandwich layer slurry weight proportion is 60-65 parts of APMPs, 30-35 parts of waste stuffs,
3 parts of bleached sulphate softwood pulps, 0-5 parts of BRATSKs；Surface layer slurry is obtained with needle slurry and broad-leaved slurry proportioning；
And surface layer slurry bottom slurry is obtained with needle slurry and broad-leaved slurry proportioning；Three part sizes enter head box through constant displacement pump respectively, then
It is combined for three layers, is got product then in turn through squeezing, dry, applying glue, dry, press polish into wet end via wet end；The face
The concentration of layer slurry is that 2.5-3.0%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 3g；The concentration of the sandwich layer slurry is 2.5-
3.0%th, beating degree is 27-33 ° of SR, weight in wet base for not less than 3g；The concentration of sandwich layer slurry is that 2.5-3.0%, beating degree are 27-
33 ° of SR, weight in wet bases are not less than 2g.
2. a kind of film coated base paper production technology according to claim 1, it is characterised in that described surface layer slurry weight proportion
For 30-40 parts of bleached sulphate softwood pulps and 60-70 parts of BRATSKs；Described bottom starches weight proportion
30-40 parts of bleached sulphate softwood pulps and 60-70 parts of BRATSKs.
3. a kind of film coated base paper production technology according to claim 1, it is characterised in that described sandwich layer slurry weight proportion
For 60-65 parts of APMPs, 15-20 parts of bleached chemi-mechanical ground wood pulps, 20-15 parts of waste stuffs, 3 parts of bleaching sulphur
Hydrochlorate softwood pulp, 0-5 parts of BRATSKs.
4. a kind of film coated base paper production technology according to claim 1, it is characterised in that in every square metre of leaching membrane paper
Prime cement consumption is 28-34g, and surface layer slurry consumption is 28-34g, and core slurry consumption is 90-180g.
5. a kind of film coated base paper production technology according to claim any one of 1-4, it is characterised in that the reducing rules
Beating consistency is that 4.5-5%, beating degree are that 28-35 ° of SR, weight in wet base are not less than 1.5g；The beating consistency of needle slurry is 4.5-
5%th, beating degree is that 27-33 ° of SR, weight in wet base are 8-10g；Beating consistency between broad-leaved be 5-5.5%, beating degree be 27-33 ° of SR,
Weight in wet base is not less than 2g；The beating consistency of waste stuff is that 4.5-5%, beating degree are that 27-33 ° of SR, weight in wet base are not less than 2g.
6. a kind of film coated base paper production technology according to claim any one of 1-4, it is characterised in that the surface layer slurry is also
Concentration including 2.8 mass parts is that 35% gum rosin, the concentration of 2.8 mass parts are 5% aluminum sulfate, and the concentration of 1 mass parts is
12.5% wet strength agent；The bottom slurry also concentration including 2.8 mass parts is that 35% gum rosin, the concentration of 2.8 mass parts are 5%
Aluminum sulfate, the concentration of 1 mass parts is 12.5% wet strength agent；The sandwich layer slurry also includes the rosin that 3.2 mass parts concentration are 35%
Glue, the concentration of 3.2 mass parts are 5% aluminum sulfate, and the concentration of 1.1 mass parts is 12.5% wet strength agent.
7. a kind of film coated base paper, it is characterised in that be made as the production technology described in claim 1-6.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510375310.6A CN105040507B (en) | 2015-06-29 | 2015-06-29 | A kind of film coated base paper and its production technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510375310.6A CN105040507B (en) | 2015-06-29 | 2015-06-29 | A kind of film coated base paper and its production technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105040507A CN105040507A (en) | 2015-11-11 |
| CN105040507B true CN105040507B (en) | 2017-08-25 |
Family
ID=54447458
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510375310.6A Active CN105040507B (en) | 2015-06-29 | 2015-06-29 | A kind of film coated base paper and its production technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105040507B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110512457A (en) * | 2019-08-08 | 2019-11-29 | 岳阳林纸股份有限公司 | A kind of manufacturing method of grease proofing film coated base paper |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105603828A (en) * | 2016-01-07 | 2016-05-25 | 仙鹤股份有限公司 | Production method for salt bag |
| CN108486948B (en) * | 2018-03-15 | 2020-12-08 | 中国制浆造纸研究院衢州分院 | Production process of natural-color paper cup base paper |
| CN111101402A (en) * | 2019-12-12 | 2020-05-05 | 宁波亚洲浆纸业有限公司 | Food cardboard and preparation method thereof |
| CN111188225A (en) * | 2020-01-06 | 2020-05-22 | 宁波亚洲浆纸业有限公司 | Core layer pulp for paper cup base paper, paper cup base paper and preparation method thereof |
| CN111235940A (en) * | 2020-01-14 | 2020-06-05 | 宁波亚洲浆纸业有限公司 | Preparation method of core layer slurry, base paper, paperboard and paper machine |
| CN114481670B (en) * | 2022-02-25 | 2023-11-10 | 东莞金洲纸业有限公司 | Calculation and compensation algorithm for dosage of paper machine chemicals or auxiliary materials |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102517970A (en) * | 2011-12-30 | 2012-06-27 | 珠海经济特区红塔仁恒纸业有限公司 | Coated ivory paperboard for blister package and production method thereof |
| CN102926278A (en) * | 2012-11-08 | 2013-02-13 | 珠海经济特区红塔仁恒纸业有限公司 | Oil-proof coating white cardboard and process for producing the same |
| CN103074822A (en) * | 2012-12-28 | 2013-05-01 | 珠海华丰纸业有限公司 | Special paper for external standard of cup bowl and manufacturing technology thereof |
| CN104562828A (en) * | 2015-01-14 | 2015-04-29 | 珠海华丰纸业有限公司 | Ultrahigh-loose thickness noodle bowl paper and production process thereof |
-
2015
- 2015-06-29 CN CN201510375310.6A patent/CN105040507B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102517970A (en) * | 2011-12-30 | 2012-06-27 | 珠海经济特区红塔仁恒纸业有限公司 | Coated ivory paperboard for blister package and production method thereof |
| CN102926278A (en) * | 2012-11-08 | 2013-02-13 | 珠海经济特区红塔仁恒纸业有限公司 | Oil-proof coating white cardboard and process for producing the same |
| CN103074822A (en) * | 2012-12-28 | 2013-05-01 | 珠海华丰纸业有限公司 | Special paper for external standard of cup bowl and manufacturing technology thereof |
| CN104562828A (en) * | 2015-01-14 | 2015-04-29 | 珠海华丰纸业有限公司 | Ultrahigh-loose thickness noodle bowl paper and production process thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110512457A (en) * | 2019-08-08 | 2019-11-29 | 岳阳林纸股份有限公司 | A kind of manufacturing method of grease proofing film coated base paper |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105040507A (en) | 2015-11-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105040507B (en) | A kind of film coated base paper and its production technology | |
| CN102912690B (en) | The flexible package punch paper of a kind of high-stiffness and production technology thereof | |
| CN103321096B (en) | A kind of coated white cardboard and production technology thereof | |
| CN105386370B (en) | A kind of Original Pulp paperboard and preparation method thereof | |
| CN110512457A (en) | A kind of manufacturing method of grease proofing film coated base paper | |
| CN106638115A (en) | Supersoft household paper and manufacturing method thereof | |
| CN109183487B (en) | Method for making salt packaging paper | |
| CN106436479B (en) | A kind of high bulk flexible package punch base board and preparation method thereof | |
| CN101736645B (en) | Composite base paper and production method thereof | |
| CN103993500A (en) | Coated white board paper specially for blister packaging and preparation process of coated white board paper | |
| CN101787662A (en) | Method for producing computer-to-plate lining paper | |
| CN203411861U (en) | Production system of coated white board | |
| CN102154957A (en) | Natural-color cigarette cardboard and production method thereof | |
| CN102888778A (en) | Production method of glassine body paper | |
| CN102979008A (en) | Raw paper, preparation method thereof, and craft paper | |
| CN107095611A (en) | A kind of tissue and preparation method thereof | |
| CN104928968A (en) | Coated kraft paper and production technology thereof | |
| CN106245415B (en) | A kind of manufacture method of glassine paper | |
| CN108301255A (en) | A kind of high bulky locker paper and preparation method thereof | |
| CN106400602A (en) | Cake supporting paper and manufacturing method thereof | |
| CN102182105A (en) | Four-stacked net forming equipment and method for producing coating kraft liner board | |
| CN107964825B (en) | Raw paper of carton paper with low gram weight and production method and application thereof | |
| CN202989686U (en) | Liquid packaging paper with high stiffness | |
| JP2022547166A (en) | Water-based adhesive for manufacturing laminated cellulose board containing single-phase graphene oxide, laminated cellulose board obtained using same, and method for producing the same | |
| CN103790069A (en) | Paperboard for anti-counterfeit cigarette |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230814 Address after: Qiliying Town Xinzhuang Village, Xinxiang County, Xinxiang City, Henan Province, 453000 Patentee after: Henan Xinya new technology packaging materials Co.,Ltd. Address before: 453000 Paper Products Industrial Park, Xinxiang County, Xinxiang City, Henan Province (680 kilometers away from National Highway 107) Patentee before: XINXIANG XINYA PAPER GROUP Co.,Ltd. |