CN105239442B - A kind of preparation method of lower shrinkage secondary stock neutral sizing - Google Patents
A kind of preparation method of lower shrinkage secondary stock neutral sizing Download PDFInfo
- Publication number
- CN105239442B CN105239442B CN201510660143.XA CN201510660143A CN105239442B CN 105239442 B CN105239442 B CN 105239442B CN 201510660143 A CN201510660143 A CN 201510660143A CN 105239442 B CN105239442 B CN 105239442B
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- China
- Prior art keywords
- paper
- neutral sizing
- secondary stock
- wood pulp
- raw material
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Links
- 238000004513 sizing Methods 0.000 title claims abstract description 16
- 230000007935 neutral effect Effects 0.000 title claims abstract description 15
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 239000002002 slurry Substances 0.000 claims abstract description 8
- 239000010893 paper waste Substances 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims abstract description 6
- 238000004537 pulping Methods 0.000 claims abstract description 3
- 229920001131 Pulp (paper) Polymers 0.000 claims description 16
- 238000004061 bleaching Methods 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 10
- 229910021653 sulphate ion Inorganic materials 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000002761 deinking Substances 0.000 claims description 4
- 230000000930 thermomechanical effect Effects 0.000 claims description 4
- 239000004744 fabric Substances 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 2
- 238000004026 adhesive bonding Methods 0.000 abstract description 7
- 238000003475 lamination Methods 0.000 abstract description 7
- 238000001816 cooling Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 238000007639 printing Methods 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Abstract
The invention discloses a kind of preparation methods of lower shrinkage secondary stock neutral sizing.The preparation method of lower shrinkage secondary stock neutral sizing of the present invention is by using unique making raw material proportioning, slurry when paper machine pulping method, to solve the problems, such as existing do not have good lamination or gluing function by the neutral sizing of primary raw material of waste paper, the method of the present invention can improve the shrinkage of paper, smoothness and intensity, the lower shrinkage secondary stock neutral sizing shrinkage produced reaches within 3mm, reach 40S or more at paper positive and negative smoothness, paper tensile strength MD >=2.8KN/M, paper tensile strength CD >=1.3KN/M, and have good lamination or gluing function, it is suitble to promote and apply.
Description
Technical field
The present invention relates to paper technologies, and in particular to a kind of preparation method of lower shrinkage secondary stock neutral sizing.
Technical background
At present in regenerated papermaking industry, do not have good lamination generally using the neutral sizing that waste paper is main material production
Or gluing function, purposes range is smaller, while the domestic lower shrinkage secondary stock neutral sizing production based on wastepaper as raw material
Enterprise can not provide lamination or product that gluing effect is stablized is to packaging due to immature etc. in production Technology
Printing enterprise causes the lower shrinkage neutral sizing product of Packaging and Printing Enterprises demand to rely primarily on whole wood pulp product or import production
Product improve cost.
Invention content
It is good it is an object of the invention to solve not having generally using waste paper as the neutral sizing of main material production at present
The problem of lamination or gluing function, provides a kind of lower shrinkage secondary stock neutral sizing having good lamination or gluing function
Preparation method.
Above-mentioned purpose of the present invention is achieved by the following technical programs:
A kind of preparation method of lower shrinkage secondary stock neutral sizing includes the following steps:
(1)Raw material is the high whiteness high-cleanness, high Deinking Pulp that Mixed Office WasteMOW is produced;Mixed Office WasteMOW raw material line
Adapted 30%37# U.S.s are useless, 20% Japan's 3# waste paper and 50% state give up high-quality little Hua and great Hua;
(2)Paper machine is manufactured paper with pulp wet end furnish:15% sulphate chemical bleaching mixing wood pulp, 75% deinking of MOW slurry and
10% waste stuff;Wherein, the sulphate chemical bleaching mixing wood pulp is the long fine wood pulp of 50% sulphate chemical bleaching and 50% chemistry
Bleach the mixing of thermomechanical wood pulp;
(3)Paper machine pulping method:Screen cloth jet-wire ratio is less than 65 meters, and product moisture norm controlling is 5.0 in production process
±0.5%。
Above-mentioned steps are the step of present invention improves, remaining preparation process is the prior art, is repeated no more.
Compared with prior art, the present invention has the advantages that:
(1)In common secondary stock wood-free paper raw material proportioning, 37# U.S.s give up and the proportional quantity of Japan 3# is within 40%, this hair
Bright raw material proportioning and traditional difference, the useless proportioning with Japan 3# of 37# U.S.s is improved, can improve the contraction of paper in this way
Property, flatness and smoothness;
(2)Common secondary stock wood-free paper does not use sulphate chemical bleached wood pulp, only the change of simple addition 5 ~ 10%
Bleaching thermomechanical wood pulp is learned, is not furnished with the long fine wood pulp of sulphate chemical bleaching, the present invention is long fine using sulphate chemical bleaching
The obtained mixing wood pulp of wood pulp and the short fine mix and match of machinery, contributes to the intensity and smoothness that improve paper;
(3)Common secondary stock wood-free paper screen cloth jet-wire ratio is 70 meters or more, and the present invention is by net Transmission Ratio Control 65
Rice is hereinafter, can improve the shrinkage after paper making;
(4)Common secondary stock wood-free paper product moisture is 6.0 ± 1.0%, and the present invention controls moisture 5.0 ± 0.5%,
It may insure the intensity and deflection of paper;
(5)The method of the present invention can improve the shrinkage, smoothness and intensity of paper, the lower shrinkage secondary stock produced
Neutral sizing shrinkage reaches within 3mm, reaches 40S or more, paper tensile strength MD >=2.8KN/ at paper positive and negative smoothness
M, paper tensile strength CD >=1.3KN/M, and have good lamination or gluing function.
Specific implementation mode
With reference to embodiment, the present invention is further elaborated.But embodiment is not the present invention any type of
It limits.
Embodiment 1
Preparation flow:Blending chest-paper machine stock tank-mono- section scummer-mono- section pressure-head box-web part of paper machine
(Aladdin former)- press section of a paper machine(Shoe press)- drying cylinder(Front baking portion)- surface size press-drying cylinder(After dry)- cold
The hard calender-of cylinder-batches-rewinding completion-cut paper choosing reason and is packaged storage.
Technological process parameter declaration:
1, raw material proportioning:
BKP lines match:The long fine wood pulp+40-60% chemical bleaching thermomechanical wood pulps of 40%-60% sulphate chemicals bleaching;
DMOW lines match:+ 50% state of+20%-30% Japan 3# waste paper that gives up of 20%-30%37# U.S.s gives up high-quality little Hua and great Hua;
2, blending chest technological parameter:Slurry concentration:4.0%-5.0%;
3, paper machine stock tank technological parameter:Slurry concentration:4.0%-5.0%;
4, one section of scummer technological parameter:Operating pressure:350-400KPa;Outlet pressure 10KPa;Single branch throughput:
500L/min;Single branch inlet outlet pressure differential:160KPa;
5, one section of pressurized screen process control parameter:Slurry throughput:70000-110000L/min, into slurry concentration:C=1.0-
1.2%, into slurry pressure: 4.0-6.0bar;(Maximum 8.0bar);Pulp pressure is minimum:1.2bar;Pressure difference:0.2-0.6bar,
Bed drain purge:15~20% .
6, head box control parameter:J/W(Jet-wire ratio)Control is at 65 meters or less.Head box opening degree of slice lip controls 7.2-
7.5mm;
7, wet end control parameter:Concentration of surfing the Internet control is in 0.8-1.5%;
8, press section of a paper machine parameter:Felt tension:4.5KN/m;One linear load:80±20KN/m;Two pressure area line pressures
Power:110±20KN/m;Three linear loads:1100±20KN/m;Four linear loads: 45±10KN/m
9, front baking control parameter:The total Steam pressure control of front baking is in 80-150KPa;
10, surface table glue machine:2.0-4.0% is controlled into sizing applicator moisture;Total resin added control is in 2.0-4.0GSM;
11, control parameter is dried afterwards:After dry total Steam pressure control in 20-80KPa;
12, cooling cylinder control parameter:Cooling cylinder surface temperature control is in 45-65 degree;
13, hard press polish control parameter:Press polish line pressure is controlled in 40-60KN/m;
14, coiling coater parameter:Batch sheet density maximum:600-700kg/m3;Batch untouched edge width:6600-
6660mm:Batch diameter:4000-4500mm;Moisture control is batched 6.0 ± 1.0%.
Claims (1)
1. a kind of preparation method of lower shrinkage secondary stock neutral sizing, it is characterised in that include the following steps:
(1)Raw material is the high whiteness high-cleanness, high Deinking Pulp that Mixed Office WasteMOW is produced;Mixed Office WasteMOW raw material line adapted
30%37# U.S.s are useless, 20% Japan's 3# waste paper and 50% state give up high-quality little Hua and great Hua;
(2)Paper machine is manufactured paper with pulp wet end furnish:15% sulphate chemical bleaching mixing wood pulp, 75% deinking of MOW slurry and 10%
Waste stuff;Wherein, the sulphate chemical bleaching mixing wood pulp is the long fine wood pulp of 50% sulphate chemical bleaching and 50% chemistry drift
The mixing of white thermomechanical wood pulp;
(3)Paper machine pulping method:Screen cloth jet-wire ratio is less than 65 meters, in production process product moisture norm controlling 5.0 ±
0.5%。
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CN201510660143.XA CN105239442B (en) | 2015-10-14 | 2015-10-14 | A kind of preparation method of lower shrinkage secondary stock neutral sizing |
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CN201510660143.XA CN105239442B (en) | 2015-10-14 | 2015-10-14 | A kind of preparation method of lower shrinkage secondary stock neutral sizing |
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CN105239442A CN105239442A (en) | 2016-01-13 |
CN105239442B true CN105239442B (en) | 2018-07-31 |
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CN110656539B (en) * | 2018-06-29 | 2021-12-10 | 玖龙纸业(东莞)有限公司 | Glasin base paper, and production method and production system thereof |
CN113481758A (en) * | 2021-07-23 | 2021-10-08 | 广州造纸股份有限公司 | Environment-friendly wall-mounted foam board release base paper and preparation method thereof |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
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US5580422A (en) * | 1993-07-27 | 1996-12-03 | Hoechst Celanese Corporation | Brightening color dyed wastepaper with a bleaching agent and a quaternary compound |
CN1276151C (en) * | 2004-05-28 | 2006-09-20 | 岳阳纸业股份有限公司 | Special pigment finishing offset paper and producing method thereof |
EP2157237B1 (en) * | 2007-03-30 | 2014-11-05 | Nippon Paper Industries Co., Ltd. | Methods for producing coating base papers and coated papers |
CN101565913A (en) * | 2009-05-08 | 2009-10-28 | 东莞玖龙纸业有限公司 | Method for producing corrugated paper with ultralow gram weight and high strength |
CN101994276A (en) * | 2009-08-13 | 2011-03-30 | 上海嘉龙纸业有限公司 | Method for preparing higher-quality paper from waste compound paper source recycled paper pulp |
CN101638861B (en) * | 2009-08-16 | 2012-07-18 | 岳阳林纸股份有限公司 | Manufacturing method of industrial film coated base paper |
CN101851873B (en) * | 2010-06-23 | 2013-04-17 | 岳阳林纸股份有限公司 | Manufacturing method of environment-friendly copying paper |
CN102828437A (en) * | 2012-09-03 | 2012-12-19 | 浙江仙鹤特种纸有限公司 | Method for producing ultrathin release raw paper |
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Address after: 523132 Mayong Town, Dongguan City, Guangdong Province, Ma II Village Patentee after: NINE DRAGONS PAPER INDUSTRIES (DONGGUAN) Co.,Ltd. Address before: Guangdong province Dongguan City Machong town Xinsha Port Industrial Zone Patentee before: DONGGUAN NINE DRAGONS PAPER INDUSTRIES Co.,Ltd. |
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