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 PDF

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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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Expired - Fee Related
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CN201510660143.XA
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Chinese (zh)
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CN105239442A (en
Inventor
刘名中
刘晋嵩
颜利兵
林新阳
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Dongguan Nine Dragons Paper Co Ltd
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Dongguan Nine Dragons Paper Co Ltd
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Priority to CN201510660143.XA priority Critical patent/CN105239442B/en
Publication of CN105239442A publication Critical patent/CN105239442A/en
Application granted granted Critical
Publication of CN105239442B publication Critical patent/CN105239442B/en
Expired - Fee Related legal-status Critical Current
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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

A kind of preparation method of lower shrinkage secondary stock neutral sizing
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%。
CN201510660143.XA 2015-10-14 2015-10-14 A kind of preparation method of lower shrinkage secondary stock neutral sizing Expired - Fee Related CN105239442B (en)

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CN105239442A CN105239442A (en) 2016-01-13
CN105239442B true CN105239442B (en) 2018-07-31

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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)

* Cited by examiner, † Cited by third party
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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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Granted publication date: 20180731

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