CN103103842A - Pulping method for waste Renminbi - Google Patents

Pulping method for waste Renminbi Download PDF

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Publication number
CN103103842A
CN103103842A CN2012105404110A CN201210540411A CN103103842A CN 103103842 A CN103103842 A CN 103103842A CN 2012105404110 A CN2012105404110 A CN 2012105404110A CN 201210540411 A CN201210540411 A CN 201210540411A CN 103103842 A CN103103842 A CN 103103842A
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China
Prior art keywords
waste
renminbi
stewing
pulping method
temperature
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CN2012105404110A
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Chinese (zh)
Inventor
张军
张永峰
李清阳
裴刚
段成兵
董学荣
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MCC Meili Paper Industry Co Ltd
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MCC Meili Paper Industry Co Ltd
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Filing date
Publication date
Application filed by MCC Meili Paper Industry Co Ltd filed Critical MCC Meili Paper Industry Co Ltd
Priority to CN2012105404110A priority Critical patent/CN103103842A/en
Publication of CN103103842A publication Critical patent/CN103103842A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

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Abstract

The invention relates to a pulping method for waste Renminbi. The method adopts a caustic soda-anthraquinone pulping method. The process comprises stewing and bleaching, wherein alkali charge is controlled between 18% to 20% in the stewing, liquor ratio is 1:3.5-4.5, the stewing liquor temperature is 80 DEG C to 85 DEG C, and before the temperature rises, idling for 30 min, then rising temperature, and rising the temperature according to the temperature rising time and vapor pressure. By the adoption of the caustic soda-anthraquinone pulping method, the waste Renminbi is carried out by pulping, and the waste Renminbi can be fully resolved through controlling the stewing parameters, so that the pulping method for the waste Renminbi can be effectively used in papermaking system. Evenness of pulp got and full stuff efficiency are high, stewing quality is stable, and meanwhile usage amount of chemical materials is small and various energy consumptions are low, process investment is small, and the cost is low. The pulping method for the waste Renminbi achieves the recycle of waste resource, and meanwhile provides a novel pulp to the paper technology. The pulp of the process can be used for manufacturing specialty paper, and the pulping method for the waste Renminbi has a certain promotional value.

Description

A kind of waste and old RMB pulping process
Technical field
The present invention relates to the pulping technology for paper-making field, particularly relate to a kind of pulping process of waste and old RMB.
Background technology
In prior art, waste and old RMB uses after mostly adopting the machinery making beating, obtains in this way pulp fiber and is difficult to discongest, and contains a large amount of fibre bundles, causes the paper smoothness low, and sand holes are many, can not utilize well.
Summary of the invention
The object of the invention is to overcome the defective of above-mentioned prior art, providing a kind of can fully decompose waste and old RMB, effectively uses the waste and old RMB pulping process of copying in paper system.
The technical scheme of taking for achieving the above object is:
A kind of waste and old RMB pulping process is characterized in that adopting caustic soda-anthraquinone pulp-making method, and its technique comprises boiling and bleaching process, and wherein boiling parameter is:
1) alkali charge 18-20%,
2) liquor ratio 1: 3.5-4.5,
3) cooking liquor temperature 80-85 ℃,
4) boiling curve: after first dallying 30 minutes before heating up, can heat up, be warming up to rapidly 0.65MPa in 90 minutes, spurt after then being incubated 60 minutes.
Described bleaching process parameter is:
1) bleaching temperature is 35 ℃
2) bleaching time is 4 hours,
3) bleaching slurry concentration 4-5%,
4) bleached pulp whiteness 65-68% (blue light method mensuration),
5) bleached pulp fiber wet weight 4-5g.
Technical characterstic of the present invention be embodied in following some:
1) alkali charge is low, and liquor ratio is little.
2) pulping evenness obviously improves, and yield is high, and unscreened yield can reach 40-45%.
3) effectively digestion time is 3-3.5 hour.
The present invention adopts soda-aq cooking to carry out slurrying to waste and old RMB and processes, waste and old RMB fully can be decomposed by controlling the boiling parameter, copy paper system thereby effectively apply to, gained slurry evenness and pulping rate are high, cooking quality is stable, chemical materials use amount and every energy consumption are lower simultaneously, and technology investment is few, and cost is low.The present invention has realized the recycling of waste and old resource, and simultaneously also for paper technology provides new slurry kind, this process slurry can with the manufacturing paper with pulp of speciality paper, have certain promotional value.
The specific embodiment
The present invention adopts soda anthraquinone process take useless RMB as raw material, and selecting equipment is rotary spherical digester.Boiling and bleaching process parameter such as following table in the method:
Figure BDA00002585513700021
During the cooking liquor configuration
1, according to using boiling alkali charge, liquor ratio, formulation cooking liquor concentration and volume.
2, determine concentration and volume after, use white liquid and the outsourcing caustic soda of alkali remanufacture to press, ratio is that 7:3 prepares.
3, the cooking liquor temperature must be heated to 80-85 ℃.
4, the cooking liquor that configures is feeded after adding spiral Presoaker and waste and old RMB uniform stirring.
5, after intensification must be dallied before, can heat up, heat up rapidly according to heating-up time, vapour pressure.
6, through after bleaching, the bleached pulp whiteness 65-68% of acquisition (blue light method mensuration), bleached pulp fiber wet weight 4-5g.

Claims (2)

1. a waste and old RMB pulping process, is characterized in that adopting caustic soda-anthraquinone pulp-making method, and its technique comprises boiling and bleaching, and wherein boiling parameter is:
1) alkali charge 18-20%,
2) liquor ratio 1:3.5-4.5,
3) cooking liquor temperature 80-85 ℃,
4) boiling curve: after first dallying 30 minutes before heating up, can heat up, be warming up to rapidly 0.65MPa in 90 minutes, spurt after then being incubated 60 minutes.
2. according to waste and old RMB pulping process claimed in claim 1, it is characterized in that described bleaching process parameter is:
1) bleaching temperature is 35 ℃
2) bleaching time is 4 hours,
3) bleaching slurry concentration 4-5%,
4) bleached pulp whiteness 65-68%,
5) bleached pulp fiber wet weight 4-5g.
CN2012105404110A 2012-12-14 2012-12-14 Pulping method for waste Renminbi Pending CN103103842A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012105404110A CN103103842A (en) 2012-12-14 2012-12-14 Pulping method for waste Renminbi

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012105404110A CN103103842A (en) 2012-12-14 2012-12-14 Pulping method for waste Renminbi

Publications (1)

Publication Number Publication Date
CN103103842A true CN103103842A (en) 2013-05-15

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Country Status (1)

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CN (1) CN103103842A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103726375A (en) * 2013-12-30 2014-04-16 中冶美利纸业股份有限公司 Sulfite pulping process of salix mongolica
CN103726376A (en) * 2013-12-30 2014-04-16 中冶美利纸业股份有限公司 Intermittent low-temperature quick pulping process for broad-leaf wood
CN104775316A (en) * 2015-04-22 2015-07-15 河北大发纸业有限公司 Method for pulping and papermaking by use of damaged Ren Min Bi destroyed waste materials

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87103946A (en) * 1987-05-28 1988-05-25 西北轻工业学院 Use producing cardboard from flax stem for leather boxes
AU2002301062A1 (en) * 2001-09-19 2003-06-12 International Paper Company Novel pulping method to improve the quality of recycled fibers
CN101302725A (en) * 2008-06-10 2008-11-12 山东银鹰化纤有限公司 Process for producing cotton dissolving pulp
CN101760989A (en) * 2008-11-28 2010-06-30 山东福荫造纸环保科技有限公司 Mixed pulp with high opacity, air permeability and tearing index and cultural paper prepared from the same
CN101967764A (en) * 2010-11-05 2011-02-09 安徽雪龙纤维科技股份有限公司 High-whiteness cotton pulp product for banknote paper and production method thereof
CN102174757A (en) * 2011-01-19 2011-09-07 山东银鹰股份有限公司 Preparation method of cotton pulp for high-strength paper
CN102174752A (en) * 2011-01-19 2011-09-07 山东银鹰股份有限公司 Preparation method of wood pulp for fibranne
CN102191707A (en) * 2010-12-30 2011-09-21 中冶美利纸业股份有限公司 Low temperature rapid pulping process of reed
CN102505547A (en) * 2011-10-24 2012-06-20 安徽雪龙纤维科技股份有限公司 Cotton pulp with high polymerization degree and production method for cotton pulp
CN102517971A (en) * 2011-12-19 2012-06-27 中冶美利纸业股份有限公司 Preparation method for mixed pulp of wheat straw and reed

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN87103946A (en) * 1987-05-28 1988-05-25 西北轻工业学院 Use producing cardboard from flax stem for leather boxes
AU2002301062A1 (en) * 2001-09-19 2003-06-12 International Paper Company Novel pulping method to improve the quality of recycled fibers
CN101302725A (en) * 2008-06-10 2008-11-12 山东银鹰化纤有限公司 Process for producing cotton dissolving pulp
CN101760989A (en) * 2008-11-28 2010-06-30 山东福荫造纸环保科技有限公司 Mixed pulp with high opacity, air permeability and tearing index and cultural paper prepared from the same
CN101967764A (en) * 2010-11-05 2011-02-09 安徽雪龙纤维科技股份有限公司 High-whiteness cotton pulp product for banknote paper and production method thereof
CN102191707A (en) * 2010-12-30 2011-09-21 中冶美利纸业股份有限公司 Low temperature rapid pulping process of reed
CN102174757A (en) * 2011-01-19 2011-09-07 山东银鹰股份有限公司 Preparation method of cotton pulp for high-strength paper
CN102174752A (en) * 2011-01-19 2011-09-07 山东银鹰股份有限公司 Preparation method of wood pulp for fibranne
CN102505547A (en) * 2011-10-24 2012-06-20 安徽雪龙纤维科技股份有限公司 Cotton pulp with high polymerization degree and production method for cotton pulp
CN102517971A (en) * 2011-12-19 2012-06-27 中冶美利纸业股份有限公司 Preparation method for mixed pulp of wheat straw and reed

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103726375A (en) * 2013-12-30 2014-04-16 中冶美利纸业股份有限公司 Sulfite pulping process of salix mongolica
CN103726376A (en) * 2013-12-30 2014-04-16 中冶美利纸业股份有限公司 Intermittent low-temperature quick pulping process for broad-leaf wood
CN104775316A (en) * 2015-04-22 2015-07-15 河北大发纸业有限公司 Method for pulping and papermaking by use of damaged Ren Min Bi destroyed waste materials

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Application publication date: 20130515