CN1201046C - Middle-or low-pressure exposion method for making pulp with broad-leaf wood - Google Patents

Middle-or low-pressure exposion method for making pulp with broad-leaf wood Download PDF

Info

Publication number
CN1201046C
CN1201046C CN 02115318 CN02115318A CN1201046C CN 1201046 C CN1201046 C CN 1201046C CN 02115318 CN02115318 CN 02115318 CN 02115318 A CN02115318 A CN 02115318A CN 1201046 C CN1201046 C CN 1201046C
Authority
CN
China
Prior art keywords
sodium
raw material
broadleaf
pressure
pulp
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.)
Expired - Fee Related
Application number
CN 02115318
Other languages
Chinese (zh)
Other versions
CN1397683A (en
Inventor
胡键
黄干强
詹怀宇
郑炽嵩
刘焕彬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Jinboyuan Investment Consulting Co Ltd
South China University of Technology SCUT
Original Assignee
Beijing Jinboyuan Investment Consulting Co Ltd
South China University of Technology SCUT
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beijing Jinboyuan Investment Consulting Co Ltd, South China University of Technology SCUT filed Critical Beijing Jinboyuan Investment Consulting Co Ltd
Priority to CN 02115318 priority Critical patent/CN1201046C/en
Publication of CN1397683A publication Critical patent/CN1397683A/en
Application granted granted Critical
Publication of CN1201046C publication Critical patent/CN1201046C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Paper (AREA)

Abstract

The present invention relates to a broadleaf pulp manufacture method by a middle pressure and low pressure explosion method. The present invention has the steps of raw material preprocessing (medicine with the dosage (the dosage of the medicine is corresponding to the bone dry weight of broadleaf raw materials) of 1 to 6% of alkali, 1 to 16% of sodium-sulfur compound and 0 to 1% of auxiliary agents is added in the broadleaf raw materials and are stirred for 0 to 24 hours under room temperature to 90 DEG C), high temperature and high pressure processing (the preprocessed materials are put in an explosion can to be processed for 3 to 15 minutes under the temperature of 140 to 220 DEG C and the pressure of 0.8mpa to 2.28mpa) and ejection (the raw materials are instantly blasted and ejected to a reception container). Broadleaf blasting paper pulp of the present invention has the advantages of high maintenance intensity, high yield, low energy consumption, high whiteness, good bleaching performance and high toughness. The broadleaf blasting pulp can be used for manufacturing medium high paper.

Description

Leaf wood mesolow Demolition Pulping method
Technical field
The present invention relates to the pulping technique of field of papermaking, in more detail leaf wood mesolow Demolition Pulping method.
Background technology
Because greening and wood raw material scarcity, China has planted a large amount of Eucalyptus, the living leaf wood of poplar constant speed respectively in the south and the north.Along with development of the West Regions, will plant the living leaf wood of more speed in the west area.These timber are mainly used in the processing glued board at present, and its leftover pieces are basically as fuel.Glued board to the demand of timber also much smaller than the speed of growth of fast growing wood.Although so China's timber resources is generally speaking deficient, a large amount of fast growing woods is suddenly waited to develop.
The leaf wood Demolition Pulping was once becoming the research focus in China, and had proposed various blasting technologies.High pressure blasting procedure for example, because it is improper that process conditions such as burst pressure, preliminary treatment dosage, temperature are grasped, the explosion pulp color and luster of developing is darker, and bleachability is poor, paper fragility is big, so the explosion pulp of producing can only be used to produce building slab, fiberboard or very low-grade paper at present.
Summary of the invention
The object of the present invention is to provide a kind of leaf wood mesolow Demolition Pulping method, make leaf wood explosion paper pulp keep intensity height, yield height, advantage of low energy consumption, and have the whiteness height, bleachability is good, the advantage of good toughness makes the leaf wood explosion pulp can be used to make medium-to-high grade paper.
The living leaf wood density of speed of China's a large amount of cultivations at present is low, and hardness is big, and the molecular weight of cellulose, hemicellulose is less, is subject to destruction in pulping process, causes paper strength to descend, and fragility increases.If preliminary treatment and blasting condition are too violent, in pulping process, generate a large amount of coloring matters, cause whiteness sharply to descend, bleachability descends.
The present invention is especially at the living leaf wood raw material of speed, make the combination that is optimized of pretreating process and blasting condition, the destruction of cellulose and hemicellulose is reduced greatly in blasting process, the reaction that lignin generates coloring matter significantly reduces, thereby make explosion pulp yield height, intensity is good, the whiteness height, bleachability is good, and paper toughness is good.
Leaf wood mesolow Demolition Pulping method of the present invention comprises the steps:
---pretreatment of raw material: the medicine (drug dosage is that relative raw material oven dry weight calculates) that in the leaf wood raw material, adds following consumption:
Alkali 1-6%
Sodium-sulphur compound 1-16%
Auxiliary agent 0-1%
Under normal temperature to 90 ℃ temperature, stirred 0-24 hour;
---mesolow is handled: pretreated material is packed in the cavity charge containers, handled 3-15 minute under 140-220 ℃, 0.8mpa-2.28mpa pressure;
---spurt: raw material moment explosion is spurted to receiving vessel.
Described alkali refers to wherein one or more mixtures of NaOH, sodium carbonate, lime.
Described sodium-sulphur compound refers to wherein one or more mixtures of sodium thiosulfate, dithionate, polysulfide, sodium sulfite, vulcanized sodium.
Described auxiliary agent refers to surface reactive material one or more mixtures wherein of high temperature resistant, the anti-highly basic of nonionic or anionic.
Preferred version of the present invention is as follows:
---pretreatment of raw material: the medicine that in the leaf wood raw material, adds following consumption:
Alkali 1-5%
Sodium-sulphur compound 1-6%
Auxiliary agent 0-0.1%
Drug dosage is that relative raw material oven dry weight calculates, and stirs 2-24 hour under normal temperature to 90 ℃ temperature;
---mesolow is handled: pretreated material is packed in the cavity charge containers, handled 3-15 minute under 210-220 ℃, 0.8mpa-2.20mpa pressure.
The present invention can require to select refining process according to last slurry, but can single hop also multistage defibrination.
The present invention compared with prior art has following advantage:
1, technology of the present invention makes fiber S after the explosion 1Layer segment destroys, S 1And S 2Slabbing is opened, and is easy to expose S like this in defibrination and pulping process 2Layer.Guaranteeing that paper pulp has the yield of high yield pulp, have the intensity of chemical pulp, and have good whiteness and bleachability.
2, process equipment of the present invention is simple, adopts the mesolow explosion, and refining energy consumption is low, the yield height of slurry, and whiteness is higher, and intensity can match in excellence or beauty with chemical pulp, pollutes few.But medium-to-high grade paper cultural papers such as manufactured copper body paper, writing paper, copy paper, high-grade cardboard.
3, technology of the present invention is under the condition that guarantees the high yield of slurry, and refining energy consumption is low, and paper pulp has or near the intensity of chemical pulp, and has higher whiteness and good bleachability.Simultaneously, this operation pressure is little, temperature is low, the processing time is short, dosage is little, so the slurrying cost is low, and technology is simple, and pollutional load is light.But waste water is reuse after simple process.
The specific embodiment
With eucalyptus raw material of thunder woods is example:
---pretreatment of raw material: the medicine (drug dosage is that relative raw material oven dry weight calculates) that in raw material, adds following consumption:
Caustic soda 5%
Inferior sodium 6%
JFC bleeding agent 0.1%
Under 80 ℃ of temperature, stirred 2 hours;
---mesolow is handled: pretreated material is packed in the cavity charge containers, handled 8 minutes under 210 ℃, 2.20mpa pressure;
---spurt: raw material moment explosion is spurted to receiving vessel;
---2 sections defibrinations;
---making beating is to 55 ° of SR.
Obtain pulp brightness 50%, yield 83%, fracture length 6800M, tear index 6.35mN.m 2/ g, burst index 2.58kPa.m 2/ g.

Claims (1)

1, a kind of leaf wood mesolow Demolition Pulping method is characterized in that comprising the steps:
---pretreatment of raw material: the medicine that in the leaf wood raw material, adds following consumption:
Alkali 1-5%
Sodium-sulphur compound 1-6%
Auxiliary agent 0-0.1%
Drug dosage is that relative raw material oven dry weight calculates, and stirs 2-24 hour under normal temperature to 90 ℃ temperature;
---mesolow is handled: pretreated material is packed in the cavity charge containers, handled 3-15 minute under 210-220 ℃, 0.8mpa-2.20mpa pressure;
---spurt: raw material moment explosion is spurted to receiving vessel;
Described alkali refers to wherein one or more mixtures of NaOH, sodium carbonate, lime; Described sodium-sulphur compound refers to wherein one or more mixtures of sodium thiosulfate, dithionate, polysulfide, sodium sulfite, vulcanized sodium; Described auxiliary agent refers to surface reactive material one or more mixtures wherein of high temperature resistant, the anti-highly basic of nonionic or anionic.
CN 02115318 2002-06-03 2002-06-03 Middle-or low-pressure exposion method for making pulp with broad-leaf wood Expired - Fee Related CN1201046C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 02115318 CN1201046C (en) 2002-06-03 2002-06-03 Middle-or low-pressure exposion method for making pulp with broad-leaf wood

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 02115318 CN1201046C (en) 2002-06-03 2002-06-03 Middle-or low-pressure exposion method for making pulp with broad-leaf wood

Publications (2)

Publication Number Publication Date
CN1397683A CN1397683A (en) 2003-02-19
CN1201046C true CN1201046C (en) 2005-05-11

Family

ID=4743577

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 02115318 Expired - Fee Related CN1201046C (en) 2002-06-03 2002-06-03 Middle-or low-pressure exposion method for making pulp with broad-leaf wood

Country Status (1)

Country Link
CN (1) CN1201046C (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107618210A (en) * 2017-09-21 2018-01-23 安吉志达包装厂 A kind of manufacturing process of high-strength corrugated board
CN109537342A (en) * 2018-11-08 2019-03-29 福建省青山纸业股份有限公司 A kind of sulphate pulp processes adding sodium sulfite

Also Published As

Publication number Publication date
CN1397683A (en) 2003-02-19

Similar Documents

Publication Publication Date Title
US10266610B2 (en) Method of processing and fractionating biomass and use of fractions thus obtained
US8092647B2 (en) Method for treating lignocellulosic materials
RU2401352C2 (en) Cellulose mass and method of boiling
CN100390354C (en) Swlfate wood-pulp enzyme-method modifying process
EP0194981B1 (en) A method of manufacturing bleached chemimechanical and semichemical fibre pulp by means of a one-stage impregnation process
JPH08503744A (en) Method for producing viscose pulp
CZ20013627A3 (en) Separation process of biomass containing lignocellulose
EP0442508B1 (en) A process for making graft copolymers from lignin and vinyl monomers
CA1275760C (en) Method of manufacturing bleached chemimechanical and semichemical fibre pulp by means of a two-stage impregnation process
Tozluoğlu et al. Integrated production of biofilm, bioethanol, and papermaking pulp from wheat straw
KR20130096812A (en) Paper with high dry strength containing hemicellulose and producing method thereof
CN1201046C (en) Middle-or low-pressure exposion method for making pulp with broad-leaf wood
Johakimu et al. Hemicellulose Extraction from South African Eucalyptus grandis using Green Liquor and its Impact on Kraft Pulping Efficiency and Paper Making Properties.
CN1284585A (en) Pollution-less low-pressure steam decrepitation process of making straw pulp
US5183535A (en) Process for preparing kraft pulp using black liquor pretreatment reaction
AU639304B2 (en) Process for preparing kraft pulp
CN1043914C (en) Method for reducing thermal and light-induced brightness reversion in lign in-containing pulps
CN1195118C (en) Low pressure herbal material blasting pulp making process
CN1693582A (en) Low pressure blast pulping method in palm fiber
CN1590639A (en) Impregnation pretreatment technology of raw material used in soda process pulp making
Feng et al. Changes in the microstructure and components of Eulaliopsis binata treated by continuous Screw Extrusion Steam Explosion
US11306113B2 (en) Process for the production of cellulose, lignocellulosic sugars, lignosulfonate, and ethanol
CA2466505A1 (en) Microwave pre-treatment of logs for use in making paper and other wood products
Mašura Prehydrolysis of beechwood: Highly purified dissolving pulp produced by sulphur-free pulping
CN1958942A (en) Method of ultrasound in use for producing purified pulp

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20050511

Termination date: 20120603