CN107268315A - A kind of pulping and paper-making new method using Chinese alpine rush as raw material - Google Patents
A kind of pulping and paper-making new method using Chinese alpine rush as raw material Download PDFInfo
- Publication number
- CN107268315A CN107268315A CN201710670550.8A CN201710670550A CN107268315A CN 107268315 A CN107268315 A CN 107268315A CN 201710670550 A CN201710670550 A CN 201710670550A CN 107268315 A CN107268315 A CN 107268315A
- Authority
- CN
- China
- Prior art keywords
- paper
- pulp
- alpine rush
- chinese alpine
- raw material
- 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.)
- Granted
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C7/00—Digesters
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C11/00—Regeneration of pulp liquors or effluent waste waters
- D21C11/0021—Introduction of various effluents, e.g. waste waters, into the pulping, recovery and regeneration cycle (closed-cycle)
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/12—Bleaching ; Apparatus therefor with halogens or halogen-containing compounds
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Paper (AREA)
Abstract
The invention discloses a kind of pulping and paper-making new method using Chinese alpine rush as raw material, including cooking section, black liquid extraction workshop section, washing and sieving workshop section, bleachery and papermaking workshop section, the present invention eliminates traditional material papering section, in the absence of dust and flying chip in melting process etc. due to using Chinese alpine rush for raw material, and Chinese alpine rush silicon content is low, only the half of wheat straw, dragon grass fiber length and it is thin, slurry yield is up to 50%, higher than 40% or so of wheat straw, high-grade, the extraordinary cultural paper of high added value can be produced；Paper pulp drainability prepared by the present invention is good, and after being extracted through the series connection of twice Double screw pulp extruder, extraction rate of black liquor is up to more than 85%, far above the 75~80% of Straw Pulp；The chemicals usage of the present invention is few, and alkali charge is significantly lower than the alkali number forever of Straw Pulp, and pollutant yield is also lower than wheat straw by 30~40%, can substantially reduce production cost and treatment of wastes produced cost, strengthens the competitiveness of enterprise.
Description
Technical field：
The present invention relates to a kind of pulp and paper making method, more particularly to a kind of pulping and paper-making new method using Chinese alpine rush as raw material,
Belong to paper industry technical field.
Background technology：
Due to corporate strategy development need and changes in market demand, local resources is made full use of, product specification is improved and enterprise is competing
Power is striven, is the developing direction of each enterprise.Raw material employed in traditional paper technology is wheat straw, and ryegrass pulping is present
Rate is low, and melting process produces a large amount of dusts, flying chip and wheat bran, and pollutant yield is big, and black liquor silicon content is high, and heteroproteose cell is more,
Not disposable, the cultural paper of production is difficult to reach higher gears time, and added value of product is relatively low.
The content of the invention：
The technical problems to be solved by the invention are：Overcoming the deficiencies in the prior art, there is provided a kind of system using Chinese alpine rush as raw material
Papermaking new method is starched, the cultural paper of production can reach higher gears time, and added value of product is higher.
The present invention is for the technical solution adopted for solving the technical problem：
A kind of pulping and paper-making new method using Chinese alpine rush as raw material, its concrete operation step is as follows：
(1) cooking section：
1. cooking liquor is prepared：Industrial solid caustic soda is taken, is calculated with weight ratio meter, caustic soda：Industrial water=（4~5）：（75~85）, stir
Mix it is uniform after cooking liquor A, it is standby；
2. after the removal of impurities of raw material Chinese alpine rush, boil house is transported to careless car is grabbed by Chinese alpine rush, Chinese alpine rush is hung to steam port by loop wheel machine,
Load together with the cooking liquor A prepared and boiling is carried out in rotary spherical digester, Chinese alpine rush and cooking liquor A weight ratio are（2~3）：（7~9）,
Temperature is between 130~150 DEG C, pressure is between 0.5~0.6Mpa, digestion time 2.5~3.5 hours in rotary spherical digester；
(2) black liquid extraction workshop section：
Thick slurry after boiling sprays into jetting storehouse, is composed in series by two Double screw pulp extruders and a horizontal belt vacuum pulp washing machine
Extraction equipment carry out countercurrent washing, after the thin phenol water of extraction is all filtered through black liquor filter, be transported to black liquor and development as resource sharp
Workshop Production lignin product is used, the coarse slurry pump after extraction delivers to washing and sieving workshop section；
(3) washing and sieving workshop section：
After thick slurry after black liquid extraction screens out thick slag and impurity through vanning and CX screen centrifuges after elder generation of this workshop section, then through cylinder
Concentrate B is obtained after thickener concentration；
(4) bleachery：
1. the preparation of calcium hypochlorite bleaching liquid：Reacted using liquid chlorine and lime and generate the principle of calcium hypochlorite to make time chlorine by oneself
Sour calcium bleaching liquid C；
2. bleaching stage：Concentrate B and calcium hypochlorite bleaching liquid C is pressed 1:After 1 ratio is well mixed, bleached pulp E is obtained, it is described
Bleached pulp E through horizontal belt vacuum pulp washing machine wash after paper pulp F, paper pulp F is put into standby in reserve pit；
(5) papermaking workshop section：
Paper pulp F is through sizing mixing, removal of impurities, copy paper, after drying, being cut into feeding paper cutter needs specification, packaging and warehousing.
The preparation technology of described calcium hypochlorite bleaching liquid comprises the following steps：
(1) lime stone and anthracite are pressed 1：0.12 weight proportion, which is added in limekiln, to be calcined, temperature control 800~
1200 DEG C, the lime of generation is interrupted from kiln bottom is discharged, and added water digestion, obtains the calcium hydroxide containing a small amount of free water；
(2), by the particulate calcium hydroxide containing 3~6% free moistures, added through the auger under niter ash silo from the top layer of chlorination tower, liquid
Chlorine enters from chlorination tower bottom, and calcium hypochlorite bleaching liquid finished product is discharged by chlorination tower bottom, and chemical equation is：2Ca(OH)2+
2Cl2→Ca(ClO)2+CaCl2+2H2O 。
The positive beneficial effect of the present invention is as follows：
1st, the present invention eliminates traditional material papering section, in the absence of the dust in melting process due to using Chinese alpine rush for raw material
With flying chip etc., and Chinese alpine rush silicon content is low, only the half of wheat straw, dragon grass fiber length and it is thin, slurry yield is higher than up to 50%
40% or so of wheat straw, these are the necessary conditions of premise for preparing top grade paper.
2nd, the paper pulp drainability prepared by the present invention is good, after being extracted through the series connection of twice Double screw pulp extruder, extraction rate of black liquor
Up to more than 85%, far above the 75~80% of Straw Pulp, black liquor solid content is 8~10%, and black liquid wave hairdressing is 6Be0 left
It is right.
3rd, chemicals usage of the invention is few, and alkali charge is the alkali number forever significantly lower than Straw Pulp, pollutant yield
It is lower than wheat straw by 30~40%, it can substantially reduce production cost and treatment of wastes produced cost.
4th, the present invention can produce high-grade, the extraordinary cultural paper of high added value, hence it is evident that enhancing enterprise competitiveness.
Embodiment:
The present invention is made further explanation and description with reference to specific embodiment：
A kind of pulping and paper-making new method using Chinese alpine rush as raw material, its concrete operation step is as follows：
(1) cooking section：
1. cooking liquor is prepared：Industrial solid caustic soda is taken, is calculated with weight ratio meter, caustic soda：Industrial water=（4~5）：（75~85）, stir
Mix it is uniform after cooking liquor A, it is standby；
2. after the removal of impurities of raw material Chinese alpine rush, boil house is transported to careless car is grabbed by Chinese alpine rush, Chinese alpine rush is hung to steam port by loop wheel machine,
Load together with the cooking liquor A prepared and boiling is carried out in rotary spherical digester, Chinese alpine rush and cooking liquor A weight ratio are（2~3）：（7~9）,
Temperature is between 130~150 DEG C, pressure is between 0.5~0.6Mpa, digestion time 2.5~3.5 hours in rotary spherical digester；
(2) black liquid extraction workshop section：
Thick slurry after boiling sprays into jetting storehouse, is composed in series by two Double screw pulp extruders and a horizontal belt vacuum pulp washing machine
Extraction equipment carry out countercurrent washing, after the thin phenol water of extraction is all filtered through black liquor filter, be transported to black liquor and development as resource sharp
Workshop Production lignin product is used, the coarse slurry pump after extraction delivers to washing and sieving workshop section；
(3) washing and sieving workshop section：
After thick slurry after black liquid extraction screens out thick slag and impurity through vanning and CX screen centrifuges after elder generation of this workshop section, then through cylinder
Concentrate B is obtained after thickener concentration；
(4) bleachery：
1. the preparation of calcium hypochlorite bleaching liquid：Reacted using liquid chlorine and lime and generate the principle of calcium hypochlorite to make time chlorine by oneself
Sour calcium bleaching liquid C；
2. bleaching stage：Concentrate B and calcium hypochlorite bleaching liquid C is pressed 1:After 1 ratio is well mixed, bleached pulp E is obtained, it is described
Bleached pulp E through horizontal belt vacuum pulp washing machine wash after paper pulp F, paper pulp F is put into standby in reserve pit；
(5) papermaking workshop section：
Paper pulp F is through sizing mixing, removal of impurities, copy paper, after drying, being cut into feeding paper cutter needs specification, packaging and warehousing.
The preparation technology of described calcium hypochlorite bleaching liquid comprises the following steps：
(1) lime stone and anthracite are pressed 1：0.12 weight proportion, which is added in limekiln, to be calcined, temperature control 800~
1200 DEG C, the lime of generation is interrupted from kiln bottom is discharged, and added water digestion, obtains the calcium hydroxide containing a small amount of free water；
(2), by the particulate calcium hydroxide containing 3~6% free moistures, added through the auger under niter ash silo from the top layer of chlorination tower, liquid
Chlorine enters from chlorination tower bottom, and calcium hypochlorite bleaching liquid finished product is discharged by chlorination tower bottom, and chemical equation is：2Ca(OH)2+
2Cl2→Ca(ClO)2+CaCl2+2H2O 。
The present invention eliminates traditional material papering section, in the absence of the ash in melting process due to using Chinese alpine rush for raw material
Dirt and flying chip etc., and Chinese alpine rush silicon content is low, the only half of wheat straw, dragon grass fiber length and it is thin, slurry yield is high up to 50%
In 40% or so of wheat straw, high-grade, the extraordinary cultural paper of high added value can be produced, hence it is evident that enhancing enterprise competitiveness.
Claims (2)
1. a kind of pulping and paper-making new method using Chinese alpine rush as raw material, its concrete operation step is as follows：
(1) cooking section：
1. cooking liquor is prepared：Industrial solid caustic soda is taken, is calculated with weight ratio meter, caustic soda：Industrial water=（4~5）：（75~85）, stir
Mix it is uniform after cooking liquor A, it is standby；
2. after the removal of impurities of raw material Chinese alpine rush, boil house is transported to careless car is grabbed by Chinese alpine rush, Chinese alpine rush is hung to steam port by loop wheel machine,
Load together with the cooking liquor A prepared and boiling is carried out in rotary spherical digester, Chinese alpine rush and cooking liquor A weight ratio are（2~3）：（7~9）,
Temperature is between 130~150 DEG C, pressure is between 0.5~0.6Mpa, digestion time 2.5~3.5 hours in rotary spherical digester；
(2) black liquid extraction workshop section：
Thick slurry after boiling sprays into jetting storehouse, is composed in series by two Double screw pulp extruders and a horizontal belt vacuum pulp washing machine
Extraction equipment carry out countercurrent washing, after the thin phenol water of extraction is all filtered through black liquor filter, be transported to black liquor and development as resource sharp
Workshop Production lignin product is used, the coarse slurry pump after extraction delivers to washing and sieving workshop section；
(3) washing and sieving workshop section：
After thick slurry after black liquid extraction screens out thick slag and impurity through vanning and CX screen centrifuges after elder generation of this workshop section, then through cylinder
Concentrate B is obtained after thickener concentration；
(4) bleachery：
1. the preparation of calcium hypochlorite bleaching liquid：Reacted using liquid chlorine and lime and generate the principle of calcium hypochlorite to make time chlorine by oneself
Sour calcium bleaching liquid C；
2. bleaching stage：Concentrate B and calcium hypochlorite bleaching liquid C is pressed 1:After 1 ratio is well mixed, bleached pulp E is obtained, it is described
Bleached pulp E through horizontal belt vacuum pulp washing machine wash after paper pulp F, paper pulp F is put into standby in reserve pit；
(5) papermaking workshop section：
Paper pulp F is through sizing mixing, removal of impurities, copy paper, after drying, being cut into feeding paper cutter needs specification, packaging and warehousing.
2. a kind of pulping and paper-making new method using Chinese alpine rush as raw material according to claim 1, it is characterised in that：Described
The preparation technology of calcium hypochlorite bleaching liquid comprises the following steps：
(1) lime stone and anthracite are pressed 1：0.12 weight proportion, which is added in limekiln, to be calcined, temperature control 800~
1200 DEG C, the lime of generation is interrupted from kiln bottom is discharged, and added water digestion, obtains the calcium hydroxide containing a small amount of free water；
(2), by the particulate calcium hydroxide containing 3~6% free moistures, added through the auger under niter ash silo from the top layer of chlorination tower, liquid
Chlorine enters from chlorination tower bottom, and calcium hypochlorite bleaching liquid finished product is discharged by chlorination tower bottom, and chemical equation is：2Ca(OH)2+
2Cl2→Ca(ClO)2+CaCl2+2H2O 。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710670550.8A CN107268315B (en) | 2017-08-08 | 2017-08-08 | It is a kind of using Chinese alpine rush as the pulp and paper making method of raw material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710670550.8A CN107268315B (en) | 2017-08-08 | 2017-08-08 | It is a kind of using Chinese alpine rush as the pulp and paper making method of raw material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107268315A true CN107268315A (en) | 2017-10-20 |
| CN107268315B CN107268315B (en) | 2019-10-25 |
Family
ID=60077081
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710670550.8A Expired - Fee Related CN107268315B (en) | 2017-08-08 | 2017-08-08 | It is a kind of using Chinese alpine rush as the pulp and paper making method of raw material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107268315B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0336842A1 (en) * | 1988-04-06 | 1989-10-11 | Clextral | Process for producing a paper pulp for fiduciary use |
| CN1648335A (en) * | 2005-03-04 | 2005-08-03 | 蒋浩 | Method for treating and reusing pulp bleaching waste water in size washing |
| CN101748631A (en) * | 2009-12-18 | 2010-06-23 | 华南理工大学 | Efficient and clean puling and bleaching method dissolving alpha-pulp by Chinese alpine rush |
| CN102400404A (en) * | 2011-12-09 | 2012-04-04 | 昆明理工大学 | Straw cutting-free method for preparing straw pulp by spherical digester alkali digestion |
| CN104611966A (en) * | 2014-12-04 | 2015-05-13 | 山东源根石油化工有限公司 | Novel pulping process with Chinese alpine rush as raw material |
| CN105178083A (en) * | 2014-06-08 | 2015-12-23 | 蒋寿悟 | Pulping method with zero discharge of sewage |
-
2017
- 2017-08-08 CN CN201710670550.8A patent/CN107268315B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0336842A1 (en) * | 1988-04-06 | 1989-10-11 | Clextral | Process for producing a paper pulp for fiduciary use |
| CN1648335A (en) * | 2005-03-04 | 2005-08-03 | 蒋浩 | Method for treating and reusing pulp bleaching waste water in size washing |
| CN101748631A (en) * | 2009-12-18 | 2010-06-23 | 华南理工大学 | Efficient and clean puling and bleaching method dissolving alpha-pulp by Chinese alpine rush |
| CN102400404A (en) * | 2011-12-09 | 2012-04-04 | 昆明理工大学 | Straw cutting-free method for preparing straw pulp by spherical digester alkali digestion |
| CN105178083A (en) * | 2014-06-08 | 2015-12-23 | 蒋寿悟 | Pulping method with zero discharge of sewage |
| CN104611966A (en) * | 2014-12-04 | 2015-05-13 | 山东源根石油化工有限公司 | Novel pulping process with Chinese alpine rush as raw material |
Non-Patent Citations (1)
| Title |
|---|
| 四川省青城造纸厂: "亚铵法龙须草制82度以上漂白浆的研究", 《四川造纸》 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107268315B (en) | 2019-10-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105780568B (en) | Biological enzyme bating delignification combines mechanical legal system sizing process twice | |
| CN104790241B (en) | A kind of clean method for preparing of high-purity high-quality bamboo wood dissolving pulp | |
| CN105568726B (en) | A kind of double pH value chemical mechanical pulp-making methods of wet strong waste paper recycling | |
| CN102587181B (en) | Environment-friendly clean pulping process | |
| CN101844885A (en) | Method for manufacturing regenerative gypsum powder by waste gypsum models | |
| CN102587178A (en) | Pulp preparing method for increasing bagasse oxygen-alkali cooking effect | |
| CN100586556C (en) | Technique for producing active clay | |
| CN111395026A (en) | Production method of high-viscosity cotton pulp | |
| CN108589374A (en) | A kind of paper pulp manufacturing technique | |
| CN103821030A (en) | Presoak for papermaking and preparation method thereof, and paper industrial packaging production process | |
| CN103061180B (en) | Short rayon fiber Wesy reed pulp dregs of rice preparation method | |
| CN107268315B (en) | It is a kind of using Chinese alpine rush as the pulp and paper making method of raw material | |
| CN103319098B (en) | A kind of method utilizing pulping and paper-making white clay to produce glass fibre | |
| CN101838943B (en) | Knot energy-saving environment-friendly pulping method and equipment | |
| CN107875884A (en) | A kind of dilution device of straw pulp making material | |
| CN105753001B (en) | A kind of method for carrying out washing dealkalize to fiber fabricated in situ calcium silicates | |
| CN113969512B (en) | Full straw papermaking pulp and preparation method and application thereof | |
| CN101235607B (en) | Method for producing natural antibacterial bamboo fiber | |
| CN102677500B (en) | A kind of material preparation technology being applicable to pulp by modifying true color unbleached and preparing dissolving pulp | |
| CN1228503C (en) | Technological system for producing environment protection type paper pulp | |
| CN102454133B (en) | Pulping agent and application and production method thereof | |
| CN100497810C (en) | Pulp and paper making method by continuously boiling hollow palm fruit string fiber | |
| CN102517971B (en) | A kind of preparation method of wheat straw reed mixing slurry | |
| CN101545226B (en) | Method for improving bagasse alkaline cooking effect through wet process with CEH bleaching waste liquor | |
| CN102644211B (en) | Preparation method of industrial hemp full stalk bleaching chemical pulp |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191025 Termination date: 20200808 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |