CN1707019A - Fast enviornment protection cold soaking pulping process with broad-leaved wood material - Google Patents
Fast enviornment protection cold soaking pulping process with broad-leaved wood material Download PDFInfo
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- CN1707019A CN1707019A CN 200510043630 CN200510043630A CN1707019A CN 1707019 A CN1707019 A CN 1707019A CN 200510043630 CN200510043630 CN 200510043630 CN 200510043630 A CN200510043630 A CN 200510043630A CN 1707019 A CN1707019 A CN 1707019A
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Abstract
The present invention provides fast green cold soaking pulping process with broad-leaved wood material. Wooden material is crushed into wooden shreds or bits, which is then produced into paper pulp with whiteness over 75 % through stacking, circular chemical spraying, cold soaking, flushing, milling into pulp, extruding, sieving to eliminate impurity, bleaching and other steps. The technological process has no steaming, complete reuse of water, no sewage exhaust to pollute environment, high paper pulp quality, high paper pulp yield and other features.
Description
1, technical field
The present invention relates to a kind of pulping technology for paper-making, specifically a kind of energy-conservation, water saving, pollution-free fast enviornment protection cold soaking pulping process with broad-leaved wood material.
2, background technology
Papermaking is one of four invents by China, have a long history, at present, the employed raw material of papermaking mainly divides wooden class, grass or undergraduate course plant class, prepared paper pulp divides wood pulp and straw pulp two big classes, no matter wood pulp or straw pulp, the production technology of prior art mainly adopts chemical steaming slurrying or heating slurrying, no matter adopt which kind of production method, all inevitably produce a large amount of waste water in the production process.In order to protect environment, country has to limit the scale of papermaking enterprise, forces many medium and small paper mill closure, suspension, merger and conversion; the result makes that a large amount of papermaking facilities is idle to be scrapped; a large amount of available natural resourcess can not make full use of, and numerous papermaking enterprise workmans go on unemployment, make paper industry move towards low ebb.
3, summary of the invention
In order to solve papermaking severe contamination problem, the invention provides a kind of no boiling drug immersion fast enviornment protection cold soaking pulping process with broad-leaved wood material.This technology need not boiling and only just can replace traditional boiling or heating by the chemicals immersion under normal temperature, normal pressure, can obtain the new technology of high-grade wood pulp.This technology need not heat and consume fuel in process of production, there is not waste water and toxic emission pollution to environment, and have that technology is simple, equipment investment is few, production cost is low, pulp quality is good, white pulp yield reaches 76% with first-class characteristics, for numerous paper-making industries are created more wide survival and development space.
Technical scheme of the present invention realizes in the following manner: wood material is ground into wood wool or wood chip, stacked formula soup circulated sprinkling cold soaking then 3 hours, and then make the high-grade paper pulp that whiteness can reach more than 75% through operations such as flushing, defibrination, shove, screening and removing impurities and bleachings and use for papermaking.
(1) preparation of cooling bath: take by weighing caustic soda 30-60 part respectively, hydrogen peroxide 3-15 part, sodium sulphate 10-30 part, cold soaking auxiliary agent 1.5-9 part, add stir in 1000 parts of water standby;
(2) slurrying step: 1. the wood material section is pulverized; 2. stack with soaking soup normal temperature circulated sprinkling and soaked 2-4 hour, raw material is 1: 3 with soaking liquid proportion; 3. the back raw material is soaked in flushing; 4. send paste mill grinding after the raw material flushing; 5. the slurry behind the defibrination send the press master shove; 6. the slurry behind the shove carries out screening and removing impurities; 7. the slurry after the removal of impurities does not add washing, uses hydrogen peroxide bleaching 90 minutes, and the weight of slurry and hydrogen peroxide is 100: 20, and the concentration of hydrogen peroxide is 27.5%, and the bleaching disposed slurry send the papermaking operation, and temperature is controlled at 60-75 ℃.
Soak back raw material wash water and take from the shove operation; Flushing back water soaks the soup water as system and returns the immersion operation; The supplementing water of fiberizer is taken from the part drainage of washing drum in the bleaching process.
The preparation of cooling bath: take by weighing caustic soda 40-50 part respectively, hydrogen peroxide 6-10 part, sodium sulphate 12-20 part, cold soaking auxiliary agent 2-6 part, add stir in 1000 parts of water standby.
The cold soaking auxiliary agent is made up of the raw material of following weight ratio: sulphur 20-50 part, magnesium carbonate 10-30 part, magnesia 30-60 part.
4, the specific embodiment
Embodiment 1
The preparation of cooling bath: 20 parts in caustic soda, 10 parts of hydrogen peroxide, 10 parts in sodium sulphate, 3 parts of cold soaking auxiliary agents, add stir in 1000 parts of water standby;
The preparation of cold soaking auxiliary agent: take by weighing 25 parts in sulphur, 30 parts in magnesium carbonate, 30 parts of mixings of magnesia are standby.
The slurrying step is as follows: 1. the wood material section is pulverized; 2. stack with soaking soup normal temperature circulated sprinkling and soaked 2-4 hour, raw material is 1: 3 with soaking liquid proportion; 3. the back raw material is soaked in flushing; 4. send paste mill grinding after the raw material flushing; 5. the slurry behind the defibrination send the press master shove; 6. the slurry behind the shove carries out screening and removing impurities; 7. the slurry after the removal of impurities does not add washing, uses hydrogen peroxide bleaching 90 minutes, and the weight ratio of slurry and hydrogen peroxide is 100: 20, and the concentration of hydrogen peroxide is 27.5%, and temperature is controlled at 60-75 ℃, and the bleaching disposed slurry send the papermaking operation.
Soak back raw material wash water and take from the shove operation, flushing water returns the immersion operation, and the flushing water amount of returning is soaked operation and is used to soak the soup water distribution, and the supplementing water of fiberizer is taken from the part drainage of washing drum in the bleaching process.
Embodiment 2
The preparation of cooling bath: 25 parts in caustic soda, 7 parts of hydrogen peroxide, 15 parts in sodium sulphate, 2 parts of cold soaking auxiliary agents, add stir in 1000 parts of water standby;
The preparation of cold soaking auxiliary agent: take by weighing 25 parts in sulphur, 20 parts in magnesium carbonate, 60 parts of mixings of magnesia are standby.
The slurrying step is identical with embodiment 1.
Embodiment 3
The preparation of cooling bath: 45 parts in caustic soda, 7 parts of hydrogen peroxide, 12 parts in sodium sulphate, 6 parts of cold soaking auxiliary agents, add stir in 1000 parts of water standby;
The preparation of cold soaking auxiliary agent: take by weighing 40 parts in sulphur, 10 parts in magnesium carbonate, 35 parts of mixings of magnesia are standby.
The slurrying step is identical with embodiment 1.
Soak the optional industrial goods of using of soup raw material: caustic soda is selected general industry NaOH for use, and the concentration of hydrogen peroxide can be selected the specification of 27.5-30% for use.Other raw materials without limits.
Claims (4)
1, fast enviornment protection cold soaking pulping process with broad-leaved wood material is characterized in that
(1) preparation of cooling bath: take by weighing caustic soda 30-60 part respectively, hydrogen peroxide 3-15 part, sodium sulphate 10-30 part, cold soaking auxiliary agent 1.5-9 part, add stir in 1000 parts of water standby;
(2) slurrying step is as follows: 1. raw meal is broken into silk; 2. stack with soaking soup normal temperature circulated sprinkling and soaked 2-4 hour, raw material is 1: 3 with soaking liquid proportion; 3. soaking the back raw material washes with shove water; 4. send paste mill grinding after the raw material flushing; 5. the slurry behind the defibrination send the press master shove; 6. the slurry behind the shove carries out screening and removing impurities; 7. the slurry after the removal of impurities need not wash, and send the papermaking operation in 90 minutes with hydrogen peroxide bleaching, and the weight ratio of slurry and hydrogen peroxide is 100: 20, and the concentration of hydrogen peroxide is 27.5%, and temperature is controlled at 60-75 ℃;
2, fast enviornment protection cold soaking pulping process with broad-leaved wood material according to claim 1, it is characterized in that the preparation of cooling bath: take by weighing caustic soda 40-50 part respectively, hydrogen peroxide 6-10 part, sodium sulphate 12-20 part, cold soaking auxiliary agent 2-6 part, add stir in 1000 parts of water standby.
3, fast enviornment protection cold soaking pulping process with broad-leaved wood material according to claim 1 is characterized in that the cold soaking auxiliary agent is made up of the raw material of following weight ratio: sulphur 20-50 part, magnesium carbonate 10-30 part, magnesia 30-60 part.
4, fast enviornment protection cold soaking pulping process with broad-leaved wood material according to claim 1 is characterized in that soaking back raw material flushing water and takes from the shove operation; Flushing back water soaks the soup water as slurrying and returns the immersion operation; The supplementing water of fiberizer is taken from the part drainage of washing drum in the bleaching process.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100436308A CN1296556C (en) | 2005-05-30 | 2005-05-30 | Fast enviornment protection cold soaking pulping process with broad-leaved wood material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100436308A CN1296556C (en) | 2005-05-30 | 2005-05-30 | Fast enviornment protection cold soaking pulping process with broad-leaved wood material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1707019A true CN1707019A (en) | 2005-12-14 |
| CN1296556C CN1296556C (en) | 2007-01-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2005100436308A Expired - Fee Related CN1296556C (en) | 2005-05-30 | 2005-05-30 | Fast enviornment protection cold soaking pulping process with broad-leaved wood material |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100400743C (en) * | 2006-01-13 | 2008-07-09 | 东营中盛环保纸业科技有限公司 | Quick cold soaking and mechanical pulping process for grass family |
| WO2010069151A1 (en) * | 2008-12-19 | 2010-06-24 | 北京英力和泓新材料技术有限公司 | Process for extracting cellulose |
| CN101220565B (en) * | 2008-01-30 | 2010-09-29 | 晏永祥 | Pulping method with zero discharge of sewage water |
| CN102400403A (en) * | 2010-09-09 | 2012-04-04 | 李朝旺 | Clean and industrial production method for high-grade rice paper pulp |
| CN106012633A (en) * | 2016-05-27 | 2016-10-12 | 刘长如 | Broad-leaved cleaning pulping process |
| CN106049148A (en) * | 2016-05-27 | 2016-10-26 | 刘长如 | Gramineous cold-soaking pulping and bleaching process |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1182148A (en) * | 1996-11-08 | 1998-05-20 | 李华民 | Digestion-less and sieving-free chemical pulp-making method producing no nuisance |
| CN1077631C (en) * | 1998-03-23 | 2002-01-09 | 周湘洪 | Cooling-pulping paper-making method |
-
2005
- 2005-05-30 CN CNB2005100436308A patent/CN1296556C/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100400743C (en) * | 2006-01-13 | 2008-07-09 | 东营中盛环保纸业科技有限公司 | Quick cold soaking and mechanical pulping process for grass family |
| CN101220565B (en) * | 2008-01-30 | 2010-09-29 | 晏永祥 | Pulping method with zero discharge of sewage water |
| WO2010069151A1 (en) * | 2008-12-19 | 2010-06-24 | 北京英力和泓新材料技术有限公司 | Process for extracting cellulose |
| CN102400403A (en) * | 2010-09-09 | 2012-04-04 | 李朝旺 | Clean and industrial production method for high-grade rice paper pulp |
| CN102400403B (en) * | 2010-09-09 | 2015-09-23 | 李朝旺 | The cleaned industry working system of high-grade rice paper slurry |
| CN106012633A (en) * | 2016-05-27 | 2016-10-12 | 刘长如 | Broad-leaved cleaning pulping process |
| CN106049148A (en) * | 2016-05-27 | 2016-10-26 | 刘长如 | Gramineous cold-soaking pulping and bleaching process |
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| Publication number | Publication date |
|---|---|
| CN1296556C (en) | 2007-01-24 |
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Granted publication date: 20070124 |