CN1287197A - Technological process of producing poplar fluff pulp - Google Patents
Technological process of producing poplar fluff pulp Download PDFInfo
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- CN1287197A CN1287197A CN 00123951 CN00123951A CN1287197A CN 1287197 A CN1287197 A CN 1287197A CN 00123951 CN00123951 CN 00123951 CN 00123951 A CN00123951 A CN 00123951A CN 1287197 A CN1287197 A CN 1287197A
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Abstract
Sliced poplar is treated through water washing in washing machine, dewatering, preheating, high temperature digestion in water solution of sodium sulfite and water solution of sodium hydroxide inside a digestion pipe, storing in buffering tower and pulp grinding in a pulp grinding machine to obtain poplar pulp. Poplar pulp is sieved, washed to eliminate dregs, further washed in pretreating tower, first bleached for a certain period in the mixed solution of hydrogen peroxide, sodium hydroxide, sodium silicate and magnesium sulfate in a middle bleaching tower, and finally re-bleached in a high bleaching tower to produce poplar fluff pulp.
Description
The present invention relates to use the technological process of producing poplar fluff pulp technical field.
At present make the stuffing that the raw material production Time of Fluff Slurry is used for sanitary napkin with pine abroad,,, the sanitary napkin cost of making is increased so the Time of Fluff Slurry cost is higher because the high pulping process yield of pine price is low; Because domestic protecting forest resources, the Time of Fluff Slurry made with pine from external import of also having to, and willow does not almost have industrial utilization as the quick growing species of trees and is worth, and does not have bibliographical information at home and abroad with its system Time of Fluff Slurry.
The objective of the invention is the invention technological process of producing poplar fluff pulp, poplar do raw material by chip, operation such as washing, boiling, defibrination and bleaching makes Time of Fluff Slurry, it makes the Time of Fluff Slurry price of making very low with uncommercial poplar almost as raw material.
The present invention is achieved in that the poplar that processes is chipped, by conveyer and cyclone separator wood chip is sent into chip bin, wood chip is sent to the rinsing machine washing by conveyer from chip bin, then it is dewatered with spiral dewater, wood chip after the dehydration advances pre-hot aggregate bin, advance the boiling pipe again, wood chip sodium sulfite aqueous solution and sodium hydrate aqueous solution boiling certain hour at high temperature in the boiling pipe, send into paste mill grinding again after it being sent into tempering tower then, wood pulp is sent into stock tank after screening, pretreater is sent in wood pulp washing and slagging-off again, wash again through it and to float tower in delivering to, in float wood pulp aqueous hydrogen peroxide solution in the tower, sodium hydrate aqueous solution, the mixed liquor insulation certain hour of sodium silicate aqueous solution and magnesium sulfate is bleached, the wood pulp of bleaching is sent into height again float tower and bleach again, make Time of Fluff Slurry.
Advantage of the present invention is: this process is simple; fluff pulp fibers flexibility and the bulkiness made are good; absorbency and full fluidity can be good; the finished product whiteness is higher; it is that the Application and Development of quick growth poplar wood provides new approach that this technology is made raw material with poplar; this process synthesis yield height, energy consumption is low, nontoxic, harmless and pollution-freely be convenient to carry out sewage disposal protection environment.
Below in conjunction with embodiment, the present invention will be further described:
Joint is removed in the poplar hand peeling, sawed-off and splitting, the screening of peeling is then sent wood chip into chip bin by conveyer and cyclone separator, wood chip is sent to the rinsing machine washing by conveyer from chip bin, then it is dewatered with spiral dewater, wood chip after the dehydration advances pre-hot aggregate bin, advance the boiling pipe again, wood chip is with containing 5% sodium sulfite aqueous solution and containing the boiling 15 minutes under 160 ℃ temperature of 2.5% sodium hydrate aqueous solution in the boiling pipe, send into paste mill grinding again after it being sent into tempering tower then, wood pulp is sent into stock tank after screening, pretreater is sent in wood pulp washing and slagging-off again, wash again through it and to float tower in delivering to, in float wood pulp in the tower with the hydrogen peroxide that contains 2.5%, 2% NaOH, 4% sodium metasilicate and 0.5% magnesium sulfate solution mixed liquor were bleached 1.5 hours under 60 ℃ temperature, the wood pulp of bleaching is sent into height again float tower, wood pulp is used and is contained 3% hydrogen peroxide in height floats tower, 2% NaOH, 5% sodium metasilicate and 0.5% magnesium sulfate solution mixed liquor were bleached 2.5 hours under 60 ℃ temperature, made Time of Fluff Slurry.
Claims (1)
- Use technological process of producing poplar fluff pulp, it is characterized in that: the poplar that processes is chipped, by conveyer and cyclone separator wood chip is sent into chip bin, wood chip is sent to the rinsing machine washing by conveyer from chip bin, then it is dewatered with spiral dewater, wood chip after the dehydration advances pre-hot aggregate bin, advance the boiling pipe again, wood chip sodium sulfite aqueous solution and sodium hydrate aqueous solution boiling certain hour at high temperature in the boiling pipe, send into paste mill grinding again after it being sent into tempering tower then, wood pulp is sent into stock tank after screening, pretreater is sent in wood pulp washing and slagging-off again, wash again through it and to float tower in delivering to, in float wood pulp aqueous hydrogen peroxide solution in the tower, sodium hydrate aqueous solution, the mixed liquor insulation certain hour of sodium silicate aqueous solution and magnesium sulfate is bleached, the wood pulp of bleaching is sent into height again float tower and bleach again, make Time of Fluff Slurry.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00123951 CN1287197A (en) | 2000-10-19 | 2000-10-19 | Technological process of producing poplar fluff pulp |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00123951 CN1287197A (en) | 2000-10-19 | 2000-10-19 | Technological process of producing poplar fluff pulp |
Publications (1)
Publication Number | Publication Date |
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CN1287197A true CN1287197A (en) | 2001-03-14 |
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Family Applications (1)
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CN 00123951 Pending CN1287197A (en) | 2000-10-19 | 2000-10-19 | Technological process of producing poplar fluff pulp |
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CN (1) | CN1287197A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101613975B (en) * | 2009-07-17 | 2011-01-05 | 中国林业科学研究院林产化学工业研究所 | Method for preparing bleached chemi-mechanical pulp for culture paper making by using cotton wood to process remainder |
CN101403121B (en) * | 2007-02-15 | 2011-08-24 | 西屋电气有限责任公司 | Removal of niobium second phase particle deposits from pickled zirconium-niobium alloys |
CN104911938A (en) * | 2007-06-12 | 2015-09-16 | 米德韦斯瓦科公司 | Fiber blend having high yield and enhanced pulp performance |
CN105128119A (en) * | 2015-07-15 | 2015-12-09 | 百仪家具有限公司 | Whitening type composite high-density fiberboard and preparation method thereof |
CN106223087A (en) * | 2016-09-14 | 2016-12-14 | 黑龙江秀泉科技有限公司 | A kind of dry method pulping process and equipment |
CN115592756A (en) * | 2022-10-11 | 2023-01-13 | 中国林业科学研究院林产化学工业研究所(Cn) | Preparation method of high-whiteness superfine bamboo powder |
-
2000
- 2000-10-19 CN CN 00123951 patent/CN1287197A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101403121B (en) * | 2007-02-15 | 2011-08-24 | 西屋电气有限责任公司 | Removal of niobium second phase particle deposits from pickled zirconium-niobium alloys |
CN104911938A (en) * | 2007-06-12 | 2015-09-16 | 米德韦斯瓦科公司 | Fiber blend having high yield and enhanced pulp performance |
CN101613975B (en) * | 2009-07-17 | 2011-01-05 | 中国林业科学研究院林产化学工业研究所 | Method for preparing bleached chemi-mechanical pulp for culture paper making by using cotton wood to process remainder |
CN105128119A (en) * | 2015-07-15 | 2015-12-09 | 百仪家具有限公司 | Whitening type composite high-density fiberboard and preparation method thereof |
CN106223087A (en) * | 2016-09-14 | 2016-12-14 | 黑龙江秀泉科技有限公司 | A kind of dry method pulping process and equipment |
CN115592756A (en) * | 2022-10-11 | 2023-01-13 | 中国林业科学研究院林产化学工业研究所(Cn) | Preparation method of high-whiteness superfine bamboo powder |
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