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Modified papermaking grade wood pulp production process

A production process and technology of papermaking grade, which is applied in the field of production process of modified papermaking grade wood pulp, can solve the problems of shortage of raw materials, need more raw materials, production difficulties, etc., so as to improve the cooking uniformity, improve the reaction performance, and reduce the degree of polymerization. Effect

Inactive Publication Date: 2011-12-14
TANGSHAN SANYOU GRP DONGGUANG PULP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] With the development of my country's viscose fiber industry, domestic enterprises mostly use cotton pulp as the raw material for viscose fiber production. However, due to the constraints of planting area and growth cycle, this raw material is increasingly in short supply, which has seriously affected the development of my country's viscose fiber industry. develop
For this reason, very few enterprises try to use bamboo pulp as the production raw material of viscose fiber, and have achieved preliminary success, as the patent No. is CN02112175.3, the invention patent called "bamboo pulp denaturation production process" discloses a The production process of bamboo pulp, but the average length of bamboo fiber is lower than that of paper-making wood fiber, and because of its high ash content and high pentose content, bamboo fiber is hard, thick-walled, narrow cell cavity, dense fiber tissue, There are problems such as air in the cells, which makes production difficult, requires a lot of raw materials, and costs high, so it has not been widely used

Method used

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  • Modified papermaking grade wood pulp production process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] 1. Prepare materials

[0022] After stacking the paper-making grade wood pulp boards on the conveyor, they are conveyed by belts and fed into the hydraulic pulper as required, sprayed with alkali with a concentration of 41g / L, sent to the press for extrusion and dehydration, and then enter the steaming ball.

[0023] 2. Cooking

[0024] Use steaming ball alkaline cooking, send the impregnated slurry into the steaming ball for cooking, keep the amount of caustic soda accounted for 13% of the absolute dry slurry, bath ratio 1:3.44, heating time 80 minutes, holding time 80 minutes, holding temperature 160 ℃, large steam release, time 50 minutes, pressure 0Mpa.

[0025] 3. Chlorination

[0026] Chloride the cooked slurry to ensure that the acid content before chlorination is 0.13g / L, the chlorine content after chlorination is 0.05g / L, and the alkali content after chlorination is 20g / m 3 .

[0027] 4. Bleaching

[0028] Send the chlorinated slurry into the bleaching tan...

Embodiment 2

[0033] 1. Prepare materials

[0034] After stacking the paper-making grade wood pulp boards on the conveyor, they are conveyed by the belt and fed to the hydraulic pulper as required, sprayed with alkali with a concentration of 42g / L, sent to the press for extrusion and dehydration, and then enter the steaming ball.

[0035] 2. Cooking

[0036] Use the steaming ball alkali method to cook, send the impregnated slurry into the steaming ball for cooking, keep the amount of caustic soda accounted for 15% of the absolute dry slurry, the bath ratio is 1:3.5, the heating time is 90 minutes, the holding time is 90 minutes, and the holding temperature is 171 ℃, large steam release, time 45 minutes, pressure 0.01Mpa.

[0037] 3. Chlorination

[0038] Chloride the cooked slurry to ensure that the acid content before chlorination is 0.15g / L, the chlorine content after chlorination is 0.08g / L, and the alkali content after chlorination is 40g / m 3 .

[0039] 4. Bleaching

[0040] Send t...

Embodiment 3

[0045] 1. Prepare materials

[0046] After stacking the paper-making grade wood pulp boards on the conveyor, they are conveyed by the belt and fed to the hydraulic pulper as required, sprayed with alkali with a concentration of 43g / L, sent to the press for extrusion and dehydration, and then enter the steaming ball.

[0047] 2. Cooking

[0048] Use the steaming ball alkali method to cook, send the impregnated slurry into the steaming ball for cooking, keep the amount of caustic soda accounted for 16% of the dry slurry, the bath ratio is 1:3.6, the heating time is 100 minutes, the holding time is 110 minutes, and the holding temperature is 175 ℃, large steam release, time 50 minutes, pressure 0.01Mpa.

[0049] 3. Chlorination

[0050] Chloride the cooked slurry to ensure that the acid content before chlorination is 0.17g / L, the chlorine content after chlorination is 0.13g / L, and the alkali content after chlorination is 48g / m 3 .

[0051] 4. Bleaching

[0052] Send the chlo...

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Abstract

The invention discloses a production process of modified paper-making grade wood pulp, which comprises the following steps: (1) preparing materials, feeding paper-making grade wood pulp boards into a hydraulic pulper, dispersing and dispersing through alkali spraying and agitator, After being sent to the press for extrusion and dehydration, it is sent to steaming balls; (2) cooking, the impregnated slurry enters steaming balls for cooking, and caustic soda is added; (3) chlorination, the cooked slurry is chlorinated, and added Hydrochloric acid, liquid chlorine, caustic soda; (4) bleaching, the chlorinated slurry is sent to the bleaching tank for bleaching; (5) acid treatment, adding hydrochloric acid for acid treatment, spraying into the bleaching tank, and papermaking , Packaged as wood pulp. The invention uses a hydraulic pulper to fully decompose and disperse the slurry, so that the impregnation of the wood fiber and the lye is more uniform, and the uniformity of cooking is greatly improved. Through the cooking process, the content of non-cellulose impurities can be reduced, and the degree of polymerization of cotton fibers can be reduced. Through the chlorination process, part of the colored impurities can be removed, and the content of methyl cellulose can be increased accordingly. Through the bleaching process, the whiteness of cellulose can be improved, and the polymerization can be continuously reduced to remove impurities. Through acid treatment, ash and iron can be removed, and the reaction performance can be improved. The modified papermaking grade wood pulp produced by the invention can meet the index requirement of dissolving wood pulp and meet the production requirement of viscose fiber.

Description

technical field [0001] The invention relates to modified paper-making grade wood pulp and a production process, in particular to a production process of modified paper-making grade wood pulp suitable for viscose fibers. Background technique [0002] With the development of my country's viscose fiber industry, domestic enterprises mostly use cotton pulp as the raw material for the production of viscose fiber. However, due to the constraints of the planting area and growth cycle, the raw material is increasingly in short supply, which has seriously affected the development of my country's viscose fiber industry. develop. For this reason, very few enterprises try to use bamboo pulp as the production raw material of viscose fiber, and have achieved preliminary success, as the patent No. is CN02112175.3, the invention patent called "bamboo pulp denaturation production process" discloses a The production process of bamboo pulp, but the average length of bamboo fiber is lower than ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): D21B1/34D21C3/02D21C9/00D21C9/10
Inventor 王忠学张宝恒陈玉彬孟令华姬荣亮吴红帅郭艳军
Owner TANGSHAN SANYOU GRP DONGGUANG PULP CO LTD
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