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Flotation process after bio-enzyme deinking

A post-flotation, biological enzyme technology, applied in the field of papermaking, can solve the problems of reduced deinking efficiency, reduced pulp throughput, and increased production load in the latter-stage flotation, achieve good deinking effect, improve washing function, reduce The effect of production load

Active Publication Date: 2015-11-25
ANHUI LEVEKING BIOTECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Most of the existing biological enzyme deinking processes use the method of directly adding deinking aids to the pulping section, but with the extension of the process, the deinking aids will be lost after flotation, purification, dehydration and other processes in the previous stage. Severe, resulting in lower flotation deinking efficiency
Existing bio-enzyme flotation deinking lines have two or three stages of flotation. Generally, a certain amount of deinking aid is added to the second or third stage of flotation to reduce the flotation, purification, and dehydration in the previous stage. The loss of deinking aids and the reduction of foaming discharge caused by other processes, but the existing process generally adds a large amount of non-degradable surfactant deinking aids in the post-flotation process
Since some large ink particles are screened or excluded in the previous stage of flotation, the smaller ink particles account for a large part in the post-flotation process, and it is difficult for these smaller ink particles to pass through the traditional method of adding a large amount of surfactants. Flotation of deinking aids is completely eliminated, and the entire system needs to be discharged through auxiliary processes such as concentration and washing to achieve the purpose of purification; moreover, a large number of non-degradable surfactant deinking aids will not only pollute the environment, but also cause Difficulty in defoaming, low liquid level in flotation device, decreased slurry passing rate, increased production load, which is not conducive to long-term and effective production

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] (1) Pulping: 200g of waste paper (100% newsprint) and water are added to the pulper, and 0.02g of lipase and 0.02g of octylphenol polyoxyethylene (80) ether are added at the same time, and the disintegration time is 15min. The disintegration temperature is 35°C, and the pulp with a pulp concentration of 10% is obtained;

[0028] (2) One-stage flotation: the pulp is added to the flotation cell, and the pulp is diluted to a pulp concentration of 0.6%. The air flow of the flotation cell is 25L / h, and the pressure is 0.3MPa. The time is 10 minutes;

[0029] (3) dehydration washing: put the slurry after one section of flotation into 100 mesh gauze, rotate at a high speed for 5min in the dehydration device, and the rotating speed is 800 rpm, and the pulp concentration after the control dehydration is 15%;

[0030] (4) Two-stage flotation: add 0.01% post-flotation deinking aid of absolute dry pulp weight after dehydration and washing in the slurry after dehydration and washin...

Embodiment 2

[0035] (1) Pulping: Add 200g waste paper (80% office + 20% books) and water into the pulper, add 0.06g lipase, 0.06g octylphenol polyoxyethylene (100) ether at the same time, and crush The time is 25min, the crushing temperature is 65°C, and a pulp with a pulp concentration of 18% is obtained;

[0036] (2) One-stage flotation: the pulp is added into the flotation cell, and the pulp is diluted to a pulp concentration of 1.5%. The air flow of the flotation cell is 35L / h, the pressure is 1MPa, and the flotation time 20min;

[0037] (3) dehydration washing: put the slurry after one section of flotation into 100 mesh gauze, rotate at a high speed for 10min in the dehydration device, and the rotating speed is 1000 rpm, and the pulp concentration after the control dehydration is 20%;

[0038] (4) Two-stage flotation: add 0.02% post-flotation deinking aid of dry pulp weight after dehydration and washing in the slurry after dehydration and washing, carry out second-stage flotation aft...

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Abstract

The invention discloses a post-floatation process of deinking a bio-enzyme. The process comprises the following steps: repulping; flotation in the first section; dehydrating and washing; flotation in the second section; and washing. The process is characterized in that an environment-friendly floatation deinking assistant consisting of 45-55% of fatty acid methyl ester sulfonate, 35-45% of polyoxyethylene sorbitan fatty acid ester and 10-15% of propylene glycol is added in the step of flotation in the second section. Through the manner, the process disclosed by the invention has the advantages that the washing function in floatation to deink is improved while the bubbling amount of the flotation system and the effective discharge amount are ensured, so that a good deinking effect is realized and the production load is reduced. Meanwhile, more micro printing ink particles are removed in multiple disc concentration and sieving and purifhing stages to prevent the micro printing ink particles from agglomerating in a subsequent section step, so that the product quality is enhanced.

Description

technical field [0001] The invention relates to the technical field of papermaking, in particular to a flotation process after biological enzyme deinking. Background technique [0002] In the deinking process of waste paper recycling, biological enzymes are widely used and generally adopt the method of flotation for deinking. Biological enzymes and deinking aids are used together. Biological enzymes separate ink particles during the pulping process. Deinking aids are generally surfactant components. The amount of discharge, thus bringing out the ink particles. Most of the existing biological enzyme deinking processes use the method of directly adding deinking aids to the pulping section, but with the extension of the process, the deinking aids will be lost after flotation, purification, dehydration and other processes in the previous stage. Severe, resulting in a decrease in deinking efficiency in the latter stage of flotation. Existing bio-enzyme flotation deinking lines...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D21C5/02
CPCY02W30/648Y02W30/64
Inventor 龚赟王剑英张清辉胡关键郭宏涛
Owner ANHUI LEVEKING BIOTECH CO LTD
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