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A papermaking wet end slurry system

A slurry and wet end technology, applied in the field of papermaking, can solve the problems of difficult water circulation operation of the wet end system, unable to meet the overall needs of the operation, and unable to peel off smoothly in sequence, and achieve guaranteed strength, good dryness and wet tensile strength. , the effect of increasing strength

Active Publication Date: 2017-09-12
HAINAN JINHAI PULP & PAPER
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The fiber length of NBKP (2.0-2.2mm) is significantly higher than that of LBKP (0.7-0.8mm). The introduction of a large amount of NBKP will make the interweaving of paper worse. However, in the prior art, the use of NBKP or less often leads to the strength of paper. Insufficient, negative effects such as increased number of paper breaks
In addition, if LBKP is used to simply replace NBKP as the padding pulp, because the pulp strength and fiber length of LBKP are lower than NBKP, the wet strength of the padding pulp formed by the interlacing of fibers will be significantly weaker than when NBKP is used, resulting in its The discs of the disc fiber recovery machine cannot be peeled off smoothly one by one, which makes the water circulation operation of the wet end system difficult and cannot meet the overall needs of the operation

Method used

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  • A papermaking wet end slurry system
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Embodiment approach 1

[0040] Two pulping lines are adopted to provide hardwood bleached chemical pulp (LBKP1, LBKP2) respectively, wherein LBKP1 is the first pulping line in the present invention, and the end of the LBKP2 pulping line is directly connected to the mixed stock tank, and the stock ratio is 70% LBKP1, 30% LBKP2, the refining concentration is 6% for LBKP1 and 6% for LBKP2, the refining power is 140kwh / t for LBKP1, and 80kwh / t for LBKP2, the anionic polymer is anionic guar gum, and the addition amount is 1 Kg per ton of the first fiber slurry is added in the form of an anionic guar gum solution with a concentration of 1% after brewing. After adding anionic guar gum, the first fiber slurry is modified by a refiner under high temperature and high pressure , the recorded slurry filtrate PCD is-100μeq / L; Cationic polymer is selected cationic starch, and the addition is 10 kilograms of every ton of second fiber slurry, and it is added in the form of a 4% cationic starch solution after cooking,...

Embodiment approach 2

[0042]Two pulping lines are adopted to provide hardwood bleached chemical pulp (LBKP1, LBKP2) respectively, wherein LBKP1 is the first pulping line in the present invention, and the end of the LBKP2 pulping line is directly connected to the mixed stock tank, and the stock ratio is 70% LBKP1, 30% LBKP2, the refining concentration is 6% for LBKP1 and 6% for LBKP2, the refining power is 140kwh / t for LBKP1, and 80kwh / t for LBKP2, the anionic polymer is anionic polyacrylamide, and the addition amount is 0.1 Kg per ton of the first fiber slurry, added in the form of an anionic polyacrylamide solution with a concentration of 0.2% after brewing, after adding anionic polyacrylamide, the first fiber slurry is modified by a refiner under high temperature and high pressure , the PCD of the slurry filtrate is -200μeq / L; the cationic polymer is a cationic acrylamide copolymer, and the addition amount is 1 kg per ton of the second fiber slurry, and the cationic acrylamide copolymer with a con...

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Abstract

The invention discloses a pulp system for a papermaking wet end. The system comprises at least one pulp line, a fiber recovery machine and a pulp mixing tank, wherein the at least one pulp line at least comprises one first pulp line, the first pulp line is used for providing first fiber pulp of broadleaf wood bleached chemical pulp, the fiber recovery machine is connected with the first tail end of the first pulp line and used for recovering second fiber pulp separated from the first fiber pulp in the first pulp line, the pulp mixing tank is connected with the second tail end of the first pulp line and the tail end of the fiber recovery machine and used for mixing third fiber pulp separated from the first fiber pulp in the first pulp line with fourth fiber pulp recovered by the fiber recovery machine, and cation polymers are added to the second fiber pulp after the second fiber pulp is separated from the first fiber pulp in the first pulp line and before the second fiber pulp enters the fiber recovery machine. Accordingly, the interweaving performance of paper and peeling smoothness of cushion pulp can be improved, and paper strength is guaranteed.

Description

technical field [0001] The invention relates to the technical field of papermaking, in particular to a slurry system at the wet end of papermaking. Background technique [0002] When making paper with inter-wire paper machine, there are high requirements for wet paper web and paper strength. Because the pulp strength of softwood bleached chemical pulp (abbreviated as NBKP) is significantly higher than that of hardwood bleached chemical pulp (abbreviated as LBKP), in order to meet For the strength requirement of high-speed sandwich paper machine, it is generally used to add 10-30% NBKP to LBKP for copying. At the same time, due to the requirements of the ecological environment, the water cycle of the paper machine must be closed and operated. A large number of fiber components in the white water under the paper machine need to rely on NBKP with long fibers as the padding pulp of the multi-disc fiber recovery machine for fiber recovery. It is possible to reduce the loss of fi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D21F1/66
Inventor 王正平
Owner HAINAN JINHAI PULP & PAPER
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