High PH treatment of pulp in a bleach sequence to produce pulp having low D.P. and low copper number for use in lyocell manufacture

a technology of lyocell and high ph treatment, which is applied in the direction of pulping with inorganic bases, non-fibrous pulp addition, papermaking, etc., can solve the problems of high purification cost of “alpha pulp” and unsuitable for use in lyocell manufacturing, and achieve high ph and reduce the degree of polymerization of pulp. , the effect of reducing the degree of polymerization

Inactive Publication Date: 2006-03-30
WEYERHAEUSER CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0006] A high pH and a low pH process for reducing the degree of polymerization of a pulp having a hemicellulose content of at least 7%, is described. The high pH process is carried out at a pH greater than 8, and the low pH process is carried out at a pH of 2 to 8. The high pH process reduces the degree of polymerization without substantially increasing the copper number. The low pH process requires a subsequent treatment with alkali to reduce the copper number of the pulp to less than 2. The process can be pract

Problems solved by technology

The highly purified “alpha pulps” are expensive to manufacture.
However, it is believed that the relatively large amounts of hemicellulose that are retained in Kraft pulp renders the pulp unsuitable for use in lyocell manufacture.
It is generally believed that a high

Method used

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  • High PH treatment of pulp in a bleach sequence to produce pulp having low D.P. and low copper number for use in lyocell manufacture
  • High PH treatment of pulp in a bleach sequence to produce pulp having low D.P. and low copper number for use in lyocell manufacture
  • High PH treatment of pulp in a bleach sequence to produce pulp having low D.P. and low copper number for use in lyocell manufacture

Examples

Experimental program
Comparison scheme
Effect test

example a

Reduction of Degree of Polymerization at High PH with a Catalyst

[0046] Once dried pulp (NB416 fluff pulp available from the Weyerhaeuser Co. of Federal Way, Wash.) now having a consistency of 10% was mixed with 1.5% NaOH (based on pulp weight) and 1.5% H2O2 (based on pulp weight) in a container and bleached at 90° C. for one hour in a lab. A catalyst was added to increase the reduction of degree of polymerization of cellulose. A control sample has a degree of polymerization of 1310. The results are summarized in Table 1.

TABLE 1CATALYSTS FOR H2O2 BLEACHING OF PULPCatalyst inD.P. (postD.P. dropPulpCatalystwater (ppm)treatment)(%)NB416-dryNone1310NB416-dryWater / H2O2 / NaOHnone116511NB416-dryFeCl2.4H2O13.6101523NB416-dryFeCl3.6H2O11.289432NB416-dryMnCl2.3H2O13.512415NB416-dryMnCl211.212425

example b

Reduction of Degree of Polymerization at High PH with a Catalyst

[0047] Never dried pulp from the Weyerhaeuser Company's Kamloops mill from the D1 stage having a consistency of 10% was mixed with NaOH and H2O2 in a container and bleached 90° C. for one hour in a lab. Sodium hydroxide was added at the rate of 1.5%, and hydrogen peroxide was added at the rate of 1.5%, where percent is based on the weight of the pulp, unless otherwise indicated. A catalyst was added to catalyze the reduction of degree of polymerization of cellulose. The pH was greater than 8. A control sample has a degree of polymerization of 939. Some of the samples were washed with deionized (DI) water prior to bleaching. The results are summarized in Table 2.

TABLE 2CATALYST EFFECTIVENESS FORBLEACHING OF MILL SAMPLESCatalystD.P. / copperin waternumber (postD.P. dropPulpCatalyst(ppm)treatment)(%)Kamloops D1None939Kamloops D1Water / H2O2 / NaOH078117Kamloops D1Double H2O20698 / 0.826Kamloops D1FeCl3.6H2O13694 / 0.826Kamloops D...

example c

Reduction of Degree of Polymerization at High PH with a Catalyst

[0049] Never dried pulp (centrifuged Kamloops D1 pulp) having a consistency of 10% was mixed with 1.0% NaOH (based on pulp weight) and 2.0% H2O2 (based on pulp weight) in a container and bleached at 88° C. for one hour in a lab. The pH was greater than 8. A catalyst was added to increase the reduction of degree of polymerization of cellulose. A control sample has a degree of polymerization of 939. The transition metals Ca and Mg that are normally present in the mill are simulated by adding water containing low concentrations of these elemental transition metals. The results are summarized in Table 3.

TABLE 3MILL WATER IMPACT ON BLEACHINGD.P. / copperCatalystnumberCu / Fein water(post-in finalPulpCatalyst(ppm)treatment)CommentproductKamloops D1None939Kamloops D1Water / H2O2 / NaOH07891.0% H2O2 on10pulpKamloops D1Water / H2O2 / NaOH0711 / 0.86 / 4Kamloops D1Water / H2O2 / NaOHWater*93913 ppm Ca / 3 ppm Mg / 0.3 ppm Mn inwaterKamloops D1CuSO365...

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Abstract

A high pH and a low pH process for reducing the degree of polymerization of a pulp having a hemicellulose content of at least 7%. The high pH is greater than 8, and the low pH process is 2 to 8. The high pH process reduces the degree of polymerization without substantially increasing the copper number. The low pH process requires a subsequent treatment with alkali to reduce the copper number of the pulp to less than 2. The process can be practiced in pulp mills with a bleaching sequence having one or more E or D stages. At the end of the bleach sequence, a pulp having a degree of polymerization of 200 to 1100, a copper number of less than 2, and a hemicellulose content of at least 7% is provided. The pulp can be used to make lyocell fibers.

Description

FIELD OF THE INVENTION [0001] The present invention provides methods for reducing the degree of polymerization of pulps without substantially reducing the hemicellulose content. The resultant pulp product has a low copper number and can be used to make lyocell fibers. BACKGROUND OF THE INVENTION [0002] Lyocell fibers are typically made from highly processed pulp known as “high alpha” pulp that is mostly cellulose and has had much of the hemicellulose and lignin removed. The highly purified “alpha pulps” are expensive to manufacture. A common process known as “Kraft” is used widely for the production of a pulp that is lower in cellulose and higher in hemicellulose as compared with the “high alpha” pulps. The Kraft method of pulping is generally one of the most efficient of all pulping methods. However, it is believed that the relatively large amounts of hemicellulose that are retained in Kraft pulp renders the pulp unsuitable for use in lyocell manufacture. Recently, there have been ...

Claims

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Application Information

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IPC IPC(8): D21C9/00D01D1/02B32BD01FD21CD21C9/10D21C9/14D21C9/147D21C9/16D21H
CPCC08B16/00C08L1/02C08L1/06D21C9/16D21C9/14D21C9/147D21C9/10
Inventor LUO, MENGKUI
Owner WEYERHAEUSER CO
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