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Method for brightening mechanical pulps

a mechanical pulp and brightening technology, applied in pulping with acid salts/anhydrides, papermaking, paper pulping, etc., can solve the problems of less effective technique at higher ph values, the presence of transition metal ions in paper pulp is known to be detrimental to the brightening process, etc., to reduce the bleaching efficiency, increase the brightness reversion, and reduce the brightness level

Inactive Publication Date: 2003-04-03
HACHE MAURICE JOSEPH ALBERT +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0011] Dilution water (i.e. cloudy white water) typically is added to mechanical pulp prior to a bleaching step. In an integrated pulp and paper mill, the dilution water is a recycled stream from the paper making operations. In acid-based mills, the dilution water typically is at a pH from 4 to 5, and contains impurities such as pulp fines, suspended and dissolved solids, fillers and transition metal ions. In a neutral to alkaline paper making environment, i.e., one that utilizes PCC as a filler, the dilution water is at a pH from 6 to 8, and contains impurities such as pulp fines, suspended calcium carbonate, and transition metal ions. Of these impurities, transition metals can be especially troublesome as they can catalyze the decomposition of bleaching chemicals resulting in reduced bleaching efficiency and lower brightness levels. They also tend to increase brightness reversion and thus further contribute to lowering the brightness of bleached pulp. Both reductive and oxidative bleaching chemicals are affected by transition metals. The most commonly used oxidative bleaching chemical is hydrogen peroxide. Reductive bleaching chemicals typically are aqueous reducing agents, including, e.g., dithionite anion, also known as hydrosulfite, borohydrides and bisulfites, and formamidine sulfinic acid.
[0013] According to this invention, the use of the low solids stream under neutral or alkaline conditions (pH 6 to 8) minimizes the adverse effects on the brightness of the resulting pulps. The Examples demonstrate that the reduction of the amount of solids in the cloudy white water significantly lowers the levels of transition metals and other impurities in the low solids stream and thereby improves the efficiency of bleaching. Preferably, the pH of the dilution water is from 6.5 to 7.5.
[0015] Chemical treatment of the high solids stream recovered from cloudy dilution water from neutral or alkaline processes according to the method of this invention allows recycling of the solids without adverse effects on brightness of the resulting paper and pulps. Without being bound by theory, it is believed that addition of a reducing agent to the solids recovered from the pulp dilution water reduces the valences of the transition metal ions. The reduced valences in turn result in better chelation of transition metals, and treated solids that typically have reduced levels of transition metals, and thus can be introduced into the bleaching and paper making process without adversely affecting pulp brightness.

Problems solved by technology

The presence of transition metal ions in paper pulp is known to be detrimental to the brightening process.
However, this technique is less effective at higher pH values, such as those encountered when precipitated calcium carbonate ("PCC") is used as a filler in a pulp and paper mill.

Method used

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  • Method for brightening mechanical pulps
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  • Method for brightening mechanical pulps

Examples

Experimental program
Comparison scheme
Effect test

example 1

Effect of Process Conditions on BGH Brightening

[0017] Pulp and white water used in this study were obtained from a North American mill. The pulp was a chemothermomechanical pulp (cTMP), which was collected after the secondary refiners and prior to the latency chest. The Precipitated Calcium Carbonate (PCC) containing white water (WW) was collected just prior to dilution at the latency chest. Studies were conducted to determine the effect on BGH bleached pulp brightness levels of the following four process variables: retention time, bleaching temperature, and bleaching consistency using either PCC-containing white water (WW) or deionized (DI) water for dilution of the pulp slurry. The hydrosulfite dosage (hydro) was 0-24 lbs. / ton BGH at a pH of 10. The raw data for these experiments can be seen in Table 1. Temperatures are in .degree. C. (Temp.), retention times are in minutes, consistency ("Consist.") in weight % of pulp in the pulp slurry, deionized water had a pH of 6.5 and PCC-co...

example 2

Fines (Solids) Removal and Reuse of Low-Solids White Water

[0022] FIG. 2 compares the BGH-bleached pulp brightness of pulp diluted with DI water, PCC-containing white water, the filtrate of PCC-containing white water, and fines that were removed by filtration of PCC-containing white water and re-suspended in DI water. The results show that the removal of solids and reuse of low solids white water for bleaching purposes minimizes the adverse effects of BGH brightening under alkaline or neutral conditions. The results also show that it is the fines portion, which consists of actual pulp fines, undissolved solids, and transition metals in the white water that is responsible for most of the brightness loss. Based on these results, further testing of the fines portion of PCC containing white water was undertaken and is summarized in the following examples.

[0023] Results of transition metal analysis of the pulp, the white water filtrate, and the fines are shown in Table 5.

5TABLE 5 Metals C...

example 3

Fines Treatment and Re-use

[0025] To reduce the transition metal concentrations, fines were treated by the Qy process. The fines first were treated with 0.1% BGH and then with 0.5% diethylenetriaminepentaacetic acid (DTPA). Experiments were conducted at a pH of 5.5, a consistency of 3.0%, and a temperature of 50.degree. C. for 30 minutes. The Qy treatment is believed to be more effective than the Q treatment, i.e., use of only chelant, because reduction of transition metal valence state by BGH renders the transition metal ions more amenable to chelation. The Qy treatment allows higher brightness levels when using hydrogen peroxide as a brightening agent. Table 6 shows the results from Q and Qy treatments on the fines portion of PCC-containing white water.

6TABLE 6 Metal Levels After Q or Qy Treatment of Fines From PCC-Containing White Water (levels in ppm, unless otherwise indicated) Al Ca (%) Cu Fe Mg Mn Q 807 8.23 4.3 668 336 76.1 Qy 726 6.84 3.3 638 312 61.2 Control 821 9.99 3.4 66...

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Abstract

The present invention is directed to an improved method for brightening mechanical pulp under neutral or alkaline papermaking conditions. The improvement comprises the steps of: (a) separating neutral or alkaline pulp dilution water into a high-solids stream and a neutral or alkaline low-solids stream; and (b) reusing the neutral or alkaline low-solids stream for pulp dilution purposes prior to a bleaching process.

Description

[0001] This invention relates generally to a method for brightening mechanical pulp.[0002] Paper pulp typically is subjected to a brightening process prior to paper making. The presence of transition metal ions in paper pulp is known to be detrimental to the brightening process. Chelation techniques, also known as Q stage techniques, have been used to remove transition metal ions from pulp, thereby enhancing brightness levels. Y. Ni et al., Pulp & Paper Canada, vol. 98, T285 (1998). Treatment of pulp with sodium hydrosulfite prior to chelation, known as the Q.sub.y stage technique, is believed to improve chelation of metals, thereby further enhancing pulp brightness. However, this technique is less effective at higher pH values, such as those encountered when precipitated calcium carbonate ("PCC") is used as a filler in a pulp and paper mill.[0003] The problem addressed by this invention is to find a more effective method for brightening mechanical pulp at high pH values.STATEMENT O...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): D21C9/10
CPCD21C9/1026
Inventor HACHE, MAURICE JOSEPH ALBERTGODA, RANGAMANNAR
Owner HACHE MAURICE JOSEPH ALBERT
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