Process for chlorine bleaching of kraft pulp using a sulfite extraction stage
First Claim
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1. A process for bleaching kraft pulp comprising:
- (a) treating an aqueous slurry of kraft pulp with a bleaching effective amount of chlorine and a cellulose protective amount of chlorine dioxide;
(b) extracting the pulp of step (a) above at an acidic pH and at a temperature range of from about 30°
C. to about 77°
C. with an effective amount of a chlorinated lignin solubilizing agent comprising an aqueous solution of a sulfite ion;
(c) treating the pulp from step (b) above with an effective amount of chlorine dioxide or sodium hypochlorite;
(d) extracting the pulp from step (c) above with an effective amount of an aqueous solution of an alkali metal hydroxide or a chlorinated lignin solubilizing agent as defined in step (b) above; and
(e) treating the pulp from step (d) above with an effective amount of chlorine dioxide.
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Abstract
Extraction of chlorine bleached kraft wood pulps with aqueous peracids at pH values of 7 or below, aqueous sulfites at pH values below 10 or with certain non-aqueous solvents provides extracted pulps having lower residual color and permits use of lesser quantities of alkali or chlorine dioxide in subsequent bleach steps to attain brightness and strength levels comparable to those attained with pulps treated by alkaline extraction at pH values of 10 or higher. At a comparable level of alkali and chlorine dioxide or hypochlorite application, extraction of chlorinated pulp with peracids provides bleached pulps with enhanced brightness.
10 Citations
6 Claims
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1. A process for bleaching kraft pulp comprising:
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(a) treating an aqueous slurry of kraft pulp with a bleaching effective amount of chlorine and a cellulose protective amount of chlorine dioxide; (b) extracting the pulp of step (a) above at an acidic pH and at a temperature range of from about 30°
C. to about 77°
C. with an effective amount of a chlorinated lignin solubilizing agent comprising an aqueous solution of a sulfite ion;(c) treating the pulp from step (b) above with an effective amount of chlorine dioxide or sodium hypochlorite; (d) extracting the pulp from step (c) above with an effective amount of an aqueous solution of an alkali metal hydroxide or a chlorinated lignin solubilizing agent as defined in step (b) above; and (e) treating the pulp from step (d) above with an effective amount of chlorine dioxide. - View Dependent Claims (2, 3, 4, 5, 6)
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Specification