Process for peroxide bleaching of mechanical pulp using sodium carbonate and non-silicate chelating agents

• US 5,248,389 A
• Filed: 07/13/1992
• Issued: 09/28/1993
• Est. Priority Date: 03/18/1992
• Status: Expired due to Fees

• Current Assignee: FMC Corporation
• Original Assignee: FMC Corporation
• Inventors: Tremblay, Steve E., Meng, Tommy Y., Heimburger, Stanley A.
• Primary Examiner(s): Jones, W. Gary
• Assistant Examiner(s): NGUYEN, TAN D
• Application Number:
  US07/912,429
• Time in Patent Office: 442 Days
• Field of Search: 162/19, 162/72, 162/76, 162/78, 162/80, 162/90
• US Class Current: 162/76
• CPC Class Codes: D21C 9/1036 Use of compounds accelerating or improving the efficiency of the processes
• CPC Class Codes: D21C 9/163 with peroxides

Abstract

A process is provided for peroxygen bleaching of high yield pulp in which sodium carbonate replaces sodium hydroxide and sodium silicate. The process employs a chelating agent as a substitute for the silicate normally required so that the process can operate as a closed cycle system.

Claims

1. A process for brightening mechanical and high yield hardwood pulp substantially free of silicate and caustic soda to produce a brightened pulp of brightness substantially equivalent to that obtained using the equivalent amount of peroxide in a silicate and caustic soda bleaching liquor comprising:

(a) incorporating hardwood pulp into a silicate-free bleach solution to provide a consistency of about 5% to 45%, the bleach solution consisting essentially of about 2% to about 6% by weight sodium carbonate on an oven dry basis of pulp, about 0.2% to about 0.6% by weight silicate substitute selected from the group consisting of organic chelating agents, polyhydroxy compounds, and oligomers and polymers of hydroxy and carboxy compounds and mixtures thereof, and about 2% to about 7% by weight hydrogen peroxide on the oven dry basis of the pulp,

(b) maintaining the bleach solution at a temperature of about 35°

C. to about 70°

C. for about 2 to about 6 hours, and

(c) separating the pulp from at least part of the bleach solution thereby providing a bleached pulp and a residual solution.

2. The process of claim 1 wherein sufficient unbleached pulp is incorporated into the bleach solution to provide a consistency of about 11 to 14%, and the bleach solution comprises about 3% to about 4% sodium carbonate, about 0.3% to about 0.6% silicate substitute and about 2.5% to about 3.5% hydrogen peroxide.

3. The process of claim 1 wherein the pulp has been bleached and is incorporated into the bleach solution at a consistency of about 25% to about 45%, and the bleach solution comprises about 3% to about 4% sodium carbonate, about 0.3% to about 0.6% silicate substitute, and about 4% to about 6% hydrogen peroxide.

4. The process of claim 1 wherein the bleached pulp from step(c) is incorporated into a second stage bleach solution at a consistency of about 25% to about 45%, the second stage bleach solution comprising about 3% to about 4% sodium carbonate, about 0.3% to about 0.6% silicate substitute, and about 4% to about 6% hydrogen peroxide and is subjected to the further steps of maintaining the second stage bleach solution at a temperature of about 35°

C. to about 70°

C. for about 2 to about 6 hours, and separating the pulp from at least part of the second stage bleach solution thereby providing a second stage bleached pulp and a second stage residual solution.

5. A process for brightening mechanical and high yield hardwood pulp substantially free of silicate and caustic soda to produce a brightened pulp of brightness substantially equivalent to that obtained using the equivalent amount of peroxide in a silicate and caustic soda bleaching liquor comprising:

(a) incorporating hardwood pulp into a silicate-free, first stage bleach solution to provide a consistency of about 5% to 14%, the first stage bleach solution comprising about 2% to about 6% by weight sodium carbonate, about 0.2% to about 0.6% by weight silicate substitute selected from the group consisting or organic chelating agents, polyhydroxy compounds, and oligomers and polymers of hydroxy and carboxy compounds and mixtures thereof, and about 2% to about 7% by weight hydrogen peroxide on an oven dry basis of the pulp,

(b) maintaining the first stage bleach solution at a temperature of about 35°

C. to about 70°

C. for about 2 to about 6 hours,

(c) separating the pulp from at least part of the first stage bleach solution thereby providing a bleached pulp and a first stage residual solution,

(d) incorporating the bleached pulp into a second stage bleach solution at a consistency of about 25% to about 45%, the second stage bleach solution comprising about 3% to about 4% sodium carbonate, about 0.3% to about 0.6% silicate substitute, and about 4% to about 6% hydrogen peroxide,

(e) maintaining the second stage bleach solution at a temperature of about 35°

C. to about 70°

C. for about 2 to about 6 hours,

(f) separating the pulp from at least part of the second stage bleach solution thereby providing a second stage bleached pulp and a second stage residual solution.

6. The process of claim 5 wherein the first stage residual solution is incorporated into the first stage bleach solution in step (a).

7. The process of claim 5 wherein the second stage residual solution is incorporated into the first stage bleach solution in step (a).

8. The process of claim 5 wherein the first stage residual solution is incorporated into the second stage bleach solution in step (d).

9. The process of claim 5 wherein the second stage residual solution is incorporated into the second stage bleach solution in step (d).

10. The process of claim 5 wherein the first stage residual solution is incorporated into first stage bleach solution in step (a) and wherein the second stage residual solution is incorporated into the second stage bleach solution in step (d).