Nonsulfur chemimechanical pulping process

• US 4,548,675 A
• Filed: 11/25/1983
• Issued: 10/22/1985
• Est. Priority Date: 05/16/1983
• Status: Expired due to Fees

• Current Assignee: New Fibers International
• Original Assignee: New Fibers International
• Inventors: Gordy, John
• Primary Examiner(s): Smith, William F.
• Application Number:
  US06/554,909
• Time in Patent Office: 697 Days
• Field of Search: 162/72, 162/90, 162/26
• US Class Current: 162/26
• CPC Class Codes: D21C 3/003 with organic compounds D21C3/20 and D21C3/222 take precedence

Abstract

A nonsulfur chemimechanical pulping process for producing pulp from woody materials is disclosed. The process is particularly suited for producing corrugating medium pulp from hardwood chips although the process can be adapted to production of other types of pulp and can use other types of woody materials. The process comprises impregnation and dilution of the chips in a dilute aqueous pulping solution of a lower alkanolamine catalyzed with ammonium hydroxide. The preferred alkanolamine is monoethanolamine present in a weight ratio to ammonium hydroxide of about 1 part to 1 part or less to 1 part to 3 parts or more. The pulping solution may be repeatedly reused and the process of this invention does not produce environmentally objectionable by-products.

Claims

1. A process for pulping woody materials comprising:

providing a pulping solution containing a dilute mixture of a lower alkanolamine and ammonium hydroxide in water;

providing a heated vessel;

admitting a predetermined quantity of chips and solution to said vessel;

impregnating said chips in said solution and digesting said chips under conditions of temperature and pressure effective to initiate a lignin depolymerization reaction in said chips for a predetermined period of time;

3. The process of claim 1 wherein said lower alkanolamine is monoethanolamine.

5. The process of claim 3 wherein the step of digesting further comprises lowering the level of solution in said vessel below the chips;

vaporizing said solution, in part, and circulating said solution vapor above, below and on all sides of said chips to digest said chips under a vapor dome.

6. The process of claim 1 wherein said chips are hardwood chips and said pulp produced is corrugating medium pulp produced in a yield of about 85-95%.

7. The process of claim 1 wherein said lignin depolymerization reaction is maintained under a temperature of about 285°

F. and a pressure of at least about 50 psi for at least about 15 minutes.

9. The process of claim 7 wherein said lower alkanolamine is monoethanolamine.

11. The process of claim 9 wherein said pulping solution comprises about 10-12 gallons monoethanolamine to 36-40 gallons ammonium hydroxide to about 1,000 gallons water.

13. The process of claim 11 wherein the step of digestion further comprises lowering the level of solution in said vessel below the chips;

vaporizing said solution at least in part; and

circulating said solution vapor above, below and on all sides of said chips to digest said chips under a vapor dome.

15. The process of claim 13, wherein the lower alkanolamine is monoethanolamine.

16. The process of claim 13, wherein said ammonium hydroxide is present in a weight ratio to the lower alkanolamine of about at least 1:

1.

17. The process of claim 13, wherein the step of digesting said chips further comprises maintaining a weight ratio of about 4:

1 of said pulping solution to said chips during said digestion step.

18. The method of claim 13 wherein said chips are maintained in said digestion vessel for a predetermined period of time of about 15 minutes.

2. refining said chips to produce said pulp and separating the used solution from the pulp.

4. The process of claim 2 wherein said monoethanolamine is present in a ratio to ammonium hydroxide of 1 part to about 3, by weight.

8. A process for producing corrugating medium pulp from hardwood chips comprising:

providing a pulping solution containing a dilute aqueous mixture of a lower alkanolamine and ammonium hydroxide;

providing a heated vessel;

admitting a predetermined quantity of said chips to said vessel;

heating said solution;

subsequently digesting said chips in said vessel under conditions of temperature and pressure effective to initiate a lignin depolymerization reaction in said chips for a predetermined period of time;

refining said chips to produce said pulp; and

separating the used solution from the pulp for chemical reactant recovery.

10. The process of claim 8 wherein said monoethanolamine is present in a ratio to ammonium hydroxide of 1 to about 3 parts by weight.

12. The process of claim 10 wherein said solution and chips are present in a ratio of about 600 gallons to 2,000-3,000 pounds chips.

14. A continuous process for producing corrugating medium pulp from hardwood chips comprising:

providing a pulping solution of a dilute aqueous mixture of 1 part of a lower alkanolamine and less than 3 parts ammonium hydroxide;

providing a heated vessel;

admitting a predetermined quantity of chips to said vessel;

heating said solution;

subsequently digesting said chips in said vessel under conditions of temperature and pressure effective to initiate alignin depolymerization reaction in said chips for a predetermined period of time;

refining said chips to produce said pulp; and

separating the used solution from the pulp for chemical reactant recovery.