Lignin removal method using ozone and acetic acid

• US 5,074,960 A
• Filed: 10/31/1990
• Issued: 12/24/1991
• Est. Priority Date: 01/25/1988
• Status: Expired due to Fees

• Current Assignee: Acetocell GmbH & Company KG
• Original Assignee: Acetocell GmbH & Company KG
• Inventors: Berg, Alex, Nimz, Horst H.
• Primary Examiner(s): Hastings, Karen M.
• Application Number:
  US07/606,595
• Time in Patent Office: 419 Days
• Field of Search: 162/65, 162/65 B, 162/75, 162/76, 162/19
• US Class Current: 162/65
• CPC Class Codes: D21C 9/153 with ozone
• CPC Class Codes: D21C 9/163 with peroxides

Abstract

Lignin contained in a cellulosic or lignocellulosic pulp product is removed by contacting the product with a gaseous medium containing ozone in the presence of a liquid agent which is a lower fatty acid, such a formic, acetic or propionic acid, having only a low solvent capacity for lignin; as a consequence of this treatment, lignin which is present in the product will be converted into a lignin derivative that has an increased solubility in the fatty acid and can be removed quantitatively by extraction from the lignocellulosic material. Purified pulp can thus be obtained with increased processing efficiency and without most pollution problems of prior art processing methods because the fatty acid used as the main constituent of the processing liquid in all stages of pulp production can be circulated counter-currently through the stages of the process with purification of the acid for recirculation only after its use in the digestion step where the normal starting materials of pulp production, i.e. wood or annual plants, are treated according to the acetosolve process at ambient pressure and temperatures of below 120° to form a raw pulp product.

Claims

1. A method of bleaching a cellulosic pulp material containing a substantial amount of lignin for removal of said lignin from said cellulosic pulp material consisting essentially of the steps of:

contacting said cellulose pulp material with a gaseous medium containing ozone in the presence of a liquid processing agent comprising an aqueous acetic acid solution having an acid content of at least 50% by weight, and causing an oxidative conversion of said lignin so as to increase the solubility of said lignin in said liquid processing agent and to improve said removal of said lignin from said cellulosic pulp material.

2. The method of claim 1 wherein water is present in an amount of less than 30% by weight of said liquid processing agent.

3. The method of claim 1 wherein said liquid processing agent comprises about 90% to about 98% by weight of acetic acid and about 2% to about 10% by weight of water.

4. The method of claim 1 wherein said contacting step is effected at a temperature below about 100°

C.

5. The method of claim 1 wherein said contacting is effected at a temperature of below about 50°

C.

6. The method of claim 1 wherein said contacting is effected at a temperature in the range of from about 0°

C. to about 30°

C.

7. The method of claim 1 wherein said gaseous medium contains at least about 100 ppm of said ozone.

8. The method of claim 1 wherein said gaseous medium contains said ozone at a concentration in the range of from about 1% to about 3% by weight of said gaseous phase.

9. The method of claim 8 wherein the concentration of ozone used is about 2%.

10. A method of producing a high grade pulp from a cellulosic material containing a substantial amount of lignin consisting essentially of the steps:

digesting said cellulosic material with an aqueous liquid comprising a major amount of acetic acid and obtaining a raw pulp which includes a residual amount of lignin;

solubilizing the residual lignin in said pulp in 50% or more acetic acid aqueous liquid mixture and from about 1% to about 3% gaseous ozone; and

recovering said pulp as a substantially lignin-free pulp.

11. The method of claim 10 wherein said solubilized lignin is extracted from said pulp using acetic acid-containing aqueous liquid.

12. The method of claim 11 wherein the steps of digesting, solubilizing and extracting said lignin using acetic acid aqueous liquid is carried out counter-currently by first utilizing purified acetic acid aqueous liquid in the extracting step, and thereafter utilizing said aqueous liquid for the solubilizing and the digesting steps.

13. The method of claim 12 wherein the acetic acid aqueous liquid used in the digesting step is thereafter purified and again utilized in the extracting step.

14. The method of claim 10 wherein the concentration of acetic acid used is greater than 70%.

15. The method of claim 11 wherein the concentration of acetic acid used is greater than 70%.

16. The method of claim 12 wherein the concentration of acetic acid used is greater than 70%.

17. The method of claim 13 wherein the concentration of acetic acid used is greater than 70%.

18. The method of claim 10 wherein the concentration of acetic acid used is greater than 90%.

19. The method of claim 11 wherein the concentration of acetic acid used is greater than 90%.

20. The method of claim 12 wherein the concentration of acetic acid used is greater than 90%.

21. The method of claim 13 wherein the concentration of acetic acid used is greater than 90%.

22. The method of claim 10 wherein the recovered pulp has a kappa value of less than 5.

23. The method of claim 10 wherein the concentration of ozone used is about 2%.

24. The method of claim 11 wherein the concentration of ozone used is about 2%.

25. The method of claim 12 wherein the concentration of ozone used is about 2%.

26. The method of claim 13 wherein the concentration of ozone used is about 2%.

27. The method of claim 14 wherein the concentration of ozone used is about 2%.

28. The method of claim 15 wherein the concentration of ozone used is about 2%.

29. The method of claim 16 wherein the concentration of ozone used is about 2%.

30. The method of claim 17 wherein the concentration of ozone used is about 2%.

31. The method of claim 14 wherein the concentration of ozone used is about 2%.

32. The method of claim 15 wherein the concentration of ozone used is about 2%.

33. The method of claim 16 wherein the concentration of ozone used is about 2%.

34. The method of claim 17 wherein the concentration of ozone used is about 2%.