US2010224336A1PendingUtilityA1
Process of bleaching a wood pulp
Assignee: UNIV MAINE SYS BOARD TRUSTEESPriority: Dec 14, 2005Filed: Apr 28, 2010Published: Sep 9, 2010
Est. expiryDec 14, 2025(expired)· nominal 20-yr term from priority
D21C 9/1042D21C 9/153
30
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Claims
Abstract
A process of bleaching a wood pulp includes contacting the pulp with ozone to delignify the pulp in an ozone bleaching stage. A phosphonate chelant is added to the pulp so that the chelant is present with the pulp during the bleaching stage. The process excludes washing of the pulp to remove chelant between the chelant addition and the bleaching stage.
Claims
exact text as granted — not AI-modified1 . A process of bleaching a wood pulp comprising:
in an ozone bleaching stage, contacting the wood pulp with ozone to delignify the pulp; and adding a phosphonate chelant to the pulp so that the chelant is present with the pulp during the bleaching stage; the process excluding washing of the pulp to remove chelant between the chelant addition and the bleaching stage.
2 . The process of claim 1 wherein the phosphonate chelant comprises an ethane 1-hydroxy diphosphonate.
3 . The process of claim 2 wherein the phosphonate chelant comprises a blend of a second phosphonate chelant with the ethane 1-hydroxy diphosphonate.
4 . The process of claim 2 wherein the phosphonate chelant consists solely of the ethane 1-hydroxy diphosphonate.
5 . The process of claim 1 wherein the phosphonate chelant is present during the bleaching stage at a concentration within a range of from about 50 ppm to about 12,000 ppm.
6 . The process of claim 5 wherein the chelant concentration is within a range of from about 500 ppm to about 3,000 ppm.
7 . The process of claim 1 wherein the ozone charge during the ozone bleaching stage is within a range of from about 0.1% to about 1%.
8 . The process of claim 7 wherein ozone charge is within a range of from about 0.2% to about 0.8%.
9 . The process of claim 1 wherein the ozone bleaching stage is conducted at a temperature within a range of from about 50° F. to about 150° F.
10 . The process of claim 1 wherein the selectivity of the delignification is improved by at least about 10% compared to the same process without the chelant.
11 . The process of claim 10 wherein the selectivity of the delignification is improved by at least about 30%.
12 . The process of claim 1 wherein the ozone bleaching stage excludes a peroxide bleaching agent.
13 . The process of claim 12 wherein the ozone bleaching stage excludes all delignification agents besides the ozone.
14 . The process of claim 1 wherein the pH of the pulp at the end of the bleaching stage is within a range of from about 1 to about 7.
15 . The process of claim 1 wherein the ozone bleaching stage is conducted without the use of cyanamide or cyanamide salt.
16 . A process of bleaching a wood pulp comprising:
in an ozone bleaching stage, contacting the wood pulp with ozone to delignify the pulp, the ozone charge during the ozone bleaching stage being within a range of from about 0.1% to about 1%; and adding a phosphonate chelant which comprises an ethane 1-hydroxy diphosphonate to the pulp so that the chelant is present with the pulp during the bleaching stage; the process excluding washing of the pulp to remove chelant between the chelant addition and the bleaching stage; the process improving the selectivity of the delignification at least about 30% compared to the same process without the addition of the chelant.
17 . The process of claim 16 wherein the phosphonate chelant consists solely of the ethane 1-hydroxy diphosphonate.
18 . The process of claim 17 wherein the chelant concentration is within a range of from about 500 ppm to about 3,000 ppm.
19 . The process of claim 18 wherein ozone charge is within a range of from about 0.2% to about 0.8%.
20 . The process of claim 19 wherein the ozone bleaching stage is conducted at a temperature within a range of from about 50° F. to about 150° F.Join the waitlist — get patent alerts
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