US2011108222A1PendingUtilityA1
Effect of low dose xylanase on pulp in prebleach treatment process
Est. expiryNov 11, 2029(~3.3 yrs left)· nominal 20-yr term from priority
D21C 5/005D21C 9/14D21H 11/00D21H 17/005D21C 9/10
52
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Claims
Abstract
A prebleach treatment of pulp with xylanase enzyme prior to chemical bleaching is disclosed. A process of making pulp comprises treating a pulp with xylanase in an amount of less than 50 g of xylanase per ton of pulp. The treating step is carried while buffering the pulp and xylanase with a buffering agent to a pH of from about 6.5 to about 7.5 prior to at least one bleaching stage to form a treated pulp.
Claims
exact text as granted — not AI-modified1 . A process of making pulp comprising:
treating a pulp with xylanase in an amount of less than 50 g of xylanase per ton of pulp, wherein the treating step is carried while buffering the pulp and xylanase with a buffering agent to a pH of from about 6.5 to about 7.5 prior to at least one bleaching stage to form a treated pulp.
2 . The process of claim 1 wherein the pulp is unbleached.
3 . The process of claim 1 wherein the xylanase is luminase enzyme.
4 . The process of claim 1 wherein the luminase is endo-β-1,4-xylanase.
5 . The process of claim 1 wherein the pulp is treated with the xylanase in an amount from about 10 g to about 50 g per ton of pulp.
6 . The process of claim 3 wherein the pulp is treated with the xylanase in an amount from about 30 g to about 50 g per ton of pulp.
7 . The process of claim 1 wherein the buffering agent is selected from a group of carbon dioxide (CO 2 ) and H 2 SO 4 .
8 . The process of claim 1 wherein the pulp is subjected to a first bleaching stage (D o ) after the treating step.
9 . The process of claim 8 wherein the treated pulp causes 10 to 30% reduction of bleaching chemicals in first bleaching stage (D o ) without causing an increase in pulp yield loss and bleached filtrate Chemical Oxygen Demand (COD) loading as compared with a pulp not being treated in accordance to claim 1 .
10 . The process of claim 8 wherein the treated pulp after the first bleaching stage step (D o ) is subjected to an Eop bleaching stage.
11 . The process of claim 10 wherein the treated pulp permits a reduction of pH by 2 units in the subsequent Eop bleaching stage to minimize the filtrate Chemical Oxygen Demand (COD) filtration as compared with a pulp not being treated in accordance to claim 1 .
12 . The process of claim 11 wherein the pH of treated pulp in Eop bleaching stage is from about 9 to about 11.
13 . The process of claim 10 wherein the treated pulp permits a reduction of temperature by 15° C. in the Eop bleaching stage as compared with a pulp not being treated in accordance to claim 1 .
14 . The process of claim 13 wherein the temperature in the Eop bleaching stage is from about 55° C. to about 85° C.
15 . The process of claim 1 wherein the xylanase is added to the pulp at and/or after the pulp is washed.
16 . The process of claim 1 wherein the buffering agent is added to the pulp simultaneously with, prior to, or after the xylanase is added to the pulp.
17 . The process of claim 1 wherein the retention time for the treating step of the pulp is from about 15 min. to about 240 min.
18 . The process of claim 1 wherein the temperature for the treating step of the pulp is from about 40° C. to about 70° C.
19 . The process of claim 1 wherein the consistency for the treating step is from about 2% to about 15%.
20 . The process of claim 1 wherein the treated pulp ISO brightness is at least about 2 to 5% greater than the brightness of the pulp made by the same or substantially the same bleaching processes without the pulp being treated in accordance to claim 1 .
21 . The process of claim 1 wherein treating the pulp with xylanase in an amount from 10 g to of 50 g of xylanase per ton of pulp and wherein the treating step is carried while buffering the pulp and xylanase with a buffering agent to a pH of from about 6.5 to about 7.5 prior to at least one bleaching stage.
22 . The process of claim 21 wherein treating the pulp with xylanase in an amount from 10 g to of 15 g of xylanase per ton of pulp and wherein the treating step is carried while buffering the pulp and xylanase with a buffering agent to a pH of from about 6.8 to about 7.2 prior to at least one bleaching stage.
23 . The process of claim 1 further comprising a step of recycling unused enzyme from a prewasher and added to an outlet of a washer for pH control.
24 . In a pulp bleaching system comprising at least one Do stage and at least one Eop bleaching stage, a prebleach treatment stage which comprises:
pulp; xylanase in an amount of less than 50 g of xylanase per ton of pulp; and a buffering agent being used buffering the pulp and xylanase to provide a pH in the prebleach treatment stage from about 6.5 to about 7.5.Join the waitlist — get patent alerts
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