US2008110584A1PendingUtilityA1

Bleaching process with at least one extraction stage

Assignee: YIN CAIFANGPriority: Nov 15, 2006Filed: Nov 15, 2006Published: May 15, 2008
Est. expiryNov 15, 2026(~0.3 yrs left)· nominal 20-yr term from priority
Inventors:Caifang Yin
D21C 9/147D21C 9/163D21C 9/1042
46
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Claims

Abstract

An improved bleaching process for bleaching pulp having at least one Eop stage or Ep stage which comprises subjecting the pulp to a Q stage in which the pulp is treated with a chelating agent at a pH of from greater than 2.5 to less than 7 followed by interstage washing prior to treating the pulp in the Eop or Ep stage. Q stage washing can be at any stage in the process provided that Q stage occurs prior to Eop or Ep stage. For example, Q stage washing may occur after brownstock washing at prior to any delignification stage. Q stage washing can also occur after earlier delignification stages or an oxygen delignification stage or a Do delignification stage. Q stage washing immediately preceding the Eop or Ep stage, or can be separated from these stages by one or more other stage.

Claims

exact text as granted — not AI-modified
1 . A bleaching process for bleaching a pulp having at least one Eop stage or Ep stage, the bleaching process comprising:
 subjecting the pulp to a Q stage in which the pulp is treated with a chelating agent at a pH of from greater than 2.5 to less than 7 followed by a washing stage prior to treating the pulp in the Eop or Ep stage.   
     
     
         2 . The bleaching process of  claim 1  comprising a bleaching sequence selected from the group of the formula:
 QEop or QEp or a combination thereof, with interstage washing after the Q stage and wherein:   Q is a stage in which a pulp is treated with a chelating agent at a pH of from greater than 2.5 to less than 7,   Eop is an extraction stage in which pulp is treated with a composition comprising oxygen, base, and peroxide; and   Ep is an extraction stage in which pulp is treated with a composition comprising base and peroxide.   
     
     
         3 . The bleaching process of  claim 1  comprising a bleaching sequence selected from the group of the formula: DoQEop, DoQEp or combination thereof, without interstage washing between Do and Q stages and with interstage washing after the Q stage and wherein Do is a delignification stage in which pulp is treated with an agent comprising chlorine dioxide without elemental chlorine dioxide (ECF). 
     
     
         4 . The bleaching process of  claim 1  wherein the chelating agent is selected from the group consisting of diethylene triamine pentaacetic acid (DTPA), to aminopolycarboxylic acids (APCA), ethylenediaminetetraacetic acid (EDTA), nitrilotriacetic acid (NTA), phosphoric acids, ethylenediaminetetramethylene-phosphonic acid (EDTMP), diethylenetriaminepentamethylenephosphonic acid (DTPMP), nitrilotrimethylenephosphonic acid (NTMP), polycarboxylic acids, gluconates, citrates, polyacrylates, and polyaspartates or any combination of two or more thereof. 
     
     
         5 . The bleaching process of  claim 1  wherein the chelating agent is EDTA or DTPA. 
     
     
         6 . The bleaching process of  claim 1  wherein the chelating agent is DTPA. 
     
     
         7 . The bleaching process of  claim 1  wherein the pulp pH is from about 5.0 to about 5.50. 
     
     
         8 . The bleaching process of  claim 1  wherein the pulp consistency in the Q stage is from about 6.0% to about 10%. 
     
     
         9 . The bleaching process of  claim 1  wherein the retention time is from about 10 min. to about 300 min. 
     
     
         10 . The bleaching process of  claim 1  wherein the temperature is from about 25° C. to about 120° C. 
     
     
         11 . The bleaching process of  claim 1  wherein the pulp washing stage after the Q stage removes at least about 50% of the chelated metals. 
     
     
         12 . The bleaching process of  claim 1  wherein the pulp washing stage after the Q stage removes at least about 75% of the chelated metals. 
     
     
         13 . The bleaching process of  claim 1  wherein the pulp washing stage after the Q stage removes substantially all of the chelated metals. 
     
     
         14 . The bleaching process of  claim 1  wherein an amount of hydrogen peroxide (H 2 O 2 ) less than an amount of hydrogen peroxide (H 2 O 2 ) used in the same or substantially the same bleaching processes without the Q stage followed by a washing stage to obtain the same or substantially level of pulp brightness in the Do stage. 
     
     
         15 . The bleaching process of  claim 1  wherein the reduction in the amount of AOX is at least about 20% less than the amount of AOX produced in the same or substantially the same bleaching processes without the Q stage to obtain the same or substantially level of pulp brightness in the Eop and/or Ep stages. 
     
     
         16 . The bleaching process of  claim 1  wherein pulp viscosity is at least about 5% greater than the viscosity of the pulp made by the same or substantially the same bleaching processes without the Q stage. 
     
     
         17 . The bleaching process of  claim 1  wherein pulp brightness is at least about 7% greater than the brightness of the pulp made by the same or substantially the same bleaching processes without the Q stage.

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