Method and apparatus for pulp yield enhancement

Abstract

The process of the present invention purposefully precipitates a portion of the dissolved lignin onto pulp fibers to improve pulp yield of unbleached pulp. The resulting retention of lignin on the pulp creates an increase in pulp yield. Washing the pulp in a series of washer stages sequentially removes entrained lignin. Between each of the washer stages, adding dilution water repulps a pulp mat that exits from a prior washer stage and creates a pulp stream for a next washer stage. After at least one of the washer stages, adding an acidifying agent to the pulp stream forms a pulp product by precipitating the entrained lignin onto cellulosic fibers contained in the pulp stream. Finally, the process removes the pulp product from the series of washer stages with the pulp product having at least about a 1 unit increase in Kappa number.

1 . A method for processing alkaline cellulosic pulp to cause a precipitation of lignin onto pulp fibers, comprising the steps of: 
 (a) washing the pulp in a series of washer stages to sequentially remove entrained lignin therefrom;    (b) between each washer stage, adding dilution water to repulp a pulp mat exiting from a prior washer stage and to create a pulp stream for a next washer stage, said pulp stream containing said entrained lignin;    (c) after at least one of the washer stages, adding an acidifying agent to said pulp stream to form a pulp product by precipitating said entrained lignin onto cellulosic fibers contained in said pulp stream; and    (d) removing said pulp product from said series of washer stages with said pulp product having at least about a 1 unit increase in Kappa number, said increase in Kappa number arising from said precipitating of said entrained lignin.    
     
     
         2 . The method as recited in    claim 1   , wherein said acidifying agent is added to said pulp stream having a concentration of said entrained lignin in a range from about 0.2 to about 5 grams per liter.  
     
     
         3 . The method as recited in    claim 1   , wherein a sufficient amount of said entrained lignin is precipitated in said pulp stream to increase Kappa number of said pulp product from about 2.5 to about 50 units.  
     
     
         4 . The method as recited in    claim 1   , wherein said acidifying agent is carbon dioxide.  
     
     
         5 . The method as recited in    claim 4   , wherein a sufficient amount of said entrained lignin is precipitated in said pulp stream to increase Kappa number of said pulp product from about 5 to about 30 units.  
     
     
         6 . The method as recited in    claim 4   , wherein said acidifying agent is added to said pulp stream having a concentration of said entrained lignin in a range from about 0.5 to about 2 grams per liter.  
     
     
         7 . The method as recited in    claim 1   , wherein said acidifying agent is added to a repulper between succeeding washing stages.  
     
     
         8 . The method as recited in    claim 1   , wherein said adding of said acidifying agent precipitates said entrained lignin after at least two washing stages and increases Kappa number by at least about one after each of said at least two washing stages.  
     
     
         9 . The method as recited in    claim 1   , wherein said method is carried out in a three washer system and said acidifying agent is added to a repulper between second and third washing stages.  
     
     
         10 . Apparatus for processing alkaline cellulosic pulp to cause a precipitation of lignin onto pulp fibers, including a series of washer stages for washing the pulp in a series of washer stages to sequentially remove entrained lignin therefrom, said apparatus comprising: 
 first means positioned between each washer stage for adding dilution water to repulp a pulp mat that exits from a prior washer stage and to create a pulp stream for a next washer stage, said pulp stream containing the entrained lignin; and    second means positioned after at least one of the washer stages for adding an acidifying agent to said pulp stream for forming a pulp product by precipitating the entrained lignin onto cellulosic fibers in said pulp stream, and for having said pulp product removed from the series of washer stages containing at least about a 1 unit increase in Kappa number, said increase in Kappa number arising from said precipitating of the entrained lignin.    
     
     
         11 . The apparatus as recited in    claim 10   , wherein said second means adds acidifying agent to said pulp stream having a concentration of the entrained lignin in a range from about 0.2 to about 5 grams per liter.  
     
     
         12 . The apparatus as recited in    claim 10   , wherein said second means precipitates a sufficient amount of the entrained lignin in said pulp stream for increasing Kappa number of said pulp product from about 2.5 to about 50 units.  
     
     
         13 . The apparatus as recited in    claim 10   , wherein said acidifying agent is carbon dioxide.  
     
     
         14 . The apparatus as recited in    claim 13   , wherein said second means precipitates a sufficient amount of the entrained lignin in said pulp stream for increasing Kappa number of said pulp product from about 5 to about 30 units.  
     
     
         15 . The apparatus as recited in    claim 13   , wherein said second means adds acidifying agent to said pulp stream having a concentration of the entrained lignin in a range from about 0.5 to about 2 grams per liter.  
     
     
         16 . The apparatus as recited in    claim 10   , wherein said second means includes a repulper for adding said acidifying agent.  
     
     
         17 . The apparatus as recited in    claim 10   , wherein said second means is for adding said acidifying agent for said precipitating of the entrained lignin after at least two washing stages and for increasing Kappa number by at least about 1 after each of said at least two washing stages.  
     
     
         18 . The apparatus as recited in    claim 10   , wherein the series of washing stages consists of a three washer system and said acidifying agent is added by said second means to a repulper between second and third washing stages.