Chemical efficiency increase in papermaking process
A method of increasing chemical efficiency of chemical additives in a papermaking system includes the steps of providing thick stock pulp comprising soluble lignin, process water, and at least about 2% by weight of cellulosic fiber based on total weight of thick stock pulp, and adding at least one laccase enzyme and at least one organic polymer to the thick stock pulp to reduce the amount of soluble lignin therein. The organic polymer is chosen from cationic polymers, non-ionic polymers and combinations thereof.
1. A method of increasing chemical efficiency of chemical additives in a papermaking system, said method comprising the steps of:
providing thick stock pulp comprising soluble lignin, process water, and at least 2% by weight of cellulosic fiber based on total weight of thick stock pulp, and
adding at least one laccase enzyme and at least one organic polymer chosen from the group consisting of cationic polyacrylamides, polyethyleneoxides, and combinations thereof, to the thick stock pulp to reduce the amount of soluble lignin therein;
wherein the at least one laccase enzyme is present in an amount of from 0.1 to 1 pound actives per ton of oven dried pulp and the at least one organic polymer is present in an amount of from 0.5 to 3 pounds actives per ton of oven dried pulp.
2. The method of claim 1 wherein the thick stock pulp comprises at least 3% by weight of the cellulosic fibers based on a total weight of the thick stock pulp and wherein the cellulosic fibers are derived from NSSC pulp, OCC pulp, deinked pulp, virgin fiber, mechanical pulp, unbleached Kraft pulp or combinations thereof.
3. The method of claim 1 wherein the cationic polyacrylamide is derived from at least one monomer chosen from diallyldimethylammonium chloride, N,N,N-trialkylamminoalkyl (meth)acrylate, N,N,N-trialkylamminoalkyl (meth) acrylamide, epichlorohydrin-dimethylamine and combinations thereof.
4. The method of claim 1 wherein the organic polymer is a polymer dispersion.
5. The method of claim 1 wherein the weight average molecular weight of the organic polymer is from 100,000 to 10 million Da.
6. The method of claim 1 wherein the organic polymer has a weight average molecular weight of from 1,000,000 to 10,000,000 Da.
7. The method of claim 1 wherein the organic polymer is the polyethyleneoxide polymer having a weight average molecular weight of greater than 1,000,000 and less than 10 million Da.
8. The method of claim 1 wherein the organic polymer is the cationic polyacrylamide having a weight average molecular weight of greater than 200,000 and less than 10 million Da.
9. The method of claim 1 wherein the reduction in the amount of soluble lignin in the process water is evidenced by at least a 5% reduction in absorbance in a UV-VIS spectra measured at 280 nm after 24 hours as compared to process water that is free of the at least one laccase enzyme and the at least one organic polymer and/or the process water exhibits a chemical oxygen demand that is reduced by at least 5% as compared to the chemical oxygen demand of process water that is free of the at least one laccase enzyme and the at least one organic polymer.
10. The method of claim 1 further comprising the step of adding an inorganic coagulant to the process water wherein the inorganic coagulant is chosen from aluminum sulfate, aluminum chloride, aluminum chlorohydrate, polyaluminum chloride, polyaluminum sulfate, iron (III) chloride, iron (III) sulfate, iron (II) chloride, iron (II) sulfate, polyferrous sulfate, and combinations thereof.
11. The method of claim 1 wherein the cationic polyacrylamide is a water dispersion and is present in an amount of from 0.5 to 1 pound of actives per ton of oven dried pulp.
12. The method of claim 1 wherein the laccase enzyme is present in an amount of from 0.5 to 1 pound of actives per ton of oven dried pulp.
13. The method of claim 1 wherein the cationic polyacrylamide and the laccase enzyme are present in a weight ratio of from 1:1 to 10:1 based on weight of actives.
14. The method of claim 1 wherein the cationic polyacrylamide and the laccase enzyme are present in a weight ratio of 1:1 based on weight of actives.
15. The method of claim 1 wherein the cationic polyacrylamide and the laccase enzyme are present in a weight ratio of 4:1 based on weight of actives.
16. The method of claim 1 wherein the cationic polyacrylamide and the laccase enzyme are present in a weight ratio of 3:1 based on weight of actives.
17. The method of claim 1 wherein the cationic polyacrylamide and the laccase enzyme are present in a weight ratio of 2:1 based on weight of actives.
18. The method of claim 1 wherein the polyethyleneoxide and the laccase enzyme are present in a weight ratio of 1:1 to 10:1 based on weight of actives.
19. The method of claim 1 further comprising the step of adding a drainage aid to the thick stock pulp to achieve a drainage time that is less than a drainage time achieved by a comparable thick stock pulp that also includes the drainage aid but that is free of the at least one laccase enzyme and at least one organic polymer, wherein the drainage aid is present in the thick stock pulp in an amount that is at least 50% less than an amount of the drainage aid in the comparable thick stock pulp based on weight of actives.
20. A method of increasing chemical efficiency of chemical additives in a papermaking system, said method comprising the steps of:
providing thick stock pulp comprising soluble lignin, process water, and at least 3% by weight of cellulosic fiber based on total weight of thick stock pulp, wherein the cellulosic fibers are derived from NSSC pulp, OCC pulp, deinked pulp, virgin fiber, mechanical pulp, unbleached Kraft pulp or combinations thereof, and
adding at least one laccase enzyme and at least one cationic polyacrylamide that is a water dispersion to the thick stock pulp to reduce the amount of soluble lignin therein;
wherein the at least one laccase enzyme is present in an amount of from 0.1 to 1 pound actives per ton of oven dried pulp dried furnish solids and the at least one organic polymer is present in an amount of from 0.5 to 3 pounds actives per ton of oven dried pulp.