Process of purifying wood pulp with caustic-borate solution and recovering the purifying chemical
View Patent ↗Systems and methods for purifying wood pulp by caustic-borate extraction. The systems and method include a method for recovering both the caustic and borate compounds from the resultant hemicaustic effluent, so that they may be recycled and re-used. Efficient recovery of these components is enabled by a nanofiltration system that has one or more alkali-resistant nanofiltration membranes.
1. A method of recovering a caustic-borate extraction solution from a hemicaustic effluent stream comprising:
providing an aqueous hemicaustic stream comprising a caustic compound, a borate compound, and hemicellulose, wherein the hemicaustic stream has a pH greater than 12;
providing a nanofiltration system comprising at least one but no more than three alkali-resistant nanofiltration membranes;
passing the aqueous hemicaustic stream through the nanofiltration system to produce a permeate stream comprising the caustic compound, the borate compound, and hemicellulose,
wherein less than about 20% by weight of the hemicellulose in the hemicaustic stream passes through the nanofiltration system to the permeate stream, and the borate concentration of the permeate stream is from about 60% to about 95% of the borate concentration of the hemicaustic stream, and greater than about 50% by weight of the caustic in the hemicaustic stream passes through the nanofiltration system to the permeate stream.
2. The method of claim 1 , wherein the aqueous hemicaustic stream comprises up to about 20 weight % caustic, and up to about 8 weight % borate.
3. The method of claim 1 , wherein the aqueous hemicaustic stream comprises from about 0.5 weight % to about 7 weight % of hemicellulose.
4. The method of claim 1 , wherein the permeate stream comprises up to about 20 weight % caustic, and up to about 8 weight % borate.
5. The method of claim 1 , wherein the permeate stream comprises less than about 0. 5 weight % hemicellulose.
6. The method of claim 1 , wherein a concentrate stream is produced from that portion of the hemicaustic stream that does not permeate the nanofiltration system, wherein the concentrate stream comprises from about 2 weight % to about 30 weight % hemicellulose.
7. The method of claim 1 , wherein the nanofiltration system comprises at least one nanofiltration membrane capable of excluding compounds having a molecular weight greater than about 200.
8. The method of claim 1 , wherein the nanofiltration system comprises at least one nanofiltration membrane comprising a polymer selected from the group consisting of polyether sulfone, polysulfone, polyarylether sulfone, polyvinylidene fluoride, polyvinyl chloride, polyketone, polyether ketone, polytetrafluoro ethylene, polypropylene, polyamide, and any combination or mixture thereof.
9. The method of claim 1 , wherein at least about 60% of the volume of the hemicaustic stream is recovered in the permeate stream.
10. The method of claim 1 , further comprising the step of concentrating the permeate stream by removing water, to increase the concentration of caustic and borate.
11. The method of claim 10 , wherein the step of concentrating the permeate comprises introducing the permeate stream to at least one evaporator unit.
12. The method of claim 10 , wherein the concentration of caustic in the concentrated permeate from about 25 weight % to about 50 weight %, and the concentration of borate in the concentrated permeate is from about 1 weight % to about 25 weight %.
13. The method of claim 1 , wherein said step of providing an aqueous hemicaustic stream further comprises:
providing cellulose fibers containing hemicellulose;
providing an extraction liquor comprising an aqueous solution of caustic and borate;
combining the cellulose fibers and the extraction liquor to produce a caustic-borate cellulose fiber slurry;
extracting the caustic-borate cellulosic fiber slurry for a sufficient amount of time to dissolve and extract the hemicellulose from the cellulosic fibers and into the extraction liquor;
washing the extracted cellulose slurry to produce a hemicaustic stream comprising the spent extraction liquor and the dissolved hemicellulose.
14. The method of claim 13 , wherein the cellulose fibers are provided in an aqueous slurry having a consistency of less than about 10%.
15. The method of claim 13 , wherein the step of combining the cellulose fibers and extraction liquor comprises passing the cellulose fibers through at least one washer unit through which the caustic-borate extraction liquor is introduced in a counter-current direction to the cellulosic fibers.
16. The method of claim 14 , wherein the step of combining the cellulose fibers and extraction liquor comprises pressing the cellulose fiber slurry to increase the consistency of the slurry to about 30% to about 40%, and thereafter combining the concentrated cellulose slurry with a caustic-borate extraction liquor.
17. The method of claim 13 , wherein the caustic-borate cellulose slurry comprises from about 2 weight % to about 20 weight % caustic.
18. The method of claim 13 , wherein the caustic-borate cellulose slurry comprises from about 7 weight % to about 14 weight % caustic compound.
19. The method of claim 13 , wherein the caustic-borate cellulose slurry comprises from about 0.5 weight % to about 10 weight % borate.
20. The method of claim 13 , wherein the caustic-borate cellulosic slurry has a pH of about 14.
21. The method of claim 13 , wherein the step of extracting the caustic-borate cellulose slurry is performed at a temperature of from about 20° C. to about 100° C.
22. The method of claim 13 , wherein the step of washing comprises passing the extracted cellulose slurry through at least one washer that applies wash water to the extracted cellulose slurry, and removes a substantial portion of the spent caustic-borate extraction solution, and removes a substantial portion of the hemicellulose from the slurry.
23. The method of claim 13 , wherein at least a portion of the hemicaustic stream is diverted and combined with the cellulose slurry before the extraction step.