Manufacture of cellulosic pulp sheets
View Patent ↗A pulp making process in which fibrous cellulosic material is pulped to form an aqueous suspension of cellulosic material, the suspension is drained through a screen to form a pulp sheet and that the pulp sheet is dried to form a dry market pulp, in which a water soluble cationic polymer is added to the suspension as the sole drainage aid wherein the water-soluble cationic polymer is either, i) a copolymer comprising (a) between 1 and 70 mole % (meth) acrylamide and (b) between 30 and 99 mole % (meth) acryloyloxyethyltrimethyl ammonium chloride with an intrinsic viscosity between 5 and 9 dl/g; or ii) a hydrolysed homopolymer of vinylformamide comprising between 1 and 100 mole % vinyl amine units and having a K value of between 45 and 240. The process of the invention provides improved drainage time and solids content of the dewatered pulp.
1. A process for preparing a dry market pulp, comprising:
sulfite pulping and then bleaching a fibrous cellulosic material to form an aqueous suspension of cellulosic material,
draining the aqueous suspension of cellulosic material through a screen to form a pulp sheet, and then
drying the pulp sheet to form a dry market pulp,
wherein
a water soluble cationic polymer is added to the aqueous suspension of cellulosic material as the sole drainage aid, and
the water-soluble cationic polymer comprises a hydrolyzed homopolymer of vinylformamide comprising between 5 and 30 mole % vinyl amine units and having a K value of between 120 and 240.
2. The process of claim 1 , wherein the water-soluble cationic polymer is the hydrolyzed homopolymer of vinylformamide having a K value of between 120 and 180.
3. The process of claim 1 , wherein the water-soluble cationic polymer is added to the aqueous cellulosic suspension in an amount between 0.05% and 1.5% based on the dry weight of suspension.
4. The process of claim 1 , wherein the hydrolyzed homopolymer of vinylformamide comprises 20 mole % to 30 mole % vinyl amine units.
5. The process of claim 1 , wherein the water-soluble cationic polymer is added at dose of at least 0.01% based on the weight of the water-soluble cationic polymer and the weight of the dried aqueous suspension of cellulosic material.
6. The process of claim 1 , wherein the water-soluble cationic polymer is added at dose of at least 0.02% based on the weight of the water-soluble cationic polymer and the weight of the dried aqueous suspension of cellulosic material.
7. The process of claim 1 , wherein the water-soluble cationic polymer is added at dose of at least 0.025% based on the weight of the water-soluble cationic polymer and the weight of the dried aqueous suspension of cellulosic material.
8. The process of claim 1 , wherein the water-soluble cationic polymer is added at dose of at least 0.03% based on the weight of the water-soluble cationic polymer and the weight of the dried aqueous suspension of cellulosic material.
9. The process of claim 1 , wherein the water-soluble cationic polymer is added at dose of 0.01% to 0.3% based on the weight of the water-soluble cationic polymer and the weight of the dried aqueous suspension of cellulosic material.
10. The process of claim 1 , wherein the aqueous suspension of cellulosic material has a concentration of solids of at least 1% based on the total weight of the suspension.
11. The process of claim 1 , wherein the aqueous suspension of cellulosic material is prepared after bleaching by combining the cellulosic material with warm water at a temperature of 40° C. to 95° C.
12. The process of claim 1 , wherein the aqueous suspension of cellulosic material is prepared after bleaching by combining the cellulosic material with warm water at a temperature of 50° C. to 80° C.
13. The process of claim 1 , wherein the aqueous suspension of cellulosic material is prepared after bleaching by combining the cellulosic material with warm water at a temperature of 60° C. to 80° C.