| CPC D21H 11/20 (2013.01) [D21C 3/02 (2013.01); D21C 5/00 (2013.01); D21C 9/10 (2013.01); D21C 9/12 (2013.01); D21C 9/123 (2013.01); D21C 9/18 (2013.01); D21H 11/04 (2013.01); D21H 11/12 (2013.01); D21H 17/005 (2013.01); D21H 17/21 (2013.01); D21H 17/28 (2013.01); D21H 17/29 (2013.01); D21H 21/10 (2013.01); D21H 21/18 (2013.01); D21H 23/04 (2013.01)] | 18 Claims |

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1. Cellulose pulp obtained by a process comprising the steps of:
a) treating the cellulosic feedstock through a chemical or semi-chemical pulping process to produce brown cellulose pulp;
b) bleaching the brown cellulose pulp through a bleaching sequence to obtain a white slurry pulp;
c) adding a carbohydrate-based polymer consisting of starch to the white slurry pulp, wherein the dosage of said polymer ranges from 2 to 12 kg/ton of cellulose pulp;
d) adding at least one enzyme to the white slurry pulp already doped with the carbohydrate-based polymer to form a doped white slurry pulp, wherein the addition of the at least one enzyme (EZ) takes place according to the following conditions:
i. reaction temperature between 4° and 90° C.;
ii. reaction pH between 3.0 and 9.0;
iii. reaction time between 10 and 300 minutes;
iv. enzyme amount between 10 and 200 g of the at least one enzyme per ton of cellulose pulp;
e) conveying the doped white slurry pulp to and through a reaction tower before a drying machine; and
f) drying the doped white slurry pulp, and denaturing the at least one enzyme, to obtain the cellulose pulp; and
wherein the at least one enzyme comprises a cellulase; and
wherein the cellulose pulp has a zeta potential of about −63 mV to about −66 mV.
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10. Cellulose pulp obtained by a process comprising the steps of:
a) treating the cellulosic feedstock through a chemical or semi-chemical pulping process to produce brown cellulose pulp;
b) bleaching the brown cellulose pulp through a bleaching sequence to obtain a white slurry pulp;
c) adding at least one enzyme to the white slurry pulp, wherein the addition of the at least one enzyme (EZ) takes place according to the following conditions:
i. reaction temperature between 4° and 90° C.;
ii. reaction pH between 3.0 and 9.0;
iii. reaction time between 10 and 300 minutes;
iv. enzyme amount between 10 and 200 g of the at least one enzyme per ton of cellulose pulp;
d) adding a carbohydrate-based polymer consisting of a starch to the white slurry pulp already doped with the at least one enzyme to form a doped white slurry pulp, wherein the dosage of said polymer ranges from 2 to 12 kg/ton of cellulose pulp;
e) conveying the doped white slurry pulp to and through a reaction tower before a drying machine; and
f) drying the doped white slurry pulp, and denaturing the at least one enzyme, to obtain the cellulose pulp;
wherein the at least one enzyme comprises a cellulase; and
wherein the cellulose pulp has a zeta potential of about −63 mV to about −66 mV.
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