Process of producing high-yield pulp
View Patent ↗The present invention relates to a process for preparing a high-yield pulp comprising a) treating a lignocellulose containing material chemically by means of an oxidizing system comprising at least one non-enzymatic oxidant substantially free from ozone and chlorine dioxide and an activator at a pH from about 2 to about 6.5; and b) treating the lignocellulose containing material mechanically for a time sufficient to produce a high-yield pulp, wherein the lignocellulose containing material is chemically treated prior to and/or during any mechanical treatment stage, and wherein the lignocellulose containing material is not chemically treated at a pH from about 11.5 to about 14 between stages a) and b).
1. A process for preparing a high-yield pulp for papermaking selected from mechanical pulp (MP), refiner mechanical pulp (RMP), pressurized refiner mechanical pulp (PRMP), thermomechanical pulp (TMP), thermomechanical chemical pulp (TMCP), high-temperature TMP (HT-TMP) RTS-TMP, Thermopulp, groundwood pulp (GW), stone groundwood pulp (SGW), pressure groundwood pulp (PGW), super pressure groundwood pulp (PGW-S), thermo groundwood pulp (TGW), thermo stone groundwood pulp (TSGW), chemimechanical pulp (CMP), chemirefinermechanical pulp (CRMP), chemithermomechanical pulp (CTMP), high-temperature CTMP (HT-CTMP), sulphite-modified thermomechanical pulp (SMTMP), reject CTMP (CTMP R ), groundwood CTMP (G-CTMP), high-yield sulphite pulp (HYS), biomechanical pulp (BRMP), pulps produced according to the OPCO process, Bi-Vis process, dilution water sulfonation process (DWS), sulfonated long fibres process (SLF), chemically treated long fibres process (CTLF), long fibre CMP process (LFCMP) or any modifications and combinations thereof comprising
a) treating a lignocellulose containing material selected from wood particles and/or fibers chemically by means of an oxidising system comprising at least one non-enzymatic oxidant selected from inorganic or organic peroxy compounds or hydrogen peroxide generating compounds substantially free from ozone and chlorine dioxide in an amount from about 0.1 to about 5 wt % based on the weight of the lignocellulose containing material and an activator in an amount from about 0.0001 to about 1 wt % based on the weight of the lignocellulose containing material at a pH from about 2 to about 6.5; and
b) treating the lignocellulose containing material mechanically in at least two or more stages for a time sufficient to produce a high-yield pulp, wherein the energy input to said at least two or more stages is at least 1150 kWh/bdmt and up to about 5000 kWh/bdmt, wherein the lignocellulose containing material is chemically treated by adding the non-enzymatic oxidant and activator to the lignocellulose containing material prior to and/or during any mechanical treatment stage, and wherein the lignocellulose containing material is not chemically treated at a pH from about 11.5 to about 14 between stages a) and b), wherein the activator is selected from transition metal ions and wherein the lignocellulosic containing material is treated at a temperature from 80 to 180° C.
2. A process according to claim 1 , wherein the pH is from about 2.5 to about 6.
3. A process according to claim 1 , wherein the pH is from about 3 to about 5.5.
4. A process according to claim 1 wherein the high-yield pulp is mechanical pulp, refiner mechanical pulp, groundwood pulp, chemimechanical pulp, semichemical pulp, thermomechanical and/or chemithermomechanical pulp.
5. A process according to claim 1 , wherein said lignocellulose containing material comprises non-defibrated wood.
6. A process according to claim 1 , wherein the lignocellulose containing material comprises mechanically treated lignocellulose containing material.
7. A process according to claim 1 , wherein the oxidising system is applied between two mechanical treatment stages.
8. A process according to claim 1 , wherein the lignocellulose containing material comprises softwood and/or hardwood.
9. A process according to claim 1 , wherein the lignocellulose containing material comprises softwood.
10. A process according to claim 1 , wherein the non-enzymatic oxidant is selected from peroxy compounds.
11. A process according claim 1 , wherein the non-enzymatic oxidant is hydrogen peroxide.
12. A process according to claim 1 , wherein the oxidising system comprises an activator selected from metal ions, TAED, cyanamide, or combinations thereof.
13. A process according to claim 1 , wherein the oxidising system further comprises an enhancer selected from nitrogen-containing polycarboxylic acids, nitrogen-containing polyphosphonic acids, nitrogen-containing polyalcohols, oxalic acid, oxalate, glycolate, ascorbic acid, citric acid, nitrilo acetate, gallic acid, fulvic acid, itaconic acid, haemoglobin, hydroxybenzenes, catecholates, quinolines, dimethoxybenzoic acids, dihydroxybenzoic acids, dimethoxybenzylalcohols, pyridine, histidylglycine, phthalocyanine, acetonitril, 18-crown-6 ether, mercaptosuccinic acid, cyclohexadienes, polyoxomethalates, and combinations thereof.
14. A process according claim 1 wherein the oxidising system further comprises an enhancer selected from EDTA, DTPA, NTA, and combinations thereof.
15. The process of claim 1 , wherein the non-enzymatic oxidant and activator are added to the lignocellulose containing material during at least one refining stage.
16. A process for preparing a high-yield pulp for papermaking selected from mechanical pulp (MP), refiner mechanical pulp (RMP), pressurized refiner mechanical pulp (PRMP), thermomechanical pulp (TMP), thermomechanical chemical pulp (TMCP), high-temperature TMP (HT-TMP) RTS-TMP, Thermopulp, groundwood pulp (GW), stone groundwood pulp (SGW), pressure groundwood pulp (PGW), super pressure groundwood pulp (PGW-S), thermo groundwood pulp (TGW), thermo stone groundwood pulp (TSGW), chemimechanical pulp (CMP), chemirefinermechanical pulp (CRMP), chemithermomechanical pulp (CTMP), high-temperature CTMP (HT-CTMP), sulphite-modified thermomechanical pulp (SMTMP), reject CTMP (CTMP R ), groundwood CTMP (G-CTMP), high-yield sulphite pulp (HYS), biomechanical pulp (BRMP), pulps produced according to the OPCO process, Bi-Vis process, dilution water sulfonation process (DWS), sulfonated long fibres process (SLF), chemically treated long fibres process (CTLF), long fibre CMP process (LFCMP) or any modifications and combinations thereof comprising
a) treating a lignocellulose containing material selected from wood particles and/or fibers chemically by means of an oxidising system comprising at least one non-enzymatic oxidant selected from inorganic or organic peroxy compounds or hydrogen peroxide generating compounds substantially free from ozone and chlorine dioxide in an amount from about 0.1 to about 5 wt % based on the weight of the lignocellulose containing material, an activator in an amount from about 0.0001 to about 0.1 wt % based on the weight of the lignocellulose containing material, and an enhancer selected from EDTA, DTPA, NTA, and combinations thereof in an amount from about 0.05 to about 0.3 wt % based on the weight of the lignocellulose containing material, at a pH from about 2 to about 6.5; and
b) treating the lignocellulose containing material mechanically in at least two or more stages for a time sufficient to produce a high-yield pulp, wherein the energy input to said at least two stages is at least 1150 kWh/bdmt and up to about 5000 kWh/bdmt wherein the lignocellulose containing material is chemically treated by adding the non-enzymatic oxidant and activator to the lignocellulose containing material prior to and/or during any mechanical treatment stage, and wherein the lignocellulose containing material is not chemically treated at a pH from about 11.5 to about 14 between stages a) and b), wherein the activator is selected from transition metal ions, and wherein the lignocellulosic containing material is treated at a temperature from 80 to 180° C.
17. A process for preparing a high-yield pulp for papermaking selected from mechanical pulp (MP), refiner mechanical pulp (RMP), pressurized refiner mechanical pulp (PRMP), thermomechanical pulp (TMP), thermomechanical chemical pulp (TMCP), high-temperature TMP (HT-TMP) RTS-TMP, Thermopulp, groundwood pulp (GW), stone groundwood pulp (SGW), pressure groundwood pulp (PGW), super pressure groundwood pulp (PGW-S), thermo groundwood pulp (TGW), thermo stone groundwood pulp (TSGW), chemimechanical pulp (CMP), chemirefinermechanical pulp (CRMP), chemithermomechanical pulp (CTMP), high-temperature CTMP (HT-CTMP), sulphite-modified thermomechanical pulp (SMTMP), reject CTMP (CTMP R ), groundwood CTMP (G-CTMP), high-yield sulphite pulp (HYS), biomechanical pulp (BRMP), pulps produced according to the OPCO process, Bi-Vis process, dilution water sulfonation process (DWS), sulfonated long fibres process (SLF), chemically treated long fibres process (CTLF), long fibre CMP process (LFCMP) or any modifications and combinations thereof comprising
a) treating a lignocellulose containing material selected from wood particles and/or fibers chemically by means of an oxidising system comprising at least one non-enzymatic oxidant comprising hydrogen peroxide and being substantially free from ozone and chlorine dioxide in an amount from about 0.1 to about 5 wt % based on the weight of the lignocellulose containing material and an activator in an amount from about 0.0001 to about 1 wt % based on the weight of the lignocellulose containing material at a pH from about 2 to about 6.5; and
b) treating the lignocellulose containing material mechanically in at least two or more stages for a time sufficient to produce a high-yield pulp wherein the energy input to said at least two stages is at least 1150 kWh/bdmt and up to about 5000 kWh/bdm, wherein the lignocellulose containing material is chemically treated by adding the non-enzymatic oxidant and activator to the lignocellulose containing material prior to and/or during any mechanical treatment stage, and wherein the lignocellulose containing material is not chemically treated at a pH from about 11.5 to about 14 between stages a) and b), wherein the activator is selected from transition metal ions, and wherein the lignocellulosic containing material is treated at a temperature from 80 to 180° C.
18. The process of claim 17 , wherein the energy input is at least 1200 kWh/bdmt.
19. A process according to claim 17 , wherein the non-enzymatic oxidant further comprises halogen containing oxidants, oxygen, nitrogen oxides, and combinations thereof.