EP3122931A1 - Verfahren zur herstellung von gebleichtem holzfaserstoff - Google Patents
Verfahren zur herstellung von gebleichtem holzfaserstoffInfo
- Publication number
- EP3122931A1 EP3122931A1 EP15711458.8A EP15711458A EP3122931A1 EP 3122931 A1 EP3122931 A1 EP 3122931A1 EP 15711458 A EP15711458 A EP 15711458A EP 3122931 A1 EP3122931 A1 EP 3122931A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- salt
- wood
- wood pulp
- composition
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- 239000000463 material Substances 0.000 title claims abstract description 18
- 229920002522 Wood fibre Polymers 0.000 title abstract description 3
- 238000000034 method Methods 0.000 claims abstract description 42
- 239000002023 wood Substances 0.000 claims abstract description 38
- 239000000203 mixture Substances 0.000 claims abstract description 34
- 150000003839 salts Chemical class 0.000 claims abstract description 21
- -1 sodium tetrahydridoborate Chemical compound 0.000 claims abstract description 21
- 239000002245 particle Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000000126 substance Substances 0.000 claims abstract description 11
- 238000000227 grinding Methods 0.000 claims abstract description 9
- 239000000654 additive Substances 0.000 claims abstract description 5
- 239000007844 bleaching agent Substances 0.000 claims abstract description 4
- 150000001875 compounds Chemical class 0.000 claims abstract description 4
- 230000001590 oxidative effect Effects 0.000 claims abstract description 4
- 238000009896 oxidative bleaching Methods 0.000 claims abstract description 3
- 238000009895 reductive bleaching Methods 0.000 claims abstract description 3
- WQDSRJBTLILEEK-UHFFFAOYSA-N sulfurous acid Chemical compound OS(O)=O.OS(O)=O WQDSRJBTLILEEK-UHFFFAOYSA-N 0.000 claims abstract 2
- 229920001131 Pulp (paper) Polymers 0.000 claims description 40
- 239000000123 paper Substances 0.000 claims description 24
- RMGVZKRVHHSUIM-UHFFFAOYSA-N dithionic acid Chemical compound OS(=O)(=O)S(O)(=O)=O RMGVZKRVHHSUIM-UHFFFAOYSA-N 0.000 claims description 21
- 229910052783 alkali metal Inorganic materials 0.000 claims description 12
- JVBXVOWTABLYPX-UHFFFAOYSA-L sodium dithionite Chemical compound [Na+].[Na+].[O-]S(=O)S([O-])=O JVBXVOWTABLYPX-UHFFFAOYSA-L 0.000 claims description 10
- 241000771208 Buchanania arborescens Species 0.000 claims description 2
- 230000032798 delamination Effects 0.000 claims description 2
- 239000000049 pigment Substances 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims 1
- GRWZHXKQBITJKP-UHFFFAOYSA-N dithionous acid Chemical compound OS(=O)S(O)=O GRWZHXKQBITJKP-UHFFFAOYSA-N 0.000 abstract description 6
- 239000012279 sodium borohydride Substances 0.000 abstract description 2
- 229910000033 sodium borohydride Inorganic materials 0.000 abstract description 2
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 16
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 11
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 10
- 239000011734 sodium Substances 0.000 description 9
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical class OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 8
- 238000004061 bleaching Methods 0.000 description 8
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 8
- 239000011122 softwood Substances 0.000 description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 7
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 7
- 150000001447 alkali salts Chemical class 0.000 description 7
- 229910052791 calcium Inorganic materials 0.000 description 7
- 239000011575 calcium Substances 0.000 description 7
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 7
- 239000006185 dispersion Substances 0.000 description 7
- 239000011121 hardwood Substances 0.000 description 7
- 229910052744 lithium Inorganic materials 0.000 description 7
- 159000000003 magnesium salts Chemical class 0.000 description 7
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 6
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 6
- 229910052708 sodium Inorganic materials 0.000 description 6
- 229910000029 sodium carbonate Inorganic materials 0.000 description 6
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 5
- 235000011613 Pinus brutia Nutrition 0.000 description 5
- 241000018646 Pinus brutia Species 0.000 description 5
- 150000001340 alkali metals Chemical class 0.000 description 5
- 150000007514 bases Chemical class 0.000 description 5
- 241000036317 Callitris verrucosa Species 0.000 description 4
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 4
- 240000009002 Picea mariana Species 0.000 description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 4
- YDONNITUKPKTIG-UHFFFAOYSA-N [Nitrilotris(methylene)]trisphosphonic acid Chemical compound OP(O)(=O)CN(CP(O)(O)=O)CP(O)(O)=O YDONNITUKPKTIG-UHFFFAOYSA-N 0.000 description 4
- 150000001342 alkaline earth metals Chemical class 0.000 description 4
- 239000013256 coordination polymer Substances 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 229910052700 potassium Inorganic materials 0.000 description 4
- 239000011591 potassium Substances 0.000 description 4
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 159000000000 sodium salts Chemical class 0.000 description 4
- 235000010265 sodium sulphite Nutrition 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 235000017997 Picea mariana var. mariana Nutrition 0.000 description 3
- 235000018000 Picea mariana var. semiprostrata Nutrition 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 159000000007 calcium salts Chemical class 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000008139 complexing agent Substances 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- WBZKQQHYRPRKNJ-UHFFFAOYSA-N disulfurous acid Chemical compound OS(=O)S(O)(=O)=O WBZKQQHYRPRKNJ-UHFFFAOYSA-N 0.000 description 3
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 3
- 239000001095 magnesium carbonate Substances 0.000 description 3
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 3
- 238000003801 milling Methods 0.000 description 3
- 239000011087 paperboard Substances 0.000 description 3
- 229910000027 potassium carbonate Inorganic materials 0.000 description 3
- 235000019832 sodium triphosphate Nutrition 0.000 description 3
- RYYXDZDBXNUPOG-UHFFFAOYSA-N 4,5,6,7-tetrahydro-1,3-benzothiazole-2,6-diamine;dihydrochloride Chemical compound Cl.Cl.C1C(N)CCC2=C1SC(N)=N2 RYYXDZDBXNUPOG-UHFFFAOYSA-N 0.000 description 2
- 241000218657 Picea Species 0.000 description 2
- 229920000388 Polyphosphate Polymers 0.000 description 2
- 241000219000 Populus Species 0.000 description 2
- 241000183024 Populus tremula Species 0.000 description 2
- 240000004923 Populus tremuloides Species 0.000 description 2
- 235000011263 Populus tremuloides Nutrition 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 235000019577 caloric intake Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000002657 fibrous material Substances 0.000 description 2
- 238000010297 mechanical methods and process Methods 0.000 description 2
- 239000001205 polyphosphate Substances 0.000 description 2
- 235000011176 polyphosphates Nutrition 0.000 description 2
- 238000004537 pulping Methods 0.000 description 2
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 2
- UNXRWKVEANCORM-UHFFFAOYSA-I triphosphate(5-) Chemical compound [O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O UNXRWKVEANCORM-UHFFFAOYSA-I 0.000 description 2
- NYYSPVRERVXMLJ-UHFFFAOYSA-N 4,4-difluorocyclohexan-1-one Chemical compound FC1(F)CCC(=O)CC1 NYYSPVRERVXMLJ-UHFFFAOYSA-N 0.000 description 1
- PDBXHPORMXSXKO-UHFFFAOYSA-N 8-benzyl-7-[2-[ethyl(2-hydroxyethyl)amino]ethyl]-1,3-dimethylpurine-2,6-dione;hydron;chloride Chemical compound Cl.N=1C=2N(C)C(=O)N(C)C(=O)C=2N(CCN(CCO)CC)C=1CC1=CC=CC=C1 PDBXHPORMXSXKO-UHFFFAOYSA-N 0.000 description 1
- 102100031260 Acyl-coenzyme A thioesterase THEM4 Human genes 0.000 description 1
- 235000018185 Betula X alpestris Nutrition 0.000 description 1
- 235000018212 Betula X uliginosa Nutrition 0.000 description 1
- 235000003717 Boswellia sacra Nutrition 0.000 description 1
- 240000007551 Boswellia serrata Species 0.000 description 1
- 235000012035 Boswellia serrata Nutrition 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 244000166124 Eucalyptus globulus Species 0.000 description 1
- 240000000731 Fagus sylvatica Species 0.000 description 1
- 235000010099 Fagus sylvatica Nutrition 0.000 description 1
- 239000004863 Frankincense Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 101000638510 Homo sapiens Acyl-coenzyme A thioesterase THEM4 Proteins 0.000 description 1
- 235000008145 Picea mariana Nutrition 0.000 description 1
- 235000008566 Pinus taeda Nutrition 0.000 description 1
- 241000218679 Pinus taeda Species 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000004973 alkali metal peroxides Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 230000003373 anti-fouling effect Effects 0.000 description 1
- 238000000149 argon plasma sintering Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000007380 fibre production Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 150000004966 inorganic peroxy acids Chemical class 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 150000004967 organic peroxy acids Chemical class 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 125000000864 peroxy group Chemical group O(O*)* 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 229940079827 sodium hydrogen sulfite Drugs 0.000 description 1
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 1
- MWNQXXOSWHCCOZ-UHFFFAOYSA-L sodium;oxido carbonate Chemical compound [Na+].[O-]OC([O-])=O MWNQXXOSWHCCOZ-UHFFFAOYSA-L 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 150000003455 sulfinic acids Chemical class 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 239000002025 wood fiber Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/02—Pretreatment of the raw materials by chemical or physical means
- D21B1/021—Pretreatment of the raw materials by chemical or physical means by chemical means
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/14—Disintegrating in mills
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1005—Pretreatment of the pulp, e.g. degassing the pulp
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1057—Multistage, with compounds cited in more than one sub-group D21C9/10, D21C9/12, D21C9/16
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1063—Bleaching ; Apparatus therefor with compounds not otherwise provided for, e.g. activated gases
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1084—Bleaching ; Apparatus therefor with reducing compounds
- D21C9/1089—Bleaching ; Apparatus therefor with reducing compounds with dithionites
Definitions
- the present invention relates to a process for the production of bleached wood pulp, a process for the production of paper or light wood materials, bleached wood pulp and the use of bleached wood pulp for the production of paper or wood-based materials, each as defined in the claims .
- Wood pulp also referred to in the art and herein as "pulp" is an important and abundant source material for the manufacture of certain types of paper, such as newsprint, magazine paper or paperboard.
- hardwoods or hardwoods or softwoods or softwoods are usually debarked, broken up into smaller pieces, usually about 5 cm ⁇ 5 cm in size (referred to in the art and herein also as “wood chips"), and then in one Grinder (in the art and also referred to herein as "refiner”), usually at elevated temperature, for example, 100 to 160 ° C, ground.
- Grinder in the art and also referred to herein as "refiner”
- suitable such hardwood or deciduous wood as well as suitable softwoods or softwoods are described, for example, in Lönnberg, Chapter (Chapter) 5, in particular Section 2. or Section 2.1.1 (Softwoods), for example spruce, fir, pine, pine or numeral 2.1 .2 (Hardwoods), for example poplar such as Populus tremula, Populus tremuloides.
- TMP thermomechanical pulp
- the TMP is bleached in a subsequent step with bleaching chemicals in order to obtain as white paper as possible in the following processing.
- bleaching chemicals used are oxidatively active substances such as hydrogen peroxide, salts of inorganic or organic peracids, for example percarbonate, or reductive substances such as sulfinic acids, salts of sulfurous acid (sulfites) or salts of dithionic acid (dithonites).
- Object of the present invention was to reduce the energy consumption - preferably in the refiner - in the production of bleached wood pulp while increasing the whiteness of the pulp as possible without further important properties of the paper made of wood pulp - for example, mechanical properties - negative change.
- the starting material for the wood pulp according to the invention are hardwoods, hardwoods and softwoods or softwoods. These woods are, for example, in Lönnberg, Chapter (Chapter) 5, in particular paragraph 2 or 2.1 .1 (softwoods), such as spruce, fir, pine, pine or item 2.1.2 (Hardwoods), for example beech, birch, eucalyptus or Poplar as Populus tremula, Populus tremuloides described and well suited for the inventive method.
- the process according to the invention is carried out as follows.
- larger wood particles preferably of debarked deciduous or coniferous wood, generally in a size of about (15-50) mm x (15-50) mm x approx (6 - 12) mm, prepared by conventional mechanical methods, for example by chopping.
- chips or chips.
- the chips or chips may be mixed with chemicals prior to further processing. For example, sodium hydrogen sulfite (NaHSO-3), sodium sulfite (Na2SOs) and / or water are pretreated.
- the chips are then delaminated in step a).
- the chips are usually first (i) subjected to mechanical pressure and / or shearing forces and then (ii) ground under relatively mild conditions, usually in a refiner.
- the chips produce "modified wood particles" (as referred to herein), usually loose fiber bundles, usually with a longitudinal dimension in the range of 5 cm to 0.3 cm, which are generally one compared to the chips used have greatly increased surface area.
- a refiner is usually a grinding unit with rotating knives and possibly fixed knives, or preferably slices for grinding fibrous materials, and preferably consists of one or two radially-relief metal discs, which are close together and form a gap between them.
- the refiner operates at atmospheric or overpressure. References are known and extensively described in Lönnberg, especially in Chapters 6 and 7.
- the above step a) (i) is usually carried out in a screw press, which usually serves for dewatering and at the same time for the pre-fiberization of the larger wood particles.
- a well-suited device for carrying out the above-mentioned step a) (i) is, for example, the "Impressafiner" from Andritz AG, Austria.
- step a) (ii) is usually carried out in a refiner or other suitable milling unit under relatively mild conditions, for example in a single-disc refiner at a disc rotation number of 1800 rpm and a pressure of 2.4 bar.
- the energy intake and / or pressure in the refiner of stage a) (ii) are lower than the corresponding parameters for the refiner in step b).
- the energy consumption in the refiner is generally determined inter alia by the Refineriminnaviere and the gap width between the Refinerimin.
- a well-suited apparatus for carrying out the aforementioned step a) (ii) is the Andritz 36-1 CP Single Disk Refiner from Andritz AG, Austria.
- step b) then the modified wood particles from step a) in a refiner - usually under harsher conditions, for example, higher Ergieentrtrag and / or higher disk speed and / or higher pressure than in step a) (ii) - ground.
- Step b) is usually carried out in a refiner under the following conditions, for example in a single-disk refiner at a disk revolution number of 2300 rpm and a pressure of 5.2 bar.
- the energy consumption in the refiner is generally determined inter alia by the Refinerimin- speed and the gap width between the Refinerimin.
- a well-suited apparatus for carrying out the aforementioned step b) is the Andritz 36-1 CP Single Disk Refiner from Andritz AG, Austria.
- Step b) may be followed by a further milling step or may be followed by a plurality of milling steps in a refiner in analogy to step b).
- the substance obtained in step b) is optionally treated in a following step c) with reductive or oxidative bleaches using otherwise customary methods known from wood fiber production, for example in the bleaching tower.
- Bleaching agents and bleaching processes in the production of wood pulp are described, for example, in detail in Lönnberg, in particular in Chapter 11.
- Suitable oxidative bleaching agents which are suitable for the process according to the invention are those having a peroxy grouping, for example hydrogen peroxide, alkali metal peroxides.
- Suitable reductive bleaches for step c) of the process according to the invention are, for example, salt of the dithionic acid H.sub.2S.sub.2 O.sub.4, salts of sulphurous acid and the like, preferably the composition Z, particularly preferably the components Z.sup.1 or Z.sup.2 or Z.sup.3.
- Suitable salts of the dithionic acid (Z1) are preferably the alkali metal salts, preferably lithium, sodium, potassium or alkaline earth metal salts, preferably calcium, magnesium salts of the dithionic acid or mixtures thereof, the forms of course being included with water of crystallization or similar adducts are.
- Particularly preferred is sodium dithionite (Na 2 S 20 4 ), which forms are of course included with water of crystallization or similar adducts.
- thiourea dioxide also called formamidinesulfinic acid
- HN C (NH 2) SO 2 H) in combination with lye, for example sodium hydroxide (NaOH in water) in question.
- component (Z3) are: a salt, preferably an alkali metal salt, preferably lithium, sodium, potassium or alkaline earth metal salt, preferably calcium, magnesium salt of sulfurous acid (H2SO3), ergo sulfites, or mixtures thereof, the forms with Of course, water of crystallization or similar adducts are included, each in combination with sodium tetraborohydride. Particularly preferred is the combination of sodium sulfite (Na 2 SC "3), which forms are of course included with water of crystallization or similar adducts, with sodium tetraborohydride (NaBhU).
- Component (Z4) is one or more of the following components (1) to (4) and, if appropriate, further additives: (1) complexing agents, for example EDTA, polyphosphates, for example sodium tripolyphosphate and / or potassium tripolyphosphate; (2) basic compounds, preferably basic salts such as carbonates or bicarbonates, for example basic salts such as carbonates or bicarbonates of the alkali metals or alkaline earth metals, preferably lithium, sodium, potassium carbonate or alkaline earth metal carbonate, preferably calcium, magnesium carbonate, more preferably sodium carbonate (Na2CC " (3) an alkali metal salt, preferably lithium, sodium, potassium or alkaline earth metal salt, preferably calcium, magnesium salt of the epidurous acid (H2S2O5); (4) an alkali metal salt , preferably lithium, sodium, potassium salt or alkaline earth metal salt, preferably calcium, magnesium salt of sulfurous acid (H2SO3), more preferably sodium sulfite (Na 2 S0 3 ).
- complexing agents
- Suitable further additives of component (Z4) are: surface-active substances such as anionic, cationic or nonionic or glucose-containing surfactants, usually in the proportion of from 1% by weight to 10% by weight, based on the composition Z; further anti-scale or anti-fouling substances such as polyacrylates in the proportion in the range of 1 wt .-% to 10 wt .-%, based on the composition Z.
- the composition Z contains a salt of the dithionic acid H2S2O4 (Z1), preferably a sodium salt, potassium salt, calcium salt, magnesium salt of the dithionic acid, including mixtures of these salts, more preferably sodium dithionite, the above in each case particularly preferably in the range from 20 to 95% by weight, very particularly preferably from 60 to 95% by weight, in each case based on the composition Z.
- Z1 a salt of the dithionic acid H2S2O4 (Z1), preferably a sodium salt, potassium salt, calcium salt, magnesium salt of the dithionic acid, including mixtures of these salts, more preferably sodium dithionite, the above in each case particularly preferably in the range from 20 to 95% by weight, very particularly preferably from 60 to 95% by weight, in each case based on the composition Z.
- the composition Z contains, on the one hand, a salt of the dithionic acid H2S204 (Z1), preferably a sodium salt, potassium salt, calcium salt, magnesium salt of the dithionic acid, including mixtures of these salts, particularly preferably sodium dithionite above-described components (Z1) in each case particularly preferably in the range from 60 to 95% by weight, based in each case on the composition Z and secondly the component (Z4), more preferably thereof (1) complexing agent polyphosphates, (2) basic Salts such as carbonates or hydrogen carbonate bonates of the alkali metals or alkaline earth metals, such as sodium carbonate; (3) an alkali metal salt of the disulfurous acid (H2S2O5); (4) an alkali metal salt of sulfurous acid (H 2 SO 3), preferably containing (Z 1) in the range of 60 to 95% by weight and (Z 4) in the range of 5 to 40% by weight, based in each case on the composition Z is.
- a salt of the dithionic acid H2S204
- the composition Z comprises 60 to 95% by weight of a sodium salt (Z1), preferably sodium dithionite; 1 to 25% by weight of a sulfite Z4 (4), preferably sodium sulfite; 1 to 10 wt .-% of a carbonate and / or a hydrogen carbonate, in each case the alkali metals Z4 (2), preferably sodium carbonate; 0 to 10% by weight of a complexing agent Z4 (1), preferably sodium tripolyphosphate; in each case based on the composition Z and wherein the sum of said components gives 100%.
- a sodium salt (Z1) preferably sodium dithionite
- a sulfite Z4 (4) preferably sodium sulfite
- 1 to 10 wt .-% of a carbonate and / or a hydrogen carbonate in each case the alkali metals Z4 (2), preferably sodium carbonate; 0 to 10% by weight of a complexing agent Z4 (1), preferably sodium tripolyphosphate; in each case
- the composition Z contains, in addition to one or more of the components (Z1) to (Z3) and one or more components Z4 (1), Z4 (3) and Z4 (4), such an amount of basic compounds Z4 (2), preferably basic salts such as carbonates or bicarbonates, for example basic salts such as carbonates or bicarbonates of alkali metals or alkaline earth metals, preferably lithium, sodium, potassium carbonate or alkaline earth metal carbonate, preferably calcium, magnesium carbonate, more preferably sodium carbonate these basic compounds act as acid buffers.
- basic salts such as carbonates or bicarbonates
- alkali metals or alkaline earth metals preferably lithium, sodium, potassium carbonate or alkaline earth metal carbonate, preferably calcium, magnesium carbonate, more preferably sodium carbonate these basic compounds act as acid buffers.
- the composition Z contains, in addition to the component (Z1) - preferably a sodium salt, potassium salt, calcium salt, magnesium salt of dithionic acid, including mixtures of these salts, particularly preferably sodium dithionite - and one or more components Z4 (1), Z4 (3) and Z4 (4) such an amount of basic compounds Z4 (2), preferably basic salts such as carbonates or bicarbonates, for example basic salts such as carbonates or bicarbonates of the alkali metals or alkaline earth metals, preferably lithium, sodium -, potassium carbonate or alkaline earth metal carbonate, preferably calcium, magnesium carbonate, particularly preferably sodium carbonate, that these basic compounds act as acid buffer.
- basic salts such as carbonates or bicarbonates
- basic salts such as carbonates or bicarbonates of the alkali metals or alkaline earth metals, preferably lithium, sodium -, potassium carbonate or alkaline earth metal carbonate, preferably calcium, magnesium carbonate, particularly preferably sodium carbonate, that these basic compounds act as acid buffer.
- composition Z is used in the inventive method in the form of a solution or suspension, but it can also be used without further solvents or diluents as pure substance.
- Suitable solvents or dispersants dissolve or disperse the composition Z without its active ingredient or active ingredients, in particular component Z1, by decomposition or otherwise rendering ineffective or greatly reducing their action.
- water-containing solvents or dispersants for example mixtures of water and protic or aprotic organic solvents, for example alcohols, or ethers, ketones.
- a preferred solvent or dispersant is water.
- the concentration of the composition Z in such solutions or dispersions is generally in the range of 1 to 30 wt .-%, preferably 5 to 20 wt .-%, each based on the mass of the solution or dispersion.
- the amount of component (Z1) or (Z2) or (Z3), preferably of component (Z1), more preferably of sodium dithionite, per kilogram of wood material to be treated, for example chips or modified wood particles, is in the range of 1 to 50 grams, preferably in the range of 5 to 20 grams.
- the solution or dispersion described above-including its preferred embodiments- is preferably prepared and used as fresh as possible, or it is stored with the most extensive possible exclusion of oxidizing media, for example atmospheric oxygen.
- the composition Z is usually added before step a) (i), or before step a) (ii) or during the performance of step a) (i) and / or step a) (ii) and / or before step b) and / or during the performance of step b) with the corresponding wood particles or modified wood particles in contact.
- a solution or dispersion of the composition Z described in more detail above, including its preferred embodiments, preferably a solution or dispersion of Z in water is introduced into the feed line for the wood particles to the corresponding devices in which the steps a) (i) a (ii) or b) are carried out, preferably in the flow direction of the wood particles or modified wood particles, shortly before the corresponding device dosed.
- a solution or dispersion of the composition Z which is described in greater detail above, can usually be metered directly into the space of the corresponding apparatuses in which steps a) (i), a (ii) or b) are carried out.
- a solution or dispersion of Z in water described in greater detail above-including its preferred embodiments- is metered into the refiner of stage a) (ii) and / or the refiner of stage b).
- the present invention also provides a process for the production of paper, preferably tissue, newsprint, magazine paper or paper for paperboard production, wherein, as described herein, a bleached wood pulp is made and this into paper, preferably tissue, newsprint, magazine paper or paper for paperboard production, usually with the known papermaking process, further processed.
- the present invention also provides a process for producing light-colored wood-based materials, preferably HDF or MDF wood-based materials, wherein, as described herein, ben bleached wood pulp and this, optionally with the addition of white pigments, glued and pressed to the wood materials.
- the present invention also provides a bleached wood pulp obtainable by a process as described herein.
- the present invention also provides the use of bleached wood pulp obtainable by the process as described herein for the production of paper or wood-based materials.
- the inventive method is characterized by the fact that the energy consumption in the refiner is reduced and the degree of bleaching of the wood pulp obtainable by the process according to the invention is higher than in the comparable prior art.
- the energy consumption in the refiner, the degree of bleaching of the wood pulp and other physical parameters were determined by the methods described in the examples.
- This raw material was further processed in the so-called ATMP process of Andritz AG (Austria) as follows.
- the chips were treated in a chip press (screw machine "Impressafiner” from the company Andritz AG, Austria) at a pressure of approximately 1.4 bar
- the material thus treated was treated with water after leaving the screw machine and placed in a refiner (Andritz 36-1 CP from Andritz AG, Austria), the so-called “Fiberizer” with a single grinding disc (diameter 0.91 m) fed where it at a grinding wheel speed of 1800 rev / min and a pressure of 2.4 bar was converted into fibrous material.
- the so-shredded material was fed into a first main refiner (Andritz 36-1 CP) and was there at a grinding wheel speed of 2300 U / min and a pressure of 5.2 bar in the presence of the composition Z, as described below, in Converted wood pulp.
- a first main refiner Engelhard 36-1 CP
- step a) according to the invention was not carried out and the chips (see above) were used directly in a first Main refiner (Andritz 36- 1 CP Andritz AG, Austria) at a pressure of 3.45 bar and a wheel speed of 1800 rev / min ground to wood pulp, in the presence of a solution described above under A) of the composition Z in water , This wood pulp was further ground in a second main refiner with two grinding wheels (Andritz 401 from Andritz AG, Austria) at atmospheric pressure.
- the Tensile Index was determined with Tappi T 456.
- the Tear Index was determined with Tappi T 414.
- the Tensile Energy Absorption (TEA) was determined with Tappi T 494.
- the Light Scattering Coefficient was determined with ISO 9416.
- Wood pulp fractionation was carried out with a Bauer Mc Nett Classifier.
- the wood pulp produced according to the described variant A) with the wood of the black spruce was processed according to the standard TAPPI T 205 by means of a standard laboratory sheet forming test paper and determined thereon mechanical properties, and the optical properties (for example whiteness) were measured on paper sheets produced according to the TAPPI T 218 standard.
- wood pulp which was obtained according to the described variant B), as described above processed into test paper and investigated by the methods described above.
- the wood pulp properties were normalized to a drainage behavior of the aqueous wood pulp (Freeness) of 200 ml.
- wood pulp obtained according to the described variant B) from the wood of the turpentine pine was processed to test paper as described in Example 1 and investigated by the methods described in Example 1.
- the wood pulp properties were normalized to a drainage behavior of the aqueous wood pulp (Freeness) of 200 ml.
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Paper (AREA)
- Chemical And Physical Treatments For Wood And The Like (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
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PL15711458T PL3122931T3 (pl) | 2014-03-25 | 2015-03-13 | Sposób wytwarzania bielonej masy włóknistej drzewnej |
SI201531045T SI3122931T1 (sl) | 2014-03-25 | 2015-03-13 | Postopek za proizvodnjo beljene lesne vlaknine |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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EP14161583.1A EP2924166A1 (de) | 2014-03-25 | 2014-03-25 | Verfahren zur Herstellung von gebleichtem Holzfaserstoff |
PCT/EP2015/055275 WO2015144455A1 (de) | 2014-03-25 | 2015-03-13 | Verfahren zur herstellung von gebleichtem holzfaserstoff |
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EP3122931A1 true EP3122931A1 (de) | 2017-02-01 |
EP3122931B1 EP3122931B1 (de) | 2019-10-30 |
Family
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Application Number | Title | Priority Date | Filing Date |
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EP14161583.1A Withdrawn EP2924166A1 (de) | 2014-03-25 | 2014-03-25 | Verfahren zur Herstellung von gebleichtem Holzfaserstoff |
EP15711458.8A Active EP3122931B1 (de) | 2014-03-25 | 2015-03-13 | Verfahren zur herstellung von gebleichtem holzfaserstoff |
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EP14161583.1A Withdrawn EP2924166A1 (de) | 2014-03-25 | 2014-03-25 | Verfahren zur Herstellung von gebleichtem Holzfaserstoff |
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Country | Link |
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US (2) | US11015290B2 (de) |
EP (2) | EP2924166A1 (de) |
JP (1) | JP6707460B2 (de) |
KR (1) | KR102426606B1 (de) |
CN (2) | CN106103842A (de) |
AU (1) | AU2015238642B2 (de) |
BR (1) | BR112016021939B1 (de) |
CA (1) | CA2943663C (de) |
CL (1) | CL2016002398A1 (de) |
ES (1) | ES2768924T3 (de) |
MX (1) | MX2016012461A (de) |
PL (1) | PL3122931T3 (de) |
RU (1) | RU2689568C2 (de) |
SI (1) | SI3122931T1 (de) |
WO (1) | WO2015144455A1 (de) |
ZA (1) | ZA201607131B (de) |
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US3981765A (en) * | 1969-07-30 | 1976-09-21 | Vita Mayer & C. | Treatment of wood chips with an alkali metal borohydride solution followed by mechanical defibration |
GB1404315A (en) * | 1971-09-15 | 1975-08-28 | Albright & Wilson | Production of bleached high yield pulp |
JPS6368377A (ja) * | 1986-09-08 | 1988-03-28 | 株式会社 ト−セ−インダストリ− | ホツチキス装置 |
FR2615874B1 (fr) | 1987-05-25 | 1992-02-21 | Atochem | Procede de preparation de pates chimicothermomecaniques |
GB2215350B (en) * | 1988-03-16 | 1992-05-20 | Thiokol Morton Inc | Process for bleaching mechanical wood pulp |
FR2634233B1 (fr) * | 1988-07-12 | 1995-04-14 | Atochem | Procede de fabrication de pates chimicothermomecaniques blanchies |
FR2675518B1 (fr) * | 1991-04-17 | 1996-10-18 | Atochem | Procede de preparation de pate a papier a haut rendement et blanchie, a partir de copeaux de bois. |
SE468644B (sv) * | 1991-05-24 | 1993-02-22 | Sunds Defibrator Ind Ab | Framstaellning av kemitermomekanisk massa samt impregneringsloesning innehaallande borhydrid och sulfit |
DK0604088T3 (da) * | 1992-12-14 | 1997-10-27 | Hoechst Celanese Corp | Eliminering af svovldioxiddannelse ved raffinørblegning |
DK0705327T3 (da) * | 1993-06-16 | 2000-08-28 | Call Hans Peter | Flerkomponentblegesystem |
SE9402101L (sv) * | 1994-06-15 | 1995-12-16 | Moelnlycke Ab | Lättavvattnad, bulkig, kemimekanisk massa med låg spet- och finmaterialhalt |
AU4271596A (en) * | 1995-12-19 | 1997-07-14 | Kvaerner Hymac Inc. | Process for treating refiner pulp |
JP2003027385A (ja) | 2001-07-16 | 2003-01-29 | Nippon Paper Industries Co Ltd | 機械パルプの製造方法 |
US7300541B2 (en) * | 2002-07-19 | 2007-11-27 | Andritz Inc. | High defiberization chip pretreatment |
US7384502B2 (en) | 2002-12-24 | 2008-06-10 | Nippon Paper Industries Co., Ltd. | Process for impregnating, refining, and bleaching wood chips having low bleachability to prepare mechanical pulps having high brightness |
DE102004050278A1 (de) | 2004-10-14 | 2006-04-27 | Basf Ag | Helle bis weiße Holzwerkstoffplatten |
CA2527325C (en) * | 2005-11-18 | 2014-05-06 | Mohini M. Sain | Manufacturing process for high performance lignocellulosic fibre composite materials |
US7967948B2 (en) | 2006-06-02 | 2011-06-28 | International Paper Company | Process for non-chlorine oxidative bleaching of mechanical pulp in the presence of optical brightening agents |
EP2142348B1 (de) * | 2007-04-24 | 2013-12-25 | Basf Se | Verfahren zur herstellung von gebleichten holzpartikeln und hellen bis weissen holzwerkstoffen |
FI121114B (fi) * | 2007-05-04 | 2010-07-15 | Kemira Oyj | Ditioniitin valmistusmenetelmä |
US8282773B2 (en) | 2007-12-14 | 2012-10-09 | Andritz Inc. | Method and system to enhance fiber development by addition of treatment agent during mechanical pulping |
RU2398676C2 (ru) * | 2008-03-06 | 2010-09-10 | Федеральное агентство по образованию Государственное образовательное учреждение высшего профессионального образования "Московский государственный университет леса" | Конструкционный плитный материал, выполненный из целлюлозосодержащих частиц, пропитанных клеем |
US8734611B2 (en) * | 2008-03-12 | 2014-05-27 | Andritz Inc. | Medium consistency refining method of pulp and system |
US20100224333A1 (en) * | 2009-03-09 | 2010-09-09 | Prasad Duggirala | Method and chemical composition to improve efficiency of mechanical pulp |
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KR101274267B1 (ko) * | 2011-01-20 | 2013-06-14 | 한국수력원자력 주식회사 | 방사선 조사에 의한 목재 종이 및 펄프의 제조방법, 이에 의하여 제조되는 목재 종이 및 목재 펄프, 및 이를 이용하여 제조되는 종이제품 |
WO2012101137A1 (de) * | 2011-01-25 | 2012-08-02 | Basf Se | Verfahren zur herstellung eines papiererzeugnisses |
CN103419264A (zh) * | 2012-05-18 | 2013-12-04 | 大亚木业(福建)有限公司 | 超低密度高性能刨花板生产方法 |
-
2014
- 2014-03-25 EP EP14161583.1A patent/EP2924166A1/de not_active Withdrawn
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2015
- 2015-03-13 CN CN201580013319.0A patent/CN106103842A/zh active Pending
- 2015-03-13 EP EP15711458.8A patent/EP3122931B1/de active Active
- 2015-03-13 SI SI201531045T patent/SI3122931T1/sl unknown
- 2015-03-13 CN CN202210863517.8A patent/CN115198551A/zh active Pending
- 2015-03-13 KR KR1020167029555A patent/KR102426606B1/ko active IP Right Grant
- 2015-03-13 ES ES15711458T patent/ES2768924T3/es active Active
- 2015-03-13 CA CA2943663A patent/CA2943663C/en active Active
- 2015-03-13 US US15/128,755 patent/US11015290B2/en active Active
- 2015-03-13 BR BR112016021939-2A patent/BR112016021939B1/pt active IP Right Grant
- 2015-03-13 AU AU2015238642A patent/AU2015238642B2/en active Active
- 2015-03-13 WO PCT/EP2015/055275 patent/WO2015144455A1/de active Application Filing
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- 2015-03-13 JP JP2016558601A patent/JP6707460B2/ja active Active
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CN115198551A (zh) | 2022-10-18 |
CN106103842A (zh) | 2016-11-09 |
JP2017510725A (ja) | 2017-04-13 |
RU2016141601A3 (de) | 2018-10-18 |
RU2689568C2 (ru) | 2019-05-28 |
EP2924166A1 (de) | 2015-09-30 |
AU2015238642B2 (en) | 2018-07-12 |
BR112016021939B1 (pt) | 2022-01-04 |
ZA201607131B (en) | 2018-08-30 |
CL2016002398A1 (es) | 2017-01-20 |
CA2943663A1 (en) | 2015-10-01 |
JP6707460B2 (ja) | 2020-06-10 |
BR112016021939A8 (pt) | 2021-05-04 |
US20180216292A1 (en) | 2018-08-02 |
CA2943663C (en) | 2022-10-04 |
US11015290B2 (en) | 2021-05-25 |
RU2016141601A (ru) | 2018-04-25 |
ES2768924T3 (es) | 2020-06-24 |
US20210254280A1 (en) | 2021-08-19 |
EP3122931B1 (de) | 2019-10-30 |
WO2015144455A1 (de) | 2015-10-01 |
MX2016012461A (es) | 2017-01-06 |
PL3122931T3 (pl) | 2020-05-18 |
AU2015238642A1 (en) | 2016-10-06 |
KR102426606B1 (ko) | 2022-07-28 |
BR112016021939A2 (de) | 2017-08-15 |
SI3122931T1 (sl) | 2020-02-28 |
US11725338B2 (en) | 2023-08-15 |
KR20160136424A (ko) | 2016-11-29 |
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