FI118090B - Additives, the use of additives in the production of paper and paperboard, the process for improving the production of paper and paperboard, and the procedure for improving paper and paperboard products - Google Patents
Additives, the use of additives in the production of paper and paperboard, the process for improving the production of paper and paperboard, and the procedure for improving paper and paperboard products Download PDFInfo
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- FI118090B FI118090B FI20040519A FI20040519A FI118090B FI 118090 B FI118090 B FI 118090B FI 20040519 A FI20040519 A FI 20040519A FI 20040519 A FI20040519 A FI 20040519A FI 118090 B FI118090 B FI 118090B
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- Prior art keywords
- paper
- component
- fatty acids
- fatty acid
- typically
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- 239000000123 paper Substances 0.000 title claims description 52
- 239000000654 additive Substances 0.000 title claims description 31
- 238000000034 method Methods 0.000 title claims description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000011087 paperboard Substances 0.000 title claims description 10
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 44
- 239000000194 fatty acid Substances 0.000 claims description 44
- 229930195729 fatty acid Natural products 0.000 claims description 44
- 230000000996 additive effect Effects 0.000 claims description 28
- 150000004665 fatty acids Chemical class 0.000 claims description 26
- 239000000725 suspension Substances 0.000 claims description 24
- 239000002253 acid Substances 0.000 claims description 20
- 150000007513 acids Chemical class 0.000 claims description 13
- 235000019645 odor Nutrition 0.000 claims description 10
- 239000011347 resin Substances 0.000 claims description 8
- 229920005989 resin Polymers 0.000 claims description 8
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 7
- 229920002472 Starch Polymers 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 235000019698 starch Nutrition 0.000 claims description 6
- 150000003626 triacylglycerols Chemical class 0.000 claims description 5
- 235000019486 Sunflower oil Nutrition 0.000 claims description 4
- 239000004826 Synthetic adhesive Substances 0.000 claims description 4
- 239000000853 adhesive Substances 0.000 claims description 4
- 230000001070 adhesive effect Effects 0.000 claims description 4
- 235000021388 linseed oil Nutrition 0.000 claims description 4
- 239000000944 linseed oil Substances 0.000 claims description 4
- 239000002600 sunflower oil Substances 0.000 claims description 4
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 4
- 239000008158 vegetable oil Substances 0.000 claims description 4
- 229920000881 Modified starch Polymers 0.000 claims description 3
- 229920001131 Pulp (paper) Polymers 0.000 claims description 3
- 239000000839 emulsion Substances 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 3
- 235000019426 modified starch Nutrition 0.000 claims description 3
- 239000003381 stabilizer Substances 0.000 claims description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 2
- 229920000057 Mannan Polymers 0.000 claims description 2
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 2
- 229920006184 cellulose methylcellulose Polymers 0.000 claims description 2
- 229920002401 polyacrylamide Polymers 0.000 claims description 2
- 229920000768 polyamine Polymers 0.000 claims description 2
- 239000004094 surface-active agent Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims 1
- LUEWUZLMQUOBSB-GFVSVBBRSA-N mannan Chemical class O[C@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@@H](O[C@@H]2[C@H](O[C@@H](O[C@H]3[C@H](O[C@@H](O)[C@@H](O)[C@H]3O)CO)[C@@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O LUEWUZLMQUOBSB-GFVSVBBRSA-N 0.000 claims 1
- 229920000642 polymer Polymers 0.000 claims 1
- 125000005456 glyceride group Chemical group 0.000 description 23
- 238000006116 polymerization reaction Methods 0.000 description 14
- 238000001035 drying Methods 0.000 description 13
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 13
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 11
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 5
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 5
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 5
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 5
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 5
- 239000005642 Oleic acid Substances 0.000 description 5
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 5
- 235000020778 linoleic acid Nutrition 0.000 description 5
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 5
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 5
- DTOSIQBPPRVQHS-PDBXOOCHSA-N alpha-linolenic acid Chemical compound CC\C=C/C\C=C/C\C=C/CCCCCCCC(O)=O DTOSIQBPPRVQHS-PDBXOOCHSA-N 0.000 description 4
- 235000020661 alpha-linolenic acid Nutrition 0.000 description 4
- 229960004488 linolenic acid Drugs 0.000 description 4
- KQQKGWQCNNTQJW-UHFFFAOYSA-N linolenic acid Natural products CC=CCCC=CCC=CCCCCCCCC(O)=O KQQKGWQCNNTQJW-UHFFFAOYSA-N 0.000 description 4
- GYSCBCSGKXNZRH-UHFFFAOYSA-N 1-benzothiophene-2-carboxamide Chemical compound C1=CC=C2SC(C(=O)N)=CC2=C1 GYSCBCSGKXNZRH-UHFFFAOYSA-N 0.000 description 3
- FXUKWLSZZHVEJD-UHFFFAOYSA-N 14-methylhexadecanoic acid Chemical compound CCC(C)CCCCCCCCCCCCC(O)=O FXUKWLSZZHVEJD-UHFFFAOYSA-N 0.000 description 3
- GHVNFZFCNZKVNT-UHFFFAOYSA-N Decanoic acid Natural products CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 description 3
- 150000004671 saturated fatty acids Chemical class 0.000 description 3
- 235000003441 saturated fatty acids Nutrition 0.000 description 3
- 238000004513 sizing Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 229930182558 Sterol Natural products 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- -1 sterol esters Chemical class 0.000 description 2
- 235000003702 sterols Nutrition 0.000 description 2
- NJVOHKFLBKQLIZ-UHFFFAOYSA-N (2-ethenylphenyl) prop-2-enoate Chemical compound C=CC(=O)OC1=CC=CC=C1C=C NJVOHKFLBKQLIZ-UHFFFAOYSA-N 0.000 description 1
- HXQHFNIKBKZGRP-URPRIDOGSA-N (5Z,9Z,12Z)-octadecatrienoic acid Chemical compound CCCCC\C=C/C\C=C/CC\C=C/CCCC(O)=O HXQHFNIKBKZGRP-URPRIDOGSA-N 0.000 description 1
- PYSRRFNXTXNWCD-UHFFFAOYSA-N 3-(2-phenylethenyl)furan-2,5-dione Chemical compound O=C1OC(=O)C(C=CC=2C=CC=CC=2)=C1 PYSRRFNXTXNWCD-UHFFFAOYSA-N 0.000 description 1
- DFYNENBDVWMLFE-VIFPVBQESA-N 5-bromo-2-[[(3s)-piperidin-3-yl]amino]benzoic acid Chemical compound OC(=O)C1=CC(Br)=CC=C1N[C@@H]1CNCCC1 DFYNENBDVWMLFE-VIFPVBQESA-N 0.000 description 1
- BSYNRYMUTXBXSQ-UHFFFAOYSA-N Aspirin Chemical compound CC(=O)OC1=CC=CC=C1C(O)=O BSYNRYMUTXBXSQ-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- HXQHFNIKBKZGRP-UHFFFAOYSA-N Ranuncelin-saeure-methylester Natural products CCCCCC=CCC=CCCC=CCCCC(O)=O HXQHFNIKBKZGRP-UHFFFAOYSA-N 0.000 description 1
- 235000021355 Stearic acid Nutrition 0.000 description 1
- 229920000147 Styrene maleic anhydride Polymers 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 239000011153 ceramic matrix composite Substances 0.000 description 1
- 238000012710 chemistry, manufacturing and control Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000000875 corresponding effect Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- FXHGMKSSBGDXIY-UHFFFAOYSA-N heptanal Chemical compound CCCCCCC=O FXHGMKSSBGDXIY-UHFFFAOYSA-N 0.000 description 1
- JARKCYVAAOWBJS-UHFFFAOYSA-N hexanal Chemical compound CCCCCC=O JARKCYVAAOWBJS-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- HPIGCVXMBGOWTF-UHFFFAOYSA-N isomaltol Natural products CC(=O)C=1OC=CC=1O HPIGCVXMBGOWTF-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 1
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 239000008117 stearic acid Substances 0.000 description 1
- 150000003432 sterols Chemical class 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/14—Carboxylic acids; Derivatives thereof
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/28—Starch
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/31—Gums
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
- D21H17/375—Poly(meth)acrylamide
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/56—Polyamines; Polyimines; Polyester-imides
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/63—Inorganic compounds
- D21H17/67—Water-insoluble compounds, e.g. fillers, pigments
- D21H17/68—Water-insoluble compounds, e.g. fillers, pigments siliceous, e.g. clays
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/02—Agents for preventing deposition on the paper mill equipment, e.g. pitch or slime control
Landscapes
- Paper (AREA)
Description
118090 ' . · Jm118090 '. · Jm
LISÄAINE, LISÄAINEEN KÄYTTÖ PAPERIN JA KARTONGIN VALMISTUKSESSA, MENETELMÄ PAPERIN JA KARTONGIN VALMISTUKSEN PARANTAMISEKSI JA MENETELMÄ PAPERI-JA 5 KARTONKITUOTTEEN PARANTAMISEKSIADDITIVE, USE OF ADDITIVE IN PAPER AND PAPERBOARD MANUFACTURE, METHOD FOR IMPROVING PAPER AND PAPERBOARD MANUFACTURE AND METHOD FOR IMPROVING PAPER AND 5 PAPERBOARD PRODUCTS
Esillä oleva keksintö kohdistuu jäljempänä esitettyjen patenttivaatimusten alkuosan mukaiseen lisäaineeseen, lisäaineen käyttöön paperin ja kartongin valmistuksessa, menetelmään paperin ja kartongin valmistuksen parantamiseksi ja menetelmään paperi-ja kartonkituotteen parantamiseksi.The present invention relates to an additive according to the preamble of the claims below, to the use of an additive in the manufacture of paper and board, to a process for improving paper and board production, and to a paper and board product.
10 Paperin ja kartongin valmistuksessa käytetyt massasuspensiot sisältävät selluloosakuitujen lisäksi eri tyyppisiä uuteaineita, eli heterogeenisen ryhmän lipofiilisia ja/tai hydrofiilisia aineita. Erityisesti mekaanista massaa sisältävät 4 massasuspensiot saattavat sisältää huomattavia määriä lipofiilisiä aineita, kuten rasvahappoja, glyseridejä, steroliestereitä, steroleja ja hartsihappoja. Myös suuren 15 hylkymäärän lisäys saattaa nostaa lipofiilisten aineiden määrää massasuspensiossa. 4The pulp suspensions used in the manufacture of paper and board contain, in addition to cellulosic fibers, various types of extractants, i.e., a heterogeneous group of lipophilic and / or hydrophilic substances. In particular, pulp suspensions containing mechanical pulp may contain significant amounts of lipophilic substances such as fatty acids, glycerides, sterol esters, sterols and resin acids. The addition of a large amount of rejection may also increase the amount of lipophilic substances in the pulp suspension. 4
Lipo Eiliset aineet ovat luonnostaan hydrofobisia ja muodostavat pihkaksi kutsuttuja :*j*; liukenemattomia tahmeita aggregaatteja, jotka helposti, erityisesti joissakin ·:··· lämpötiloissa, muodostavat kerrostumia paperi-ja kartonkikoneiden eri pinnoille.Lipo Yesterday's substances are naturally hydrophobic and form what's called a pitch: * j *; insoluble sticky aggregates that easily deposit, especially at some temperatures: · · ···, on different surfaces of paper and board machines.
: Tahmeat aggregaatit kiinnittyvät tyypillisesti paperi-ja kartonkikoneiden • * # 20 kuivatusosan sylintereille, teloille ja kudoksille, mutta saattavat aiheuttaa ongelmia muuallakin paperi-ja kartonkikoneissa, esimerkiksi kerrostumalla puristinosan • * · ·...· huoville ja teloille. Vaikeudet saattavat johtaa ajettavuusongelmiin, ratakatkoihin ja koneen perusteelliseen puhdistustarpeeseen. Liukenemattomat aggregaatit saattavat * · • * · ·*·· : lisäksi aiheuttaa laatuongelmia, kuten reikiä ja pilkkuja paperituotteessa.: Sticky aggregates typically adhere to cylinders, rolls, and fabrics in the drying section of paper and board machines, but may also cause problems elsewhere in paper and board machines, for example, by depositing the press section on the felt and rolls. Difficulties can lead to runner problems, track breaks and a thorough cleaning of the machine. Insoluble aggregates may also cause quality problems such as holes and dots in the paper product.
• · • · • ·· . ·: \ 25 Pihkan korostuminen paperikoneilla on näyttänyt tapahtuvan näennäisen ♦ ♦ * epäsäännöllisesti. Erilaisia menetelmiä ongelman ratkaisemiseksi on ehdotettu.• · • · • ··. ·: \ 25 The appearance of resin on paper machines has seemed to occur ♦ ♦ * irregularly. Various methods for solving the problem have been proposed.
··· ; Esimerkiksi puun pitempiaikainen varastointi näyttää vähentävän glyseridien 4 • · · • * * · määrää mekaanisessa massassa. Pitempiaikainen varastointi johtaa kuitenkin • · paperin ja kartongin vaaleuden huononemiseen ja tietenkin 30 varastointikustannuksiin.···; For example, longer storage of wood seems to reduce the amount of glycerides 4 • · · • * * · in the mechanical pulp. However, prolonged storage will result in • · a reduction in the lightness of the paper and cardboard and, of course, 30 storage costs.
' ; 4 1 1 8090 2'; 4 1 1 8090 2
Paperikoneen säännöllinen pesu joillakin kemikaaleilla saattaa auttaa ongelman ' ratkaisemisessa. Myös joidenkin lisäaineiden, kuten anionisten dispergoivien aineiden, alumiinisulfaatin, adsorbenttien, kationisten polymeerien tai entsyymien käyttöä on ehdotettu. Myös paperikoneen materiaalit ja konstruktiot valitaan siten, 5 että vältetään korroosion muodostuminen, kerrostumien syntymisen ehkäisemiseksi.Regular washing of the paper machine with some chemicals can help solve the problem. Some additives, such as anionic dispersants, aluminum sulfate, adsorbents, cationic polymers or enzymes, have also been proposed. The materials and structures of the papermaking machine are also selected such that corrosion is avoided to prevent the formation of deposits.
Silti ongelmia esiintyy.Still, there are problems.
Joskus paperi- ja kartonkituotteet voivat olla huonontuneet selittämättömästä epämiellyttävästä hajusta. Usein hajusta on syytetty käytettyä liimakomponenttia, esimerkiksi tärkkelystä. Mitään ainoata yksinkertaista vastausta hajuongelmiin ei ' 10 ole löytynyt. Hajuongelmia näyttää syntyvän useammin joillakin paperikoneilla kuin toisilla.Sometimes, paper and board products may be degraded by an unexplained unpleasant odor. Often the smell component, such as starch, has been blamed for the odor. No single simple answer to odor problems has been found. Odor problems appear to occur more frequently on some paper machines than on others.
Paperinvalmistusprosessissa käytetään paperin massaliimausta tai pintaliimausta antamaan paperituotteelle hyvä hydrofobiteetti. Matalammilla pH-tasoilla, eli kun pH < 6, käytetään liimakomponentteina yleensä hartsihappoja yhdessä erilaisten IS alumiinikomponenttien kanssa. Korkeammilla pH-tasoilla käytetään yleisesti synteettisiä liimoja, kuten ASA- ja AKD-liimoja. Näiden liimojen mahdollinen haittapuoli on sellaisten hydrolyysituotteiden muodostuminen, jotka voivat olla jopa tahmeampia kuin itse Himakomponentti.The papermaking process uses pulp gluing or surface sizing to give the paper product good hydrophobicity. At lower pH levels, that is, at pH <6, resin acids are generally used as adhesive components in combination with various IS aluminum components. At higher pH levels synthetic adhesives such as ASA and AKD are commonly used. A potential drawback of these adhesives is the formation of hydrolysis products which may be even more sticky than the Hima component itself.
* , .* Esillä olevan keksinnön tarkoituksena on aikaansaada parannettu lisäaine • · * • · · 20 käytettäväksi paperin ja kartongin valmistuksessa vähentämään edellämainittuja • · **· haittoja.It is an object of the present invention to provide an improved additive for use in the manufacture of paper and board to reduce the aforementioned disadvantages.
··· * • * « · • · · *···* Esillä olevan keksinnön tarkoituksena on tällöin erityisesti aikaansaada lisäaine, joka vähentää tahmeiden aggregaattien muodostumista.The object of the present invention is, in particular, to provide an additive which reduces the formation of sticky aggregates.
• « · • · · r ··· · • · · ί,.,ϊ Esillä olevan keksinnön tarkoituksena on tällöin myös aikaansaada lisäaine, joka ;*·*; 25 aikaansaa hydrofobiteetin lisäyksen paperi-ja kartonkituotteessa.It is also an object of the present invention to provide an additive which; * · *; 25 provides an increase in hydrophobicity in the paper and board product.
· · • · * » ‘1’ Esillä olevan keksinnön tarkoituksena on vielä aikaansaada parannettu menetelmä • * » · * : pihkaongelmien vähentämiseksi paperi-ja kartonkikoneella.It is a further object of the present invention to provide an improved method for reducing pitch problems in a paper and board machine.
«*MI"*MI
• * '.f •i 3 118090• * '.f • i 3 118090
Esillä olevan keksinnön tarkoituksena on vielä lisäksi aikaansaada parannettu menetelmä hydrofobiteetin, erityisesti ns. lyhytaikaisen hydrofobiteetin, nostamiseksi valmistetussa paperissa ja paperimassassa.It is a further object of the present invention to provide an improved process for hydrophobicity, particularly so-called. short-term hydrophobicity in manufactured paper and pulp.
Esillä olevan keksinnön tarkoituksena on myös aikaansaada parannettu menetelmä 5 hajuhaittojen vähentämiseksi valmistetussa paperissa ja kartongissa.It is also an object of the present invention to provide an improved method of reducing odor nuisance in manufactured paper and board.
Esillä mainittujen tarkoitusperien saavuttamiseksi ovat lisäaine ja menetelmä paperin ja kartongin valmistuksen parantamiseksi ja menetelmä paperi-ja kartonkituotteen parantamiseksi esillä olevan keksinnön mukaan tunnettuja siitä mitä on esitetty jäljempänä esitettyjen itsenäisten vaatimusten tunnusmerkkiosissa.To accomplish the aforementioned purposes, the additive and the method for improving the production of paper and board and the method for improving the paper and board product according to the present invention are known from those set forth in the characterizing parts of the independent claims below.
10 Tyypillinen keksinnön mukainen lisäaine käsittää ainakin yhden komponentin, joka sisältää rasvahappoglyseridejä, tyypillisesti triglyseridejä, joissa on korkea pitoisuus tyydyttämättömiä, erityisesti monityydyttämättömiä, rasvahappoja.A typical additive according to the invention comprises at least one component containing fatty acid glycerides, typically triglycerides having a high content of unsaturated, especially polyunsaturated, fatty acids.
Uskotaan, että komponentin tyydyttämättömät rasvahapot voivat muodostaa ristisidoksia niin lisätyssä komponentissa olevien glyseridien välillä kuin | 15 massasuspensiossa jo olevien glyseridien välillä, jolloin glyseridien polymerisaatio, ? niin sanottua kuivuminen, tulee tapahtumaan. : • · * * · · „ Uskotaan, että glyseridien tyydyttämättömät rasvahapot reagoivat ilman hapen • · ' ' . Ί* . kanssa, erityisesti korkeimmissa lämpötiloissa, muodostaen ristisidoksia glyseridien • · · .···. välillä. Tyydytettyjen rasvahappojen tai hartsihappojen ei uskota vastaavasti * · * · · 20 muodostavan ristisidoksia, jolloin vastaavaa polymerisaatiota ei uskota tapahtuvan.It is believed that unsaturated fatty acids in the component can cross-link between glycerides in the added component and | 15 between the glycerides already in the pulp suspension, whereby the polymerization of the glycerides,? the so-called dehydration, will happen. : • · * * · · “It is believed that the unsaturated fatty acids of glycerides react without oxygen • · ''. Ί *. , especially at the highest temperatures, forming cross-linkages of glycerides • · ·. ···. between. Saturated fatty acids or resin acids, respectively * · * · · 20 are not believed to form crosslinks, whereby corresponding polymerization is not expected to occur.
»··* • · ***’ Nyt on yllättäen huomattu, että on mahdollista vaikuttaa massasuspensiossa olevien . . lipofiilisten aineiden käyttäytymiseen lisäämällä tätä uutta lisäainetta, joka sisältää • · · • * · *11/ glyseridejä, edullisesti triglyseridejä, joissa on korkea pitoisuus tyydyttämättömiä, • · erityisesti monityydyttämättömiä, rasvahappoja. Lisäaine mahdollistaa esimerkiksi * i · 25 sen, että voidaan vaikuttaa tahmeiden aggregaattien muodostumiseen ja * · * * · .»·· * • · *** 'It has now been unexpectedly discovered that it is possible to influence those in the pulp suspension. . to the behavior of lipophilic substances by the addition of this novel additive containing • 11 · glycerides, preferably triglycerides with a high content of unsaturated fatty acids, in particular polyunsaturated fatty acids. For example, the additive allows * i · 25 to influence the formation of sticky aggregates and * · * * ·.
käyttäytymiseen massasuspensiossa ja paperi-tai kartonkirainassa, epämiellyttävien :*·* · hajujen muodostumiseen paperi- tai kartonkituotteessa ja/tai vaikuttaa lopullisen paperituotteen hydrofobiteettiin.behavior in the pulp suspension and on the paper or board web, the formation of unpleasant: * · * · odors in the paper or board product and / or the hydrophobicity of the final paper product.
118090 ? 4118090? 4
On huomattu, että on mahdollista nostaa glyseridien polymeroitumisnopeutta lisäämällä tyydyttämättömien, erityisesti monityydyttämättömien, rasvahappojen n määrää massasuspensiossa. Täten ei-polymeroituj en glyseridien, eli tahmeiden glyseridiaggregaattien, pitoisuus pienenee. Uskotaan myös, että polymeroidut 5 glyseridit voivat muodostaa kerrostumia massasuspensiossa ja paperirainalla olevien ; ei-polymeroitujen tahmeiden aggregaattien ympärille, näin pienentäen näiden tahmeiden aggregaattien negatiivista vaikutusta paperinvalmistusprosessissa.It has been found that it is possible to increase the rate of polymerization of glycerides by increasing the amount of unsaturated fatty acids, especially polyunsaturated fatty acids, in the pulp suspension. Thus, the content of non-polymerized glycerides, i.e. sticky glyceride aggregates, is reduced. It is also believed that the polymerized glycerides can form layers in the pulp suspension and in the paper web; around non-polymerized sticky aggregates, thus reducing the negative impact of these sticky aggregates in the papermaking process.
On huomattu että mitä suurempi on tyydyttämättömien, erityisesti monityydyttämättömien, rasvahappojen määrä massasuspensiossa sitä vähemmän 10 syntyy pihkan, eli tahmeiden aggregaattien aiheuttamia ajettavuusongelmia.It has been found that the higher the amount of unsaturated, especially polyunsaturated, fatty acids in the pulp suspension, the fewer the runner problems caused by the pitch, i.e. the sticky aggregates.
Tarvitaan tarpeeksi suuri tyydyttämättömien ja monityydyttämättömien rasvahappojen pitoisuus varmistamaan polymerisaatio. Yli 0,5 kg/t, tyypillisesti 0,5 -10 kg/t, tyypillisemmin 2 - 5 kg/t, glyseridilisäys, jossa on korkea monityydyttämättömien rasvahappojen pitoisuus, voi siten antaa toivotun tuloksen.A sufficiently high content of unsaturated and polyunsaturated fatty acids is required to ensure polymerization. More than 0.5 kg / h, typically 0.5-10 kg / h, more typically 2 to 5 kg / h, the addition of glyceride with a high content of polyunsaturated fatty acids can thus give the desired result.
15 Lisäaine, jossa tyydyttämättömien tai monityydyttämättömien rasvahappojen pitoisuus on korkea, voidaan lisätä massasuspensioon tai paperi-tai kartonkirainalle, esimerkiksi massa- tai pintaliimauksella. Lisäaine voidaan lisätä massasuspensioon massaliimauksena ennen perälaatikkoa, perälaatikossa tai ( ·;··· jossakin muussa sopivassa kohdassa. Lisäaine voidaan toisaalta lisätä märälle tai : 20 kuivalle rainalle mmm pintaliimauksen tai päällystyksen yhteydessä.15 An additive having a high content of unsaturated or polyunsaturated fatty acids may be added to the pulp suspension or to the paper or board web, for example by pulp or surface sizing. The additive may be added to the pulp suspension as a bulk sizing before the headbox, in the headbox or (·; ··· at any other convenient location. On the other hand, the additive may be added to wet or:
* * · ·.··.; ·-.* * · ·. ··.; · -.
• « " \, Komponentti pihkaongelmien tai epämiellyttävien hajujen vähentämiseksi tai * * • * · · .·*·, hydrofobiteetin lisäämiseksi voi siten esillä olevan keksinnön mukaan sisältää * · • · · ’ _ · ’ -rasvahappoglyseridejä, joissa yli 10 prosentissa, tyypillisesti yli 40 prosentissa, • rasvahapoista on enemmän kuin 1 kaksoissidos, * * · · :***; 25 -rasvahappoglyseridejä, joissa >60 prosentissa, edullisesti >65 prosentissa, * · · .·.··. tyypillisesti > 70 prosentissa, rasvahapoista, on 2 kaksoissidosta, ja/tai * .**·. - rasvahappoglyseridejä, joissa > 10 prosentissa, edullisesti > 30 prosentissa, • · · . tyypillisesti > 45 prosentissa, rasvahapoista on 3 kaksoissidosta.Thus, according to the present invention, a component to reduce pitch problems or unpleasant odors, or to increase hydrophobicity, may contain * · • · · '_ ·' fatty acid glycerides in which more than 10%, typically more than 40% fatty acids have more than 1 double bond * * · ·: ***; 25 fatty acid glycerides with> 60%, preferably> 65%, * · · · · · ·. , has 2 double bonds, and / or *. ** -. - fatty acid glycerides in which> 10%, preferably> 30%, typically> 45%, of the fatty acids have 3 double bonds.
· · • · · * ‘ Keksinnön mukainen komponentti voi olla raakaa tai osittain polymerisoitua 30 kasviöljyä, kuten auringonkukkaöljyä, joka sisältää suuren määrän ' 5 118090 linoli(C 18:2)happoa, ja/tai pellavaöljyä, joka sisältää suuren määrän linoleeni(C 18:3)happoa.The component of the invention may be crude or partially polymerized vegetable oils, such as sunflower oil containing a high amount of '5118090 linoleic (C 18: 2) acid, and / or linseed oil containing a high amount of linolenic (C). 18: 3) acid.
Keksinnön mukainen lisäaine voi mainitun komponentin lisäksi sisältää - yhtä tai useampaa emulsiota stabiloivaa ainetta, kuten luonnollisia tai synteettisiä 5 polymeerejä, esimerkiksi tärkkelyksiä, tärkkelysjohdannaisia, CMC:tä, mannaaneja, polyakryyliamideja, polyamiineja, - yhtä tai useampaa pinta-aktiivista ainetta ja/tai • ainakin yhtä tavanomaista liimakomponenttia, kuten synteettistä liima-ainetta.The additive of the invention may contain, in addition to said component, - one or more emulsion stabilizing agents, such as natural or synthetic polymers, for example starches, starch derivatives, CMCs, mannan, polyacrylamides, polyamines, - one or more surfactants, and / or at least one conventional adhesive component such as a synthetic adhesive.
Tyypillisesti voidaan käyttää kationisia emulsiota stabiloivia aineita. Tällöin 10 voidaan käyttää kationisia tärkkelysjohdannaisia, kuten - kylmään veteen liukenevia tärkkelyksiä, joiden DS (substituutioaste) on > 0,1 tai - tavanomaisia märänpään tärkkelyksiä, joiden DS on 0,01 - 0,05.Typically, cationic emulsion stabilizers may be used. Here, cationic starch derivatives such as - cold water soluble starches having a DS (degree of substitution) of> 0.1 or - conventional starch starches having a DS of 0.01 to 0.05 can be used.
Synteettisiä liima-aineita, kuten AKD, ASA, styreeniakrylaatti, , styreenimaleiinianhydridi tai styreeniakryylihappo kopolymeerejä, voidaan käyttää. , 15 Paperinvalmistusprosessissa massasuspensiot sisältävät normaalisti joitakin määriä f hartsihappoja ja rasvahappoja, jälkimmäiset esiintyvät vapaina happoina tai % esteröityinä glyserideinä. Massasuspensiossa olevat hartsi- ja rasvahapot voidaan • · · *·* * jakaa kahteen ryhmään: ♦ * # * · - kuivuvat hapot, eli tyydyttämättömät rasvahapot, kuten pinoleenihaappo tai # ♦ · 20 linoleenihappo (C18:3), linolihappo (Cl 8:2) ja Öljyhappo (C 18:1), ja * **! - ei-kuivuvat hapot, kuten hartsihappo ja tyydytetyt rasvahapot, kuten steariinihappo » .··· (Cl8:0), ante-iso-heptadekaanihappo (C17:0ai) ja palmitiinihappo (C16:0). v * * * ·Synthetic adhesives such as AKD, ASA, styrene acrylate, styrene maleic anhydride or styrene acrylic acid copolymers may be used. In the papermaking process, pulp suspensions normally contain some amounts of f resin acids and fatty acids, the latter occurring as free acids or as% esterified glycerides. The resin and fatty acids in the pulp suspension can be divided into two groups: ♦ * # * · - drying acids, i.e. unsaturated fatty acids such as pinolenic acid or # ♦ · 20 linolenic acid (C18: 3), linoleic acid (Cl 8: 2) and oleic acid (C 18: 1), and * **! non-drying acids such as resin acid and saturated fatty acids such as stearic acid. ··· (Cl8: 0), ante-iso-heptadecanoic acid (C17: 0ai) and palmitic acid (C16: 0). v * * * ·
Nyt on huomattu, että kuivuvien happojen, eli tyydyttämättömien rasvahappojen, « · · .It has now been found that drying acids, i.e. unsaturated fatty acids, «· ·.
* * ; · suhteella ei-kuivuviin happoihin, eli hartsihappoihin ja tyydytettyihin i* * · : vö *;* 25 rasvahappoihin, näyttää olevan tärkeä rooli glyseridien polymeroinnissa ja a · · *.* * kuivumisessa. Mitä korkeampi on tyydyttämättömien, erityisesti { f * * · * · w # 11 *···* monityydyttämättömien, rasvahappojen määrä verrattuna ei-kuivuvien * · ;.· · komponenttien määrään sen nopeammin polymerointi tulee tapahtumaan.* *; · Ratio to non-drying acids, i.e., resin acids and saturated fatty acids, seems to play an important role in the polymerization of glycerides and in the drying of a · · *. *. The higher the amount of unsaturated, especially {f * * · * · w # 11 * ··· * polyunsaturated fatty acids compared to the non-drying * ·;. · · Components, the faster polymerization will occur.
* • * ' 6 118090* • * '6 118090
Nyt on myös huomattu, että joidenkin ei-kuivuvien happojen hajoaminen massasuspensiossa tai paperi- tai kartonkirainassa saattaa muodostaa komponentteja, kuten heptaldehydiä tai hexaldehydiä, joka aiheuttaa erittäin epämiellyttävää hajua. Lisäksi on yllättäen huomattu että keksinnön mukaisella 5 rasvahappojen ja/tai glyseridien polymeroinnilla massasuspensiossa tai paperi- tai kartonkirainassa voidaan välttää hajua aiheuttavan hajoamisen tapahtuminen.It has now also been found that the decomposition of some non-drying acids in the pulp suspension or paper or board web may result in components such as heptaldehyde or hexaldehyde which cause a highly unpleasant odor. Furthermore, it has surprisingly been found that the polymerization of the fatty acids and / or glycerides of the invention in a pulp suspension or in a paper or board web can prevent odor-causing degradation.
Seuraavassa esimerkissä paperikoneella tehtyjen mittausten tulokset osoittavat että glyseridien polymerisointia massasuspensiossa tapahtuu samanaikaisesti kun tahmeita agglomeraatteja, eli pihkaongelmia, esiintyy vähemmän paperikoneella.In the following example, the results of measurements on a papermaking machine show that the polymerization of glycerides in the pulp suspension occurs simultaneously with less sticky agglomerates, i.e. pitch problems, occurring on the papermaking machine.
10 Esimerkki osoittaa että suhteellisen korkea kuivuvien happojen, eli tyydyttämättömien rasvahappojen, konsentraatio edistää glyseridien polymerointia.The example demonstrates that a relatively high concentration of drying acids, i.e. unsaturated fatty acids, promotes the polymerization of glycerides.
ESIMERKKIEXAMPLE
Näytteitä otettiin - paperituotteesta paperikoneen märässä päässä ja 15 - kuivatusta paperituotteesta.Samples were taken of: - Paper product at the wet end of a paper machine and 15 - dried Paper product.
Seuraavien rasvahappojen, ante-iso-heptadekaanihappo (Cl7:0ai), pinoleeni-ja :***; linoleenihappo (Cl8:3), linolihappo (Cl8:2) ja öljyhappo (Cl8:1), konsentraatio ·;··: analysoitiin jokaisessa näytteessä.The following fatty acids, ante-iso-heptadecanoic acid (Cl7: 0ai), pinolene and: ***; linolenic acid (Cl8: 3), linoleic acid (Cl8: 2) and oleic acid (Cl8: 1), concentration ·; ··: analyzed in each sample.
• 1 * · · ; * · · .·1·] Käytettiin analysointimenetelmää, joka • 1 • 1 20 - mittasi vapaiden rasvahappojen konsentraation kuten myös rasvahappojen : * • · « 1 konsentraation ei-polymerisoiduissa glyserideissä, mutta joka *··1 - ei mitannut rasvahappojen konsentraatiota polymeroiduissa glyserideissä.• 1 * · ·; * · ·. · 1 ·] An analytical method was used which • 1 • 1 20 - measured the concentration of free fatty acids as well as fatty acids: * • · «1 concentration in non-polymerized glycerides but which * ·· 1 - did not measure the concentration of fatty acids in polymerized glycerides .
·'·>! • · * 1 1 ' .· '·>! • · * 1 1 '.
* · 1 ‘.'I.1 Ante-iso-heptadekaanihapon (C17:0ai) konsentraatiota käytetiin referenssinä = 1.The concentration of ante-iso-heptadecanoic acid (C17: 0ai) was used as reference = 1.
* « • 4 · ** «• 4 · *
Seuraava melkein muuttumaton suhde eri rasvahappojen välillä voitiin huomata 25 kaikissa paperituotteen näytteissä, jotka otettiin paperikoneen märästä päästä.The following almost constant ratio between the different fatty acids could be observed in all the paper product samples taken from the wet end of the papermaking machine.
• 1 * · · • · 1 ·1· · · 118090 7 I C17:0ai Cl 8:3 Cl 8:2 C18:l ante-iso-hepta- pinoleeni-tai t dekaanihappo linoleenihappo linolihappo öljyhappo 1 noin 10 noin 15 noin 8 5 Näytteissä, jotka otettiin kuivuneesta paperituotteesta, saatiin sitä vastoin kaksi selvästi erilaista tulosta. Jatkokokeilla voitiin näyttää, että ero korreloi massasuspensiossa esiintyvän hartsihapon konsentraatioeron kanssa IIA C17:0ai C18:3 C18:2 C18:l ante-iso-hepta- pinoleeni- tai 10 dekaanihappo linoleenihappo linolihappo öljyhappo 1 noin 10 noin 15 noin 8 IIB C17:0ai C18:3 C18:2 C18:l ante-iso-hepta- pinoleeni-tai " dekaanihappo linoleenihappo linolihappo öljyhappo f 15 1 noin 1 noin 1 noin 4• 1 * · · • · 1 · 1 · · 118090 7 I C17: or Cl 8: 3 Cl 8: 2 C18 ante-iso-heptaprololene or t decanoic acid linoleic acid linoleic acid oleic acid 1 about 10 about 15 about In contrast, samples taken from the dried paper product gave two distinctly different results. Further experiments could show that the difference correlated with the difference in concentration of the resin acid in the pulp suspension IIA C17: or C18: 3 C18: 2 C18: ante-iso-heptapinolene or 10 decanoic acid linolenic acid oleic acid 1 about 10 about 8 IIB C17 C18: 3 C18: 2 C18: ante-iso-hepta-pinolene or "decanoic acid linolenic acid linoleic acid oleic acid f 15 1 about 1 about 1 about 4
Voidaan nähdä että näytteissä IIA mitatut tyydyttämättömien rasvahappojen :*·*· suhteelliset konsentraatiot ovat samat kuin märän pään paperituotteesta otetuista ·;**: näytteistä. Tämä näyttää että mitään tyydyttämättömien rasvahappojen * ; polymerisointia ei ole tapahtunut paperikoneella.It can be seen that the relative concentrations of unsaturated fatty acids: * · * · measured in Samples IIA are the same as in the wet end Paper Samples ·; **: samples. This seems to be nothing about unsaturated fatty acids *; polymerization has not occurred on a paper machine.
·» * * · * · . ..ty *·♦ .:. 20 Näytteissä IIB mitatut tyydyttämättömien rasvahappojen suhteelliset konsentraatiot ·*·· .**·. ovat huomattavasti alhaisempia kuin näytteissä IIA. Tämä näyttää että glyseridejä on *···* polymerisoitunut ja kuivunut tehden tyydyttämättömät rasvahapot ei mitattaviksi : käytetyllä analysointimenetelmällä.· »* * · * ·. ..ty * · ♦ .:. 20 Relative Concentrations of Unsaturated Fatty Acids Measured in Samples IIB · * ··. ** ·. are significantly lower than in samples IIA. This shows that the glycerides are * ··· * polymerized and dried, making the unsaturated fatty acids not measurable: the analytical method used.
• · * * ·*· • · ’·* Näytteet ΠΑ otettiin kun hartsihappokonsentraatio, eli ei-kuivuvan komponentin • · · .Samples ΠΑ were taken at the concentration of the resin acid, i.e., the non-drying component.
*;]/ 25 konsentraatio, massasuspensiossa oli korkea, yleensä yli 0,6 kg/t (valmiissa * * • · "* paperissa mitattuna) ja näytteet IIB otettiin kun hartsihappokonsentraatio oli matala, • · * · * ·£ !··’ : yleensä alle 0,6 kg/t (valmiissa paperissa mitattuna). Glyseridien polymeroinnin «·*·« nähtiin jatkuvan tässä nimenomaisessa massasuspensiossa niin kauan kuin 118090 8 hartsihapon konsentraatio pysyi alle 0,6 kg/t. Kun hartsihapon konsentraatio nousi niin polymerointinopeus laski.*;] / 25 concentration, high in pulp suspension, generally greater than 0.6 kg / t (measured in finished * * paper) and samples IIB were taken at low resin acid concentration, : generally less than 0.6 kg / h (measured in finished paper) Glyceride polymerization «· * ·« was seen to continue in this particular pulp suspension as long as the 118090 8 resin acid concentration remained below 0.6 kg / h. As the resin acid concentration increased, the polymerization rate decreased .
Siksi uskomme, että massasuspensiossa kuivuvien ja ei-kuivuvien uuteaineiden suhteella on tärkeä merkitys gjyseridien polymerisoinnissa. Täten 5 polymerisointinopeutta voidaan lisätä, kuten esillä olevassa keksinnössä on ehdotettu, lisäämällä kuivuvien rasvahappokomponenttien konsentraatiota.Therefore, we believe that the ratio of drying to non-drying extractants in the pulp suspension plays an important role in the polymerization of the glycerides. Thus, the polymerization rate can be increased as proposed in the present invention by increasing the concentration of the drying fatty acid components.
Tyydyttämättömiä, edullisesti monityydyttämättömiä, rasvahappoja voidaan käyttää tähän tarkoitukseen.Unsaturated, preferably polyunsaturated, fatty acids can be used for this purpose.
' . ' ' ' .4 ·«· * · · * * · * - /·>.'. '' '.4 · «· * · · * * · * - / ·>.
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Claims (21)
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20040519A FI118090B (en) | 2004-04-08 | 2004-04-08 | Additives, the use of additives in the production of paper and paperboard, the process for improving the production of paper and paperboard, and the procedure for improving paper and paperboard products |
| PCT/EP2005/003642 WO2005098131A1 (en) | 2004-04-08 | 2005-04-07 | An additive, use of said additive in paper or board production, a method of improving paper or board manufacturing and a method of improving paper or board product |
| CNA200580010351XA CN1938480A (en) | 2004-04-08 | 2005-04-07 | An additive, the use of said additive in the production of paper or board, a method of improving the manufacture of paper or board and a method of improving paper or board products |
| CA002559411A CA2559411A1 (en) | 2004-04-08 | 2005-04-07 | An additive having a fatty acid glycerides component having a high percentage of fatty acids, use of said additive in paper or board production, a method of improving paper or board manufacturing and a method of improving paper or board product |
| US11/547,572 US20080277085A1 (en) | 2004-04-08 | 2005-04-07 | Additive, Use of Said Additive in Paper or Board Production, a Method of Improving Paper or Board Manufacturing and a Method of Improving Paper or Board Product |
| EP05716550A EP1756361A1 (en) | 2004-04-08 | 2005-04-07 | An additive, use of said additive in paper or board production, a method of improving paper or board manufacturing and a method of improving paper or board product |
| US12/507,160 US20090283230A1 (en) | 2004-04-08 | 2009-07-22 | additive, use of said additive in paper or board production, a method of improving paper or board manufacturing and a method of improving paper or board product |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20040519A FI118090B (en) | 2004-04-08 | 2004-04-08 | Additives, the use of additives in the production of paper and paperboard, the process for improving the production of paper and paperboard, and the procedure for improving paper and paperboard products |
| FI20040519 | 2004-04-08 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| FI20040519A0 FI20040519A0 (en) | 2004-04-08 |
| FI20040519L FI20040519L (en) | 2005-10-09 |
| FI118090B true FI118090B (en) | 2007-06-29 |
Family
ID=32104169
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FI20040519A FI118090B (en) | 2004-04-08 | 2004-04-08 | Additives, the use of additives in the production of paper and paperboard, the process for improving the production of paper and paperboard, and the procedure for improving paper and paperboard products |
Country Status (6)
| Country | Link |
|---|---|
| US (2) | US20080277085A1 (en) |
| EP (1) | EP1756361A1 (en) |
| CN (1) | CN1938480A (en) |
| CA (1) | CA2559411A1 (en) |
| FI (1) | FI118090B (en) |
| WO (1) | WO2005098131A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2239369A1 (en) * | 2009-04-09 | 2010-10-13 | Kemira OYJ | Product for the sizing of paper |
| CN104894915A (en) * | 2015-05-20 | 2015-09-09 | 大唐国际发电股份有限公司高铝煤炭资源开发利用研发中心 | Papermaking adhesive control agent, and preparation method and application of control agent |
| CN109577076A (en) * | 2018-12-26 | 2019-04-05 | 江苏理文造纸有限公司 | A kind of filler and preparation method thereof for liner board |
Family Cites Families (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1958614A (en) * | 1925-10-10 | 1934-05-15 | Ellis Foster Co | Resinous products or compositions including lacquers, paints, varnishes and other coating compositions |
| US1672705A (en) * | 1927-07-28 | 1928-06-05 | Bradshaw Lawrence | Sized cellulose-fiber product and process of making |
| US1956961A (en) * | 1931-02-28 | 1934-05-01 | Reid James | Treated paper and process of producing the same |
| US1941536A (en) * | 1932-05-18 | 1934-01-02 | Masonite Corp | Hard vegetable fiber product of high strength and process of making same |
| US3102065A (en) * | 1961-03-22 | 1963-08-27 | Virginia Chemicals & Smelting | Method and composition for dispersing of pitch |
| US3251732A (en) * | 1962-09-06 | 1966-05-17 | Hercules Powder Co Ltd | Rosin size and method of preparing same and paper sized therewith |
| US3274050A (en) * | 1963-04-29 | 1966-09-20 | Buckman Labor Inc | Pitch control in pulp and papermaking |
| US3438807A (en) * | 1965-12-15 | 1969-04-15 | Union Carbide Corp | Silicone sized paper and cellulosic fiber |
| US4950420A (en) * | 1988-08-31 | 1990-08-21 | Nalco Chemical Company | Antifoam/defoamer composition |
| US5256252A (en) * | 1992-07-15 | 1993-10-26 | Nalco Chemical Company | Method for controlling pitch deposits using lipase and cationic polymer |
| US20020099067A1 (en) * | 1993-07-08 | 2002-07-25 | Ulrich Posanski | Pharmaceutical compositions for sparingly soluble therapeutic agents |
| US5685815A (en) * | 1994-02-07 | 1997-11-11 | Hercules Incorporated | Process of using paper containing alkaline sizing agents with improved conversion capability |
| DE4424532A1 (en) * | 1994-07-12 | 1996-01-18 | Henkel Kgaa | Use of alkoxylation products of carboxylic acid derivatives and / or carboxylic acids containing OH groups |
| DE19515273A1 (en) * | 1995-04-26 | 1996-10-31 | Henkel Kgaa | Process for controlling the settling of sticky contaminants from pulp suspensions |
| AU4729697A (en) * | 1997-09-09 | 1999-03-29 | Peterson Seffle Aktiebolag | Packaging material |
| US6102065A (en) * | 1999-02-03 | 2000-08-15 | Tobias; Stewart W. | Liquid propane delivery system |
| US6576049B1 (en) * | 2000-05-18 | 2003-06-10 | Bayer Corporation | Paper sizing compositions and methods |
| DE10133399A1 (en) * | 2001-07-13 | 2003-01-23 | Cognis Deutschland Gmbh | Low water-content wax-based composition for impregnating tissue paper or wet wipes to give body-care material contains dialkyl(ene) ether, dialkyl(ene) carbonate, dicarboxylic acid and/or hydroxyfatty alcohol |
| CN100336970C (en) * | 2001-10-23 | 2007-09-12 | 诺维信公司 | Oxidizing enzymes in the manufacture of paper materials |
| US20030124710A1 (en) * | 2001-10-23 | 2003-07-03 | Novozymes A/S | Oxidizing enzymes in the manufacture of paper materials |
-
2004
- 2004-04-08 FI FI20040519A patent/FI118090B/en not_active IP Right Cessation
-
2005
- 2005-04-07 CA CA002559411A patent/CA2559411A1/en not_active Abandoned
- 2005-04-07 WO PCT/EP2005/003642 patent/WO2005098131A1/en not_active Ceased
- 2005-04-07 CN CNA200580010351XA patent/CN1938480A/en active Pending
- 2005-04-07 EP EP05716550A patent/EP1756361A1/en not_active Withdrawn
- 2005-04-07 US US11/547,572 patent/US20080277085A1/en not_active Abandoned
-
2009
- 2009-07-22 US US12/507,160 patent/US20090283230A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| WO2005098131A1 (en) | 2005-10-20 |
| US20080277085A1 (en) | 2008-11-13 |
| CN1938480A (en) | 2007-03-28 |
| US20090283230A1 (en) | 2009-11-19 |
| CA2559411A1 (en) | 2005-10-20 |
| FI20040519L (en) | 2005-10-09 |
| FI20040519A0 (en) | 2004-04-08 |
| EP1756361A1 (en) | 2007-02-28 |
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