WO2006081845A1 - Utilisation d'arabinoxylanes en tant qu'additifs dans la fabrication du papier - Google Patents
Utilisation d'arabinoxylanes en tant qu'additifs dans la fabrication du papier Download PDFInfo
- Publication number
- WO2006081845A1 WO2006081845A1 PCT/EP2005/009657 EP2005009657W WO2006081845A1 WO 2006081845 A1 WO2006081845 A1 WO 2006081845A1 EP 2005009657 W EP2005009657 W EP 2005009657W WO 2006081845 A1 WO2006081845 A1 WO 2006081845A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pulp
- arabinoxylan
- arabinoxylans
- xylan
- paper
- Prior art date
Links
Classifications
-
- 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
- D21C5/00—Other processes for obtaining cellulose, e.g. cooking cotton linters ; Processes characterised by the choice of cellulose-containing starting materials
- D21C5/005—Treatment of cellulose-containing material with microorganisms or enzymes
-
- 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
- D21H17/22—Proteins
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
Definitions
- the present invention relates to the use of arabinoxylans as an additive in papermaking.
- the mechanical properties of paper are influenced by a number of different parameters, both chemical and physical.
- Several theories for explaining the tear strength properties of paper have been proposed, most of which emphasize the particular relevance of fiber-to-fiber bonding.
- xylans from the raw material wood and its secondary product pulp is discussed. Specifically, the use of softwood acetyl-4-O-methyglucuronoxylan and softwood arabino-4-O-methylglucuronoxylan is cited.
- the examples of the use of xylans call the lenzing xylan. This product is obtained by alkaline extraction of beech wood pulp in the viscose process and has only low degrees of polymerization of about 35.
- various xylans have been investigated for their properties for fiber properties or as a paper additive. However, the work mentioned shows that an improvement in the breaking length is accompanied by a decrease in other strength properties or unacceptable deterioration of the optical properties.
- An object of the invention is therefore the use of arabinoxylans as an additive in papermaking.
- Suitable arabinoxylans are polysaccharides which are found, for example, in various annual plants and agricultural residues such as e.g. Oat husks, straw or corn is included.
- the arabinoxylans can be prepared by a variety of extraction techniques, e.g. with water, steam or solvents using a variety of auxiliary chemicals and by enzymatic isolation and purification steps.
- alkaline extracted arabinoxylans and especially arabinoxylans from oat hulls are used, e.g.
- the peculiarity of the arabinoxylans from oat husks in comparison to the xylans from hardwood and softwood is that they have a comparatively high number of arabinose substituents but not the 4-0-methylglucuronic acids occurring in deciduous and coniferous xylans. Compared to xylans from pulps such as Lenzing xylan, the arabinoxylans have a much higher chain length.
- arabinoxylans are understood to mean those xylans which have 5 to 20% (w / w based on the total sample), preferably 7 to 15%, particularly preferably 8 to 13%, arabinose substituents on their main chain, and less than 5 %, preferably less than 2%, more preferably less than 1% carry 4-O-methylglucuronic acid substituents (chromatographic determination of sugar after acid hydrolysis).
- Arabinoxylans obtained by extraction of oat hulls with aqueous alkaline solution to give an alkaline extract and subsequent precipitation of the alkaline extract in a precipitation bath of water and a water-miscible organic liquid A, whereby the alkaline extract is not neutralized prior to precipitation, are particularly preferred.
- Such arabinoxylans usually have chain lengths of at least 100 after a possible bleaching stage. In most cases, the chain lengths of these arabinoxylans are in the range 120 to 240.
- Another object of the invention is a process for producing a pulp comprising contacting a concentrated solution or suspension of a arabinoxylans with pulp or a pulp system containing pulp.
- the arabinoxylan solution or suspension is added to the fiber suspension prior to foliar formation.
- the action of the arabinoxylan also takes place in combination with other paper chemicals which are introduced into the pulp before, after or together with the arabinoxylan.
- the use of arabinoxylan for the various products of the paper industry is advantageous.
- paper chemicals include, for example, wet strength agents, fillers, retention aids, fixatives, defoamers, deaerators, sizing agents, optical brighteners, and colorants.
- a homogeneous solution or suspension of arabinoxylans can be achieved, for example, by strong mechanical stress such as stirring, by the action of temperature or by means of chemicals, preferably basic chemicals such as alkali metal or alkaline earth metal hydroxides, preferably NaOH.
- concentration of the arabinoxylan solution or suspension can be varied within a wide range of 0.1% to 40% (w / w). Preferably, the range is from 0.1 to 25% (w / w), more preferably the range from 0.5% to 10% (w / w).
- the arabinoxylan solution or suspension may then be incubated with the pulp and the desired paper aides and high consistency additives (solids content) of up to 20% before the pulp enters the headbox of the paper machine. Then you can go through Squeezing off the supernatant solution may use unadsorbed chemicals for the next batch.
- the pulp in the headbox i. immediately before entering the papermaking machine with the additives and the arabinoxylan solution or suspension in any order.
- the addition of arabinoxylans in the headbox usually achieves better results than the previous incubation with the pulp.
- arabinoxylan solution or suspension is added to the pulp suspension prior to milling the pulp fibers.
- the optimum amount used depends on which other paper auxiliaries are used in the mass, so that the amount used of the arabinoxylans based on pulp in a wide range of 0.1% up to 40% (w / w) are varied. Preferably, however, amounts of from 0.5 to 10% of arabinoxylan are used. In most cases, the use of paper additives already at lower Arabinoxylankonzentrationen the optimum increase in strength is achieved.
- compositions of xylans are given as% w / w based on the total sample, obtained by chromatographic determination of sugar after acid hydrolysis.
- a 4-0-methylglucuronoxylan from birch wood (no arabinose side chains, 8.8% molar ratio of 4-O-methylglucuronic acid based on xylose units, determined by 1 H-NMR, DP ca. 95) was used as a 5% solution in water dissolved under heating. 20 g of softwood sulfite pulp were suspended in water and mixed with the xylan solution. For tests with higher amounts of xylan solution, correspondingly smaller amounts of water were used to suspend the pulp. After addition of the xylan suspensions, the pulp consistency was 7.1% in each case. The experimental batches were each incubated for 2 h at 50 ° C. After incubation, the pulp was sucked through a suction filter.
- the Lenzing xylan from beech wood pulp (no arabinose side chains, about 1% 4-O-methylglucuronic acid, DP about 35) was dissolved as a 5% solution in water with heating. 20 g of softwood sulfite pulp were suspended in water and mixed with the xylan solution. For tests with higher amounts of xylan solution, correspondingly smaller amounts of water were used to suspend the pulp. After addition of the xylan suspensions, the pulp consistency was 7.1% in each case. The experimental batches were each incubated for 2 h at 50 ° C. After incubation, the pulp was sucked through a suction filter.
- the tear length can be improved by the addition of arabinoxylan from oat husks compared to the reference experiment by more than 1000 m. In this addition mode, increases in strength can be achieved even at lower levels of arabinoxylan use.
- the dosage of the paper additive was consistent with a charge density of 0.013 meq / g of pulp in all experiments carried out. Subsequently, the metered addition of the Arabinoxylantheen was made. After 5 minutes, the portioning and the formation of the test sheets. All experiments were carried out at room temperature. The testing of the strengths was carried out according to ISO 974 (DIN EN 21974).
- the tear length can be significantly increased again by the addition of arabinoxylan compared to the reference experiment. It is clear from the reference that the strengths are generally at a higher level due to the use of the paper additive. However, a synergistic effect becomes apparent in the interaction with the paper additive for the action of the arabinoxylan. The increases in the breaking length are now even up to about 1800 m. The higher increases in strength are effective even at significantly lower Arabinoxylan transitmengen than in the trials without paper additive.
- the specific volume of the pulps is designated by the BuIk, which is plotted in FIG. 2 against the Tensile Tensile Strength (Influence of Arabinoxylan from Oat Spelts (9.38% on Pulp) on the Bulk Tensile Plot of Beech Sulfite Pulp) , It becomes clear that the curve for the different points of the freewheeling curve is shifted to higher BuIk values. To produce a product with the desired strengths, a higher sheet volume can be generated by adding the arabinoxylan. The increased BuIk leads to an increase in the light scattering coefficient and thus to better optical properties.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Biochemistry (AREA)
- Microbiology (AREA)
- Paper (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
L'invention se rapporte à l'utilisation d'arabinoxylanes en tant qu'additifs dans la fabrication du papier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002586187A CA2586187A1 (fr) | 2005-02-02 | 2005-09-08 | Utilisation d'arabinoxylanes en tant qu'additifs dans la fabrication du papier |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP05002073.4 | 2005-02-02 | ||
EP05002073A EP1688534A1 (fr) | 2005-02-02 | 2005-02-02 | L'utilisation de Arabinoxylanes pour la production de papier |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2006081845A1 true WO2006081845A1 (fr) | 2006-08-10 |
Family
ID=34933545
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2005/009657 WO2006081845A1 (fr) | 2005-02-02 | 2005-09-08 | Utilisation d'arabinoxylanes en tant qu'additifs dans la fabrication du papier |
Country Status (5)
Country | Link |
---|---|
US (1) | US20060169432A1 (fr) |
EP (1) | EP1688534A1 (fr) |
CA (1) | CA2586187A1 (fr) |
RU (1) | RU2007116306A (fr) |
WO (1) | WO2006081845A1 (fr) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2500201C (fr) * | 2002-10-01 | 2010-07-13 | The Procter & Gamble Company | Produits papier en ouate cellulosique renforcee a faible teneur en xylane |
US20080128100A1 (en) * | 2002-10-01 | 2008-06-05 | Frank Rehders | Strengthened tissue paper products comprising low level of xylan |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0538177A1 (fr) * | 1991-10-18 | 1993-04-21 | Novo Nordisk A/S | Xylanases de souches de Rhodothermus et leur utilisation pour le traitement de pâte de liquocellulose |
WO1997027293A1 (fr) * | 1996-01-22 | 1997-07-31 | Novo Nordisk A/S | Enzyme possedant une activite de type xylanase |
US5834301A (en) * | 1992-03-25 | 1998-11-10 | The United States Of America As Represented By The Secretary Of Agriculture | Method of removing color from kraft wood pulps |
US5902581A (en) * | 1995-12-04 | 1999-05-11 | Genencor International, Inc. | Xylanase from acidothermus cellulolyticus |
EP1039020A1 (fr) * | 1999-03-23 | 2000-09-27 | Oji Paper Co., Ltd. | Procede de blanchiment de pate lignocellulosique |
US20030124192A1 (en) * | 2000-01-05 | 2003-07-03 | Fitchett Colin Stanley | Pharmaceutical compositions and their preparation |
WO2004082381A1 (fr) * | 2003-03-14 | 2004-09-30 | Laboratoires Goëmar S.A. | Nouveau procede pour la potentialisation et la stimulation des defenses naturelles des plantes |
EP1479765A2 (fr) * | 1993-03-10 | 2004-11-24 | Novozymes A/S | Enzymes dérivées d'aspergillus aculeatus présentant une activité de xylanase |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5444217A (en) * | 1993-01-21 | 1995-08-22 | Moore Epitaxial Inc. | Rapid thermal processing apparatus for processing semiconductor wafers |
DE4409372A1 (de) * | 1994-03-18 | 1995-09-21 | Schickedanz Ver Papierwerk | Verfahren zur Herstellung von gekrepptem Hygiene-Zellstoffpapier |
US6942754B2 (en) * | 1999-03-23 | 2005-09-13 | Oji Paper Co., Ltd. | Process for producing xylooligosaccharide from lignocellulose pulp |
US6824646B2 (en) * | 1999-03-23 | 2004-11-30 | Oji Paper Co., Ltd. | Process for oxygen bleaching and enzyme treating lignocellulosic pulp with liquid treatment and recovery |
CA2500201C (fr) * | 2002-10-01 | 2010-07-13 | The Procter & Gamble Company | Produits papier en ouate cellulosique renforcee a faible teneur en xylane |
-
2005
- 2005-02-02 EP EP05002073A patent/EP1688534A1/fr not_active Withdrawn
- 2005-09-08 RU RU2007116306/12A patent/RU2007116306A/ru unknown
- 2005-09-08 WO PCT/EP2005/009657 patent/WO2006081845A1/fr not_active Application Discontinuation
- 2005-09-08 CA CA002586187A patent/CA2586187A1/fr not_active Abandoned
- 2005-09-20 US US11/231,016 patent/US20060169432A1/en not_active Abandoned
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0538177A1 (fr) * | 1991-10-18 | 1993-04-21 | Novo Nordisk A/S | Xylanases de souches de Rhodothermus et leur utilisation pour le traitement de pâte de liquocellulose |
US5834301A (en) * | 1992-03-25 | 1998-11-10 | The United States Of America As Represented By The Secretary Of Agriculture | Method of removing color from kraft wood pulps |
EP1479765A2 (fr) * | 1993-03-10 | 2004-11-24 | Novozymes A/S | Enzymes dérivées d'aspergillus aculeatus présentant une activité de xylanase |
US5902581A (en) * | 1995-12-04 | 1999-05-11 | Genencor International, Inc. | Xylanase from acidothermus cellulolyticus |
WO1997027293A1 (fr) * | 1996-01-22 | 1997-07-31 | Novo Nordisk A/S | Enzyme possedant une activite de type xylanase |
EP1039020A1 (fr) * | 1999-03-23 | 2000-09-27 | Oji Paper Co., Ltd. | Procede de blanchiment de pate lignocellulosique |
US20030124192A1 (en) * | 2000-01-05 | 2003-07-03 | Fitchett Colin Stanley | Pharmaceutical compositions and their preparation |
WO2004082381A1 (fr) * | 2003-03-14 | 2004-09-30 | Laboratoires Goëmar S.A. | Nouveau procede pour la potentialisation et la stimulation des defenses naturelles des plantes |
Also Published As
Publication number | Publication date |
---|---|
EP1688534A1 (fr) | 2006-08-09 |
US20060169432A1 (en) | 2006-08-03 |
RU2007116306A (ru) | 2009-03-10 |
CA2586187A1 (fr) | 2006-08-10 |
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