EP2029806A2 - Procédé de préparation de matière fibreuse - Google Patents

Procédé de préparation de matière fibreuse

Info

Publication number
EP2029806A2
EP2029806A2 EP07723953A EP07723953A EP2029806A2 EP 2029806 A2 EP2029806 A2 EP 2029806A2 EP 07723953 A EP07723953 A EP 07723953A EP 07723953 A EP07723953 A EP 07723953A EP 2029806 A2 EP2029806 A2 EP 2029806A2
Authority
EP
European Patent Office
Prior art keywords
wood
digestion
chemicals
chemical solution
annual plants
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.)
Withdrawn
Application number
EP07723953A
Other languages
German (de)
English (en)
Inventor
Esa-Matti Aalto
Hans-Ludwig Schubert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Voith Patent GmbH
Original Assignee
Voith Patent GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from DE200610027006 external-priority patent/DE102006027006A1/de
Priority claimed from DE200610061480 external-priority patent/DE102006061480A1/de
Application filed by Voith Patent GmbH filed Critical Voith Patent GmbH
Publication of EP2029806A2 publication Critical patent/EP2029806A2/fr
Withdrawn legal-status Critical Current

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
    • D21C3/00—Pulping cellulose-containing materials
    • 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
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/02—Chemical or chemomechanical or chemothermomechanical pulp
    • D21H11/06—Sulfite or bisulfite 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
    • D21C3/00—Pulping cellulose-containing materials
    • D21C3/22—Other features of pulping processes
    • D21C3/222—Use of compounds accelerating the pulping processes

Definitions

  • the invention relates to a process for the production of pulp from wood or annual plants with a lignin content of more than 15% for softwoods, for hardwoods of more than 12% and for annual plants of more than 10%, in each case based on the produced otro pulp, wherein the Fiber has predetermined strength properties.
  • Processes which produce pulps with a relatively high lignin content of over 15% for softwood and over 12% for hardwood. They provide a yield of 70% or more based on the starting material used. These methods are based on chemical and / or mechanical decomposition of the wood.
  • CTMP pulps are typically made with chemical levels of 3% to 5%.
  • industrially established processes for the production of high yield fibers eg. As the NSSC process, up to 10% chemicals are used based on the starting material. With such a limited use of chemicals, no recovery for the recovery of the chemicals is yet to be installed.
  • this type of pulp production leads to a considerable environmental, especially water pollution, not only because of the chemical entry but mainly because of the organic cargo that is discharged into the receiving waters.
  • High yield pulps are ground to high levels of grinding for current uses. Only then will they reach an acceptable level of strength.
  • a high grinding degrees are here values of about 300 ml CSF (Canadian Standard Freeness), equivalent to 41 0 SR (Schopper-Riegler, see below) and 500 ml CSF, equivalent to 26 "SR to look at as it z. B. 80, No. 12, December 1979, for high yield pulps from softwood
  • the fibers are rubbed against each other or on a grinder or on a grinding media and thus changed in their surface properties towards a better bonding behavior.
  • the high degree of grinding is therefore not an end in itself. It results rather from the requirements of the strength properties of the fiber.
  • the high yield fibers produced by mechanical and / or chemical means are used in particular where it is not absolutely necessary to have a high final whiteness and high whiteness stability. They could open up many more applications if the strength level could be increased.
  • This object is achieved with a method for the production of pulp from wood or annual plants with a lignin content of at least 15% for softwood and 12% for hardwood and 10% for annual plants, each based on the otro fiber mass, with the steps:
  • the method according to the invention is based on the fact that higher quantities of chemicals are used for the production of high-yield fibers than has hitherto been customary. More than 5% of softwood chemicals are well above the hitherto common chemicals levels for engineering pulp production, also more than 3.5% for hardwood and 2.5% for annual plants. This high use of chemicals yields fibers with good yield and excellent strength properties. Thus, for softwood at grinding degrees of only 12 0 SR to 15 0 SR, breaking lengths of more than 8 km, but also breaking lengths of more than 9 km and more than 10 km are measured. For deciduous trees, values of more than 5 km, but also breaking lengths of more than 6 km and more than 7 km are measured at only 20 0 SR. This achieves the desired high level of strength.
  • Suitable annual plants are, in particular, bamboo, hemp, rice straw, bagasse, wheat, miscanthus or the like.
  • the fibrous materials produced by the process according to the invention have tear lengths of more than 8 km up to 11 km and tear strengths of more than 70 cN up to more than 110 cN, even at degrees in the range from 12 ° SR to 15 ° SR Leaf weight of 100 g / m 2 .
  • These low freeness levels are also achieved with a low specific demand for grinding energy, which is less than 500 kWh / t pulp for softwood pulps, and for hardwood pulp the demand for grinding energy may even be less than 300 kWh / t pulp.
  • the realization that the high level of strength already at low degrees of grinding of 12 0 SR to 15 0 SR for softwood and 20 0 SR for hardwood and below is achieved is an essential part of the invention.
  • Lignin content can be maintained.
  • the inventive method is also suitable for the production of softwood pulps with a lignin content of more than 18%, preferably more than 21%, preferably more than 24% based on the otro
  • Fiber mass Hardwood fibrous materials with a lignin content of more than 14%, preferably more than 16%, more preferably more than 18% and also
  • %, in particular more than 19% can also be produced by the process according to the invention and show a high level of strength.
  • the composition of the chemical solution used for the digestion can be determined in accordance with the wood to be broken or the annual plants and the desired pulp properties. As a rule, only one sulfite component is used. Alternatively or in addition, a sulfide component may be added. Digestion with a sulfite component is not disturbed by the presence of sulfide components. Technically, sodium sulfite is usually used, but also the use of ammonium or potassium sulfite or magnesium bisulfite is possible. In particular, when high amounts of sulfite are used, can be dispensed with the use of an alkaline component, because even without the addition of alkaline components, a high pH value sets, which favors the digestion.
  • an acidic and / or an alkaline component can be added.
  • the alkaline component is usually sodium hydroxide (NaOH) is used.
  • NaOH sodium hydroxide
  • carbonates in particular sodium carbonate. All information on chemical quantities of the digestion process in this document, eg. As for the total use of chemicals or for the distribution of the sulfite component and the alkaline component, unless otherwise stated, are each calculated and reported as sodium hydroxide (NaOH).
  • acids can be added to adjust the desired pH.
  • preference is given to the addition of SO 2 , if appropriate in aqueous solution. It is inexpensive and readily available, especially if the spent chemical solution z. B. based on sodium sulfite, after digestion is prepared for further use.
  • Optimal is a use of z.
  • anthraquinone which is between 0.005% and 0.5%.
  • Use of anthraquinone of up to 1% also provides the desired effect.
  • a use of more than 3% anthraquinone is usually uneconomical.
  • a chemical solution is prepared. Usually an aqueous solution is used.
  • organic solvents may be provided.
  • the Mixing ratio of water and alcohol can be optimized for the respective raw material in a few experiments.
  • the amount of chemicals to be used according to the invention for producing a pulp with a yield of at least 70% is at least 5% for softwood, at least 3.5% for hardwood and at least 2.5% for annual plants, in each case based on the otro wood or annual plant mass to be broken up.
  • the quality of the produced pulp shows the best results with a chemical use of up to 15% for softwoods up to 10% for hardwood and up to 10% for annual plants. Preference is given to between 9% and 11% chemicals based on the used otro wood in softwood added. For hardwoods, the use of chemicals is rather lower, preferably between 4% and 10%, more preferably between 6% and 8% and in annual plants between 3 and 10%.
  • a ratio between an alkaline component and sulfur dioxide (SO 2 ) can be adjusted within a wide range.
  • SO 2 is mentioned here as representative of the above-mentioned acidic component. So it can be used instead of SO 2 and an acid. Since the possibly added quinone component is used only in minimal amounts, usually well below 1%, it is negligible for setting this ratio.
  • a ratio of alkaline component: SO 2 in a range of 4: 1 to 1.6: 1 is well suited to carry out the process according to the invention and to achieve fibers with high strength properties.
  • a customary, particularly suitable range is between 2: 1 and 1.6: 1.
  • the adjustment of the proportionate components takes place depending on the raw material to be digested and the respectively selected process control (digestion temperature, digestion time, impregnation).
  • the process of the invention can be carried out in a wide pH range.
  • the ratio of alkaline component to acidic component or the use of an acidic or an alkaline component can be adjusted so that at the beginning of the process, a pH between 6 and 11, preferably between 7 and 11, more preferably between 7.5 and 10 is set.
  • the method according to the invention is tolerant with regard to the pH; There are few chemicals required for pH adjustment. This has a favorable effect on the costs of chemicals.
  • acid or alkaline component arises, for.
  • a pH between 8 and 10 usually between 8.5 and 9.5 in the free-flowing chemical solution and the dissolved organic components that have been liquefied by the digestion, a.
  • the dissolved organic components are mainly lignosulfonates.
  • the liquor ratio ie the ratio of the amount of otro wood or annual plants to the chemical solution, is set between 1: 1, 5 and 1: 6.
  • a liquor ratio of 1: 3 to 1: 5 is preferred. In this range, a good and simple mixing and impregnation of the material to be digested is ensured.
  • For softwood a liquor ratio of 1: 4 is preferred.
  • the liquor ratio can also be significantly higher to allow rapid wetting and impregnation.
  • the concentration of the chemical solution can be kept so high that the liquid volumes to be circulated are not too large.
  • the mixture or impregnation of the wood or Einjährauf gleichgut preferably takes place at elevated temperatures. Heating the chips and the chemical solution up to 110 0 C, preferably up to 120 0 C, more preferably up to 130 0 C leads to a rapid and uniform digestion of the wood.
  • For the mixing or impregnation of the wood chips is a period of up to 30 minutes, preferably up to 60 minutes, more preferably from to advantageous to 90 minutes. The optimum time depends, among other things, on the amount of chemicals and the liquor ratio and the type of digestion (liquid or vapor phase).
  • the digestion of the mixed with the chemical solution or impregnated lignocellulosic material is preferably carried out at temperatures between 120 0 C and 190 0 C, preferably between 150 0 C and 180 0 C.
  • temperatures between 155 0 C and 170 0 C. set. Higher or lower temperatures can be adjusted, but in this temperature range, the energy required to heat and accelerate the digestion are in an economic relationship. Higher temperatures can also have a negative effect on the strength and whiteness of the fibers.
  • the pressure generated by the high temperatures can be easily absorbed by appropriate design of the digester.
  • the duration of the heating is only a few minutes, usually up to 30 minutes, advantageously up to 10 minutes, in particular when heated by means of steam.
  • the duration of the heating can take up to 90 minutes, preferably up to 60 minutes, z. B. when it is digested in the liquid phase and the chemical solution is to be heated together with the wood chips.
  • the duration of the digestion is chosen especially depending on the desired pulp properties.
  • the duration of the digestion can be shortened to up to 2 minutes, z. B. in the case of a vapor phase digestion of a hardwood with low lignin content. But it can also be up to 180 minutes, if z. B. the digestion temperature low and the natural lignin content of the réelleumbleden wood is high. Even if the initial pH of the digestion is in the neutral range, a long digestion time may be required.
  • the digestion time is up to 90 minutes, especially in coniferous wood.
  • the digestion time is up to 60 minutes, advantageously up to 30 minutes.
  • a digestion time of up to 60 minutes is mainly considered for hardwoods.
  • the digestion time is up to 90 minutes.
  • a quinone component in particular anthraquinone, allows a reduction the digestion time up to 25% of the time required without addition of anthraquinone. If the use of quinone components is omitted, the digestion time is extended by more than one hour, for example from 45 minutes to 180 minutes, for comparable digestion results.
  • the duration of the digestion is set as a function of the selected liquor ratio.
  • Chemical consumption is recorded as the amount of chemicals measured in terms of the original amount of chemicals after removal or separation of the chemical solution and, if necessary, detection of chemical solution measured after defibration or in conjunction with detection of the chemical solution.
  • the consumption of chemicals depends on the absolute amount of chemicals used for the digestion, based on the otro wood mass to be digested. The higher the use of digestion chemicals, the lower the direct sales of chemicals. When using 27.5% of chemicals based on otro wood pulp, for example, only about 30% of the chemicals used are consumed. However, when 15% of the chemicals are used in relation to otro wood, 60% of the chemicals used are consumed, as demonstrated in laboratory tests.
  • the consumption of chemicals for the process according to the invention is up to 80%, preferably up to 60%, according to a preferred embodiment of the process during the digestion. particularly preferably up to 40%, advantageously up to 20%, particularly advantageously up to 10%, of the chemical used at the beginning of the digestion.
  • the chemical consumption for producing one ton of pulp is about 6% to 14% sulfite and / or sulfide component and possibly alkaline and / or acidic component and possibly quinone component based on otro pulp (hardwood and softwood or annual plants).
  • this amount of chemicals is sufficient to produce a pulp having the predetermined properties.
  • up to 30% chemicals based on otro wood or annual plant mass As the above mentioned up to 30% chemicals based on otro wood or annual plant mass. The use of these amounts of chemicals at the beginning of the digestion shows advantageous effect, since the fibers obtained in this way have previously unavailable properties, in particular high strength properties and high degrees of whiteness.
  • Excess chemicals are present after mixing and impregnating the wood with the chemical solution or after digestion in the free flowing liquid. This excess is deducted before digestion (1st alternative) or after digestion (2nd alternative).
  • the composition of the removed chemical solution is detected and then adjusted to a predetermined composition for re-use for the production of fibers.
  • At least some of the chemicals used for digestion have - as described above - penetrated into the material to be digested and / or has been consumed in the digestion. The unused chemicals can easily be used again for the next digestion.
  • the chemical solution contains no or only very few substances, especially when removed before digestion, but also when removed after digestion, which is the next time the recovered chemical solution is used again Disruption proves to be annoying.
  • the method according to the invention which aims to provide an oversupply of digestion chemicals during impregnation, can thus be extremely economical despite the initially uneconomic approach of high chemical use, because the removal or separation and the strengthening of the chemical solution can be carried out easily and inexpensively.
  • the process of the invention is specifically controlled so that only as little of the starting material used is degraded or dissolved.
  • the aim is to produce a pulp which has a lignin content of at least 15% based on the otro fiber mass for softwood, preferably a lignin content of at least 18%, more preferably 21%, advantageously at least 24%.
  • For hardwood is sought to achieve a lignin content of at least 12% based on the otro fiber mass, preferably of at least 14%, more preferably of at least 16%, advantageously of at least 18%.
  • the preferred lignin content is between 10 and 28%, in particular between 12 and 26%.
  • the yield of the process according to the invention is at least 70%, preferably more than 75%, advantageously more than 80%, in each case based on the wood used. This yield correlates with the lignin content of the pulp stated above.
  • the original lignin content of wood is specific to the species.
  • the yield loss is predominantly a loss of lignin.
  • the proportion of carbohydrates is markedly increased, eg. B. because digestion chemicals in an undesirable manner also bring cellulose or hemicelluloses in solution.
  • a further, advantageous measure is to remove after defibering and optionally grinding the lignocellulosic material, the remaining chemical solution and feed it to a further use.
  • this reuse can include two aspects. On the one hand, the decomposed during the partial digestion or dissolved in organic material, mainly lignin, continue to be used. It is burned, for example, to gain process energy. Or it is prepared to be used elsewhere. On the other hand, the used and unused chemicals are reprocessed so that they can be used for a renewed, partial digestion of lignocellulosic material. This includes the treatment of used chemicals.
  • the chemical solution used is used extremely efficiently. After defibering and optionally grinding, the pulp is washed to displace the chemical solution as much as possible through water.
  • the filtrate produced in this washing or displacement process contains considerable amounts of chemical solution and organic material.
  • this filtrate is supplied to the removed or separated chemical solution before the chemical solution is fortified and fed to the next digestion.
  • the chemicals and organic components contained in the filtrate do not disturb the digestion. To the extent that they still contribute to delignification during the next digestion, their content is recorded in the chemical solution and taken into account in determining the amount of chemicals required for this digestion.
  • the chemicals further contained in the filtrate behave inert during the pending digestion. They do not bother.
  • the organic constituents contained in the filtrate are also inert. They will continue to be used in the processing of the chemical solution after the next digestion, either to generate process energy or otherwise.
  • the yield was calculated by weighing the raw material used and the pulp obtained after the pulping, in each case dried at 105 ° C. to constant weight (atro).
  • the lignin content was determined as Klason lignin according to TAPPT T 222 om-98.
  • the acid-soluble lignin was determined according to TAPPI UM 250
  • the freeness was measured according to Zellcheming leaflet V / 3/62. - The density was determined according to Zellcheming regulation V / 11/57.
  • the breaking length was determined according to Zellcheming regulation V / 12/57.
  • the tear resistance was determined according to DIN 53 128 Elmendorf.
  • Tensile, Tear and Burst Index was carried out according to TAPPI 220 sp. 96.
  • the whiteness was determined by preparing the test sheets according to Zellcheming leaflet V / 19/63, measured according to SCAN C 11:75 with a Datacolor elrepho 450 x photometer; the whiteness is given in percent according to ISO standard 2470.
  • the viscosity was determined according to the leaflet IV / 36/61 of the Association of Pulp and Paper Chemists and Engineers (Zellcheming).
  • Example 1 Softwood pulping in the liquid phase
  • a mixture of spruce wood and Douglas fir wood chips was after a damping (30 minutes in saturated steam at 105 0 C) with a sodium sulfite pulping solution at a liquor ratio of wood: digestion solution 1: 3 added.
  • the total use of chemicals was less than 15% based on otro woodchips.
  • the pH at the beginning of the digestion was adjusted to pH 6 by addition of SO 2 .
  • the impregnated with chemical solution spruce wood chips were heated over a period of 90 minutes at 170 0 C and digested for 60 minutes at this maximum temperature.
  • the open-ended wood chips were shredded. Aliquots of the pulp so produced were ground for different lengths to determine the strength at different degrees of grinding. The energy required to shred the partially digested chips was less than 300 kWh / t of pulp.
  • the yield in this experiment was 77% based on the wood pulp used. This corresponds to a pulp with a lignin content of well over 20%.
  • the average lignin content for spruce wood is given as 28% in relation to the otro wood mass (Wagensuppl, Anatomie des Holzes, VEB frabuchverlag für, 1980).
  • the actual lignin content of the pulp is higher than 20%, because during digestion mainly but not exclusively lignin is broken down.
  • Carbohydrates cellulose and hemicelluloses
  • the values given show that the digestion has a good selectivity with regard to lignin and carbohydrate degradation.
  • the whiteness is unexpectedly high with values of over 55% ISO and thus provides a good starting point for a possible subsequent bleaching, in the whiteness of 75% ISO can be achieved.
  • a grinding time of 20 to 30 minutes is required. Up to a grinding time of 20 minutes (freeness SR 12 0 - 15 0 SR), the freeness developed independently of the pH value at the start of the digestion (pH 6 to pH 9.4) in a narrow corridor.
  • the pulp was made from spruce wood chips with the pH at the beginning of the digestion being 9.4.
  • the chemical solution 0.1 anthraquinone was added based on the amount of wood used.
  • the duration of the digestion was 60 minutes. The following values resulted:
  • the duration of digestion can be reduced from approx. 180 minutes to 60 minutes under otherwise unchanged digestion conditions. This time saving is valuable, above all because the plants for producing pulp can be made smaller. Further savings potential lies in the fact that the temperature required for digestion only needs to be maintained for a much shorter period of time.
  • Eucalyptus chips were added after attenuation with a sodium sulfite digestion solution at a liquor ratio of wood digestion solution 1: 3.
  • the use of chemicals here was 10.5% (as NaOH) on otro woodchips.
  • the fibers produced in the vapor phase have excellent strengths.
  • the tenacity was measured, for example, at 10 km and at 11 km at 15 "SR
  • the tearing resistance was measured, for example, at 82.8 cN and at 91.0 cN
  • These values correspond to the best values for high lignin content pulps for pulps in For pulps with a high lignin content from the prior art comparable strength values are not known. It can be seen particularly clearly from the examples that the fibrous materials according to the invention require only a small amount of energy during grinding in order to build up high breaking lengths without reducing the tear propagation resistance. Grinding 12 0 SR was achieved in 0-10 minutes; Grinding degree 13 0 SR 5-30 minutes, usually 10-20 minutes.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Paper (AREA)

Abstract

L'invention concerne un procédé de préparation de matière fibreuse avec une teneur en lignine d'au moins 15 % pour le bois de conifère, d'au moins 12 % pour le bois de feuillus ou d'au moins 10 % pour les plantes annuelles, sur la base de la masse de fibre séchée à l'étuve. Ledit procédé consiste à préparer une solution de produits chimiques avec plus de 5 % de produits chimiques (sous forme de NaOH) pour le bois de conifère ou avec plus de 3,5 % de produits chimiques (sous forme de NaOH) pour le bois de feuillus ou plus de 2,5 % pour les plantes annuelles, sur la base de la quantité de bois séché à l'étuve, à mélanger la solution de produits chimiques avec le bois ou les plantes annuelles selon un rapport de bain prédéterminé, à chauffer la solution de produits chimiques et le bois ou les plantes annuelles à une température supérieure à la température ambiante et ensuite, soit (variante 1) à éliminer la solution de produits chimiques s'écoulant librement et à pulper le bois ou les plantes annuelles en phase vapeur, soit (variante 2) à pulper le bois ou les plantes annuelles en phase liquide et à séparer la solution de produits chimiques s'écoulant librement et le bois ou les plantes annuelles.
EP07723953A 2006-06-08 2007-04-04 Procédé de préparation de matière fibreuse Withdrawn EP2029806A2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE200610027006 DE102006027006A1 (de) 2006-06-08 2006-06-08 Verfahren zum Herstellen von Faserstoff aus Holz
DE200610061480 DE102006061480A1 (de) 2006-12-23 2006-12-23 Verfahren zum Herstellen von Faserstoff
PCT/EP2007/003012 WO2007140837A2 (fr) 2006-06-08 2007-04-04 Procédé de préparation de matière fibreuse

Publications (1)

Publication Number Publication Date
EP2029806A2 true EP2029806A2 (fr) 2009-03-04

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Application Number Title Priority Date Filing Date
EP07723953A Withdrawn EP2029806A2 (fr) 2006-06-08 2007-04-04 Procédé de préparation de matière fibreuse

Country Status (6)

Country Link
US (1) US20090314443A1 (fr)
EP (1) EP2029806A2 (fr)
JP (1) JP2009540132A (fr)
BR (1) BRPI0712857A2 (fr)
CA (1) CA2634378A1 (fr)
WO (1) WO2007140837A2 (fr)

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DE102007022750A1 (de) * 2007-05-11 2008-11-13 Voith Patent Gmbh Verfahren zum Zerfasern von chemisch behandeltem lignocellulosischem Rohstoff
DE102007036376A1 (de) * 2007-07-31 2009-02-05 Voith Patent Gmbh Gebleichter Faserstoff
DE102007036382A1 (de) * 2007-07-31 2009-02-05 Voith Patent Gmbh Lignocellulosischer Faserstoff aus Einjahrespflanzen
CN101748633B (zh) * 2008-12-19 2012-07-04 北京英力生科新材料技术有限公司 纤维素提取新工艺
US20110060077A1 (en) * 2009-09-10 2011-03-10 Yeng-Fong Shih Process for Manufacturing High-Performance Natural Fiber Reinforced Composites
WO2013082735A1 (fr) * 2011-12-07 2013-06-13 北京英力生科新材料技术有限公司 Procédé mécano-chimique de fabrication de pâte à papier
CN102677504B (zh) * 2012-05-29 2014-02-26 宜宾丝丽雅集团有限公司 一种高湿模量纤维用抗菌性竹浆粕的制造工艺

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GB885605A (en) * 1958-09-11 1961-12-28 Stora Kopparbergs Bergslags Ab Improved method for the production of neutral sulfite pulp
JPH0931880A (ja) * 1995-07-17 1997-02-04 Mitsubishi Paper Mills Ltd 化学パルプの漂白法及び改質法
GB2382592A (en) * 2001-11-30 2003-06-04 Sca Hygiene Prod Gmbh Use of ozone to enhance the wet strength of fibrous cellulosic material
CN1177101C (zh) * 2002-07-05 2004-11-24 岳阳纸业股份有限公司 机械磨石磨木浆渣浆化学处理热磨浆工艺
CN1208519C (zh) * 2003-01-15 2005-06-29 岳阳纸业股份有限公司 表面施胶新闻纸及其制造方法
DE102005036075A1 (de) * 2005-08-01 2007-02-15 Voith Patent Gmbh Verfahren zur Herstellung von Tissuepapier
KR100694840B1 (ko) * 2005-06-09 2007-03-14 유해일 옥수숫대 셀룰로오스로부터의 기계펄프의 제조방법

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Also Published As

Publication number Publication date
US20090314443A1 (en) 2009-12-24
JP2009540132A (ja) 2009-11-19
WO2007140837A2 (fr) 2007-12-13
CA2634378A1 (fr) 2007-12-13
BRPI0712857A2 (pt) 2012-07-31
WO2007140837A3 (fr) 2008-04-03

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