EP0501059A1 - Procédé de lessivage par explosion à la vapeur pour faire du papier - Google Patents

Procédé de lessivage par explosion à la vapeur pour faire du papier Download PDF

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Publication number
EP0501059A1
EP0501059A1 EP91306166A EP91306166A EP0501059A1 EP 0501059 A1 EP0501059 A1 EP 0501059A1 EP 91306166 A EP91306166 A EP 91306166A EP 91306166 A EP91306166 A EP 91306166A EP 0501059 A1 EP0501059 A1 EP 0501059A1
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EP
European Patent Office
Prior art keywords
cooking
process according
chips
steam
impregnation
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EP91306166A
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German (de)
English (en)
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EP0501059B1 (fr
Inventor
Bohuslav Vaclav Kokta
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    • 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
    • D21C1/00—Pretreatment of the finely-divided materials before digesting
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
    • D21B1/00—Fibrous raw materials or their mechanical treatment
    • D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
    • D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
    • D21B1/30—Defibrating by other means
    • D21B1/36—Explosive disintegration by sudden pressure reduction

Definitions

  • This invention relates to a steam explosion pulping process for papermaking.
  • CTMP/CMP ultra-high-yield chemithermomechanical or chemimechanical pulping
  • the steam explosion pulping process consists of the chemical impregnation of chips, short duration saturated steam cooking at temperatures varying from 180°C to 210°C, pressure release, refining and bleaching (if necessary).
  • the object of this invention is to provide a process in which additional yield saving and brightness level increase and cost decrease are obtained when compared to the previous invention of Kokta, CA-A-1 230 208 by substituting sodium hydroxide with milder swelling agents like: sodium carbonate, sodium bicarbonate, magnesium carbonate, magnesium chloride, etc.
  • the major problems accompanying previous processes using explosive decompression are believed to have been degradation due to the oxidation of wood and acid hydrolysis leading to loss in brightness, deterioration of fiber and paper properties and loss of yield.
  • the approach adopted by this invention is thereto to attempt to curtail hydrolytic and oxidative wood degradation and thereby to protect against loss of yield, brightness and fiber strength.
  • the loss of fiber strength will be particularly great if the degree of polymerisation of the cellulose falls below the critical value which is about 500-600. Hydrolytic degradation will also cause yield lowss due mainly to degradation of hemi-cellulose.
  • the process of this invention tries to achieve a positive improvement in the strength of the paper that will be produced from the fibers by increasing the number of hydrophilic groups on the fiber surfaces thereby adding to the potential sites for hydrogen bonding.
  • the starting material will normally be chips in which the fibers are of a length suitable for paper making. Shavings could also be used but sawdust would be undesirable except as a minor part of the total furnish as the fibers are partially cut.
  • the chips should also, as is well known, be suitable in the sense of being free from bark and foreign matter.
  • impregnation is to protect the chips against oxidation during cooking and during transfer from the cooking vessel to the refiner. It is also an objective to provide a positive increase in strength by developing hydrophylic groups on the fiber surface during steam treatment. This will then provide additional sites for hydrogen bonding.
  • the preferred antioxidant is sodium sulphite Na2SO3 which also forms hydrophilic groups, and which is available at a low cost. It is used to provide a concentration of absorbed chemical of about 1 to 16% by weight. Concentrations below 4% would be used where brightness protection is unimportant and high strength is not required. Where, however, brightness is important the sodium sulphite should be at least 4%. If physical properties are important these will be improved by using a concentration of at least 4% sodium sulphite and will be further improved as the concentration is further increased towards 16%.
  • the concentration of the solution is preferably about the same as the percentage of chemical to be absorbed where there are equal quantities of chips and liquor.
  • a ton of chips of 50% consistency mixed with one ton of 8% solution will result in about 8% absorbed on the pulp.
  • Thorough impregnation is important so as to distribute the antioxidant evenly rather than depositing it just on the surface.
  • Other antioxidants that can be used are potassium sulphite or magnesium sulphite.
  • Ammonium sulphite could be used if cooking conditions are not severe, or with a buffer.
  • Complexing agents such as ethylene diamine tetracetic acid (EDTA), sodium diethylene triaminepentacetate (DTPA), sodium tripolyphosphate (TPF) and other complexing agents known in the art as being usable under alkaline conditions may be added to minimize the catalytic effect of metals such as iron on oxidative degradation.
  • a swelling agent to assist the antioxidant or hydrophilic agent in penetrating the wood and this contributes also to softening the chip.
  • Suitable swelling agents are ammonium hydroxide or sodium carbonate or sodium bicarbonate or magnesium carbonate or magnesium sulphate any of which will contribute also to providing hydrophilic groups.
  • Other swelling agents that can be used and which may be desirable as auxiliary swelling agents for high density wood are zinc chloride, sodium chloride, sodium bromide, magnesium chloride, calcium isocyanate, Schweitzers solution, cupriethylenediamne (C.E.D.) tetraethylammonium hydroxide or dimethyldibenzylammonium hydroxide.
  • the concentration of swelling agent and conditions of swelling must be controlled in such a way as to avoid any dissolution of the hollocellulose.
  • the percentage of swelling agent in the impregnating solution will be in the range of about 1 to 4% depending on the agent and the conditions.
  • the impregnating solution must be alkaline and have enough free hydroxyl to be able to neutralize the liberated wood acids such as formic acid and acetic acid. Normally the starting pH is about 7.5 or higher and the final pH after steam cooking should be at least 6 or higher.
  • the time of impregnation at atmospheric pressure in holding tanks typically ranges from about 12 hours to 24 hours at a temperature of about 30°C to 60°C. Approximately equal weights of chips and of aqueous impregnating solution can be used. For industrial purposes, however, the time may be shortened to an hour or to minutes by impregnating with steam under pressure and at a higher temperature.
  • the pressure should be up to about 1 atmospheric extra pressure at a temperature of about 100°C to 110°C.
  • the chips should be compressed in advance of impregnation in cool solutions of chemicals. Under these conditions, penetration will be achieved in a shorter time. Penetration is what predominantly occurs; there is no significant cooking as evidenced by the fact that there is no significant sulphonic and carboxylic group increase.
  • the impregnated chips are steam cooked at a high temperature and pressure.
  • the temperature of cooking should be within the range of about 180°C to 210°C and preferably within the range 190-200°C, which is in excess of the temperatures considered possible according to the publications of Asplund and Higgins previously referred to. These temperatures correspond with a pressure of 10 atmospheres for 180°C and 15.5 atmospheres for 200°C. It is these high pressures and temperatures which make a very important contribution to ensuring excellent penetration of the chips by the cooking liquor and results in higher efficience of ionic groups formation on fiber surface.
  • the cooking may be preceded by steam flushing under low pressure steam at 100°C for a short period such as one minute.
  • steam flushing under low pressure steam at 100°C for a short period such as one minute.
  • This preliminary treatment is then followed by cooking for about 30 seconds to 6 minutes and preferably about 1 to 4 minutes.
  • the chips resulting from the explosive decompression are softened and partially defibrated.
  • Refining energies are usually low and can be expected to be in the range of 1.7 to 4 MJ/kg, hardwoods, CSF ⁇ 100 ml, which is considerably lower than that of conventional CMP and similar to that described in Kokta, CA-A-1 230 208 and US-A-4 798 651.
  • Time of impregnation 24 hours; temperature of impregnation: 60°C.
  • Liquid/chip ratio during impregnation was equal to 3.
  • Explosion pulps were prepared using vapor phase team cooking of chemically pretreated aspen wood chips at a cooking temperature of 190°C and cooking time 4 minutes.
  • Cooking took place using saturated steam in a laboratory batch reactor built by Stake Tech. Co. Cooking was preceded by one minute steam flushing at atmospheric pressure. After cooking, the pressure was instantaneously released and chips which exploded into the release vessel were washed and cooled down with one liter of tap water, and subsequently refined after being stored in a cold room. The reported amount of steam used for cooking varied from 0.5 to 1 kg of steam for 1 kg of chips. Yield was measured as follows: exploded chips (75 g) were washed with one liter of tap water and subsequently defibrated for 90 seconds in a laboratory blender at 2% consistency. The pulp was washed again with one liter of water, dried at 105°C to constant weight and the resulted weights were compared to the initial O.D. weight of chips.
  • Paper sheets were prepared and tested according to standard CPPA testing methods on 1.2 g sheets. Brightness (Elrepho) was evaluated on sheets made with deinosized water. Ionic content (sulfonate and carboxylate ions) was determined by means of conductometric titration.
  • the present invention consisting in substituting NaOH by agents such as carbonates or bicarbonates results not only in the yield and brightness advantage but also in cost decrease.

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Mechanical Engineering (AREA)
  • Paper (AREA)
EP91306166A 1991-02-28 1991-07-08 Procédé de lessivage par explosion à la vapeur pour faire du papier Expired - Lifetime EP0501059B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CA2037275 1991-02-28
CA 2037275 CA2037275A1 (fr) 1991-02-28 1991-02-28 Procede de fabrication de pate a papier par cuisson a la vapeur suivie de detente explosive de celle-ci

Publications (2)

Publication Number Publication Date
EP0501059A1 true EP0501059A1 (fr) 1992-09-02
EP0501059B1 EP0501059B1 (fr) 1995-11-29

Family

ID=4147084

Family Applications (1)

Application Number Title Priority Date Filing Date
EP91306166A Expired - Lifetime EP0501059B1 (fr) 1991-02-28 1991-07-08 Procédé de lessivage par explosion à la vapeur pour faire du papier

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EP (1) EP0501059B1 (fr)
CA (1) CA2037275A1 (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000019004A1 (fr) * 1998-09-25 2000-04-06 Stake Technology Ltd. Traitement de vapocraquage semi-alcalin de materiau fibreux pour la production de pate a papier
US6413362B1 (en) 1999-11-24 2002-07-02 Kimberly-Clark Worldwide, Inc. Method of steam treating low yield papermaking fibers to produce a permanent curl
US6506282B2 (en) 1998-12-30 2003-01-14 Kimberly-Clark Worldwide, Inc. Steam explosion treatment with addition of chemicals
CN103362008A (zh) * 2012-04-01 2013-10-23 中国科学院过程工程研究所 一种以碱木质素为胶粘剂的汽爆秸秆生态板制备方法
FR3026655A1 (fr) * 2014-10-01 2016-04-08 Commissariat Energie Atomique Dispositif de reduction de la taille de particules de biomasse a fonctionnement continu

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2638150C (fr) 2008-07-24 2012-03-27 Sunopta Bioprocess Inc. Methode et appareil permettant le transport d'une charge d'alimentation cellulosique
CA2638160C (fr) 2008-07-24 2015-02-17 Sunopta Bioprocess Inc. Methode et appareil permettant le transport d'une charge d'alimentation cellulosique
CA2638152C (fr) 2008-07-24 2013-07-16 Sunopta Bioprocess Inc. Methode et appareil permettant le traitement d'une charge d'alimentation cellulosique
CA2638159C (fr) 2008-07-24 2012-09-11 Sunopta Bioprocess Inc. Methode et appareil permettant le traitement d'une charge d'alimentation cellulosique
CA2650919C (fr) 2009-01-23 2014-04-22 Sunopta Bioprocess Inc. Methode et installation de transport de produit de depart cellulosique
US9127325B2 (en) 2008-07-24 2015-09-08 Abengoa Bioenergy New Technologies, Llc. Method and apparatus for treating a cellulosic feedstock
US8915644B2 (en) 2008-07-24 2014-12-23 Abengoa Bioenergy New Technologies, Llc. Method and apparatus for conveying a cellulosic feedstock
CA2650913C (fr) 2009-01-23 2013-10-15 Sunopta Bioprocess Inc. Methode et appareillage de transport de produits de depart cellulosiques
CA2638157C (fr) 2008-07-24 2013-05-28 Sunopta Bioprocess Inc. Methode et appareil permettant le transport d'une charge d'alimentation cellulosique
PL2467532T3 (pl) 2009-08-24 2014-11-28 Abengoa Bioenergy New Tech Llc Sposób wytwarzania etanolu i współproduktów z biomasy celulozowej
CN104404803B (zh) * 2014-08-29 2016-08-17 济南米铎碳新能源科技有限公司 秸秆组分分离及秸秆组分全利用的方法
CN106522004B (zh) * 2016-11-10 2018-10-23 北京化工大学 一种纤维素与半纤维素联合预处理装置

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0172135A1 (fr) * 1984-07-17 1986-02-19 Rudy Vit Méthode, procédé et appareil pour la conversion du bois, des résidus de bois, des fibres végétales et de la biomasse en pâte
EP0284585A2 (fr) * 1987-03-24 1988-09-28 Stake Technology Ltd. Procédé de fabrication de pâte papetière

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE455314B (sv) * 1985-09-03 1988-07-04 Punya B Chaudhuri Framstellning av cellulosamassa innefattande kemisk forbehandling och defibrering genom expansion
EP0487793B1 (fr) * 1990-11-26 1995-08-30 Bohuslav Vaclav Kokta Procédé d'explosion pour la préparation de pâte à papier

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0172135A1 (fr) * 1984-07-17 1986-02-19 Rudy Vit Méthode, procédé et appareil pour la conversion du bois, des résidus de bois, des fibres végétales et de la biomasse en pâte
EP0284585A2 (fr) * 1987-03-24 1988-09-28 Stake Technology Ltd. Procédé de fabrication de pâte papetière

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000019004A1 (fr) * 1998-09-25 2000-04-06 Stake Technology Ltd. Traitement de vapocraquage semi-alcalin de materiau fibreux pour la production de pate a papier
US6506282B2 (en) 1998-12-30 2003-01-14 Kimberly-Clark Worldwide, Inc. Steam explosion treatment with addition of chemicals
US6413362B1 (en) 1999-11-24 2002-07-02 Kimberly-Clark Worldwide, Inc. Method of steam treating low yield papermaking fibers to produce a permanent curl
CN103362008A (zh) * 2012-04-01 2013-10-23 中国科学院过程工程研究所 一种以碱木质素为胶粘剂的汽爆秸秆生态板制备方法
FR3026655A1 (fr) * 2014-10-01 2016-04-08 Commissariat Energie Atomique Dispositif de reduction de la taille de particules de biomasse a fonctionnement continu

Also Published As

Publication number Publication date
CA2037275A1 (fr) 1992-08-29
EP0501059B1 (fr) 1995-11-29

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