EP0019963B1 - Process for the delignification and bleaching of chemical and semichemical cellulose pulps - Google Patents
Process for the delignification and bleaching of chemical and semichemical cellulose pulps Download PDFInfo
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- EP0019963B1 EP0019963B1 EP80200450A EP80200450A EP0019963B1 EP 0019963 B1 EP0019963 B1 EP 0019963B1 EP 80200450 A EP80200450 A EP 80200450A EP 80200450 A EP80200450 A EP 80200450A EP 0019963 B1 EP0019963 B1 EP 0019963B1
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- treatment
- peroxide
- process according
- oxygen
- pulp
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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
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/10—Bleaching ; Apparatus therefor
- D21C9/1057—Multistage, with compounds cited in more than one sub-group D21C9/10, D21C9/12, D21C9/16
Definitions
- the present invention relates to a sequential process for the delignification and bleaching of chemical and semi-chemical cellulosic pulps by the action of oxygen, further comprising a subsequent bleaching treatment with peroxide.
- the bleaching of chemical and semi-chemical cellulose pulps intended in particular for the manufacture of paper generally requires several successive bleaching treatments, possibly interspersed with washing, dilution and / or concentration steps, in order to reach the level of residual lignin and to the desired whiteness.
- the object of the invention is to provide a process which makes it possible to overcome the drawbacks of the known processes cited above and in particular to avoid excessive depolymerization of the cellulose in chemical and semi-chemical pastes.
- the method according to the invention also makes it possible to produce paper pulps with good yields.
- the pasta obtained also has a good degree of whiteness.
- the invention relates to a process for the delignification and bleaching of chemical and semi-chemical cellulosic pulps comprising an oxygen treatment in an alkaline medium and a subsequent treatment using peroxides according to which the effluents from the peroxide treatment are at least partially recycled for oxygen treatment.
- stage O only part of the effluents from the peroxide treatment, preferably not exceeding 80% of their weight, is recycled to the oxygen treatment. Good results have been obtained by recycling to the oxygen treatment from 5 to 70% of the weight of the effluents from the peroxide treatment (also called stage P below).
- the oxygen treatment is generally carried out using an oxygen-containing gas such as oxygen or air. Other mixtures of oxygen-containing gases can also be used.
- the partial pressures of oxygen can vary within wide limits. They are generally between 100 kPa and 2 MPa.
- the temperatures are generally between 353 and 423 K and preferably between 373 and 503 K.
- the oxygen treatment is carried out in the presence of an alkaline aqueous solution.
- alkalis can be used for this purpose. In general, they are chosen from hydroxides, bicarbonates and carbonates of alkali metals and ammonium and their mixtures. Good results are obtained by using an alkali containing sodium hydroxide.
- the amount of alkali used can vary within wide limits. It is generally between 0.1 and 20%, and preferably between 1 and 15% of the weight of dry pulp.
- the density of the paste used in stage 0 is generally between 3 and 50% and preferably between 5 and 40%.
- additives can be used in stage 0, without this being essential, such as cellulose protecting agents, sequestering agents, pH regulators, etc.
- the total content of various additives generally does not exceed 10% of the weight of the dry paste.
- the protective agents are generally chosen from derivatives of alkaline earth metals. These derivatives are most often alkaline earth metal salts and more particularly magnesium salts. It is thus possible to use during the oxygen treatment of carbonate, sulphate, oxide or magnesium hydroxide.
- the oxygen treatment can be carried out in any device known per se suitable for delignification and capable of withstanding the pressures used. Various types of autoclaves can thus be used.
- the dough After the oxygen treatment, the dough is degassed. It can be sent as is to subsequent whitening treatment.
- the dough can also be subjected to one or more washing or dilution, and possibly concentration, stages before sending it to the subsequent bleaching treatment.
- These various steps can be carried out in various types of apparatus known in themselves.
- the concentrations can thus be carried out in various types of apparatus allowing the extraction of the dough such as rotary filters or various types of press.
- Any effluents from these washing, dilution and concentration stages subsequent to stage 0 can be recycled to stage 0 and / or subjected to incineration so as to regenerate the alkali. In general, at least 10% of the weight of these effluents is sent to recovery boilers for incineration.
- the pulp obtained can then optionally undergo intermediate bleaching treatments before being sent to the peroxide treatment. It is thus possible to subject the paste obtained from stage O, optionally after the washing, dilution or concentration steps mentioned above, to at least one intermediate treatment chosen from treatments with carboxylic peracids and ozone. However, such intermediate bleaching treatments are not essential. Good results have been obtained by sending the pulp from the oxygen treatment to the peroxide treatment, without any intermediate bleaching treatment.
- the peroxide treatment is carried out in the presence of peroxidized compounds of various types. It is thus possible to use hydrogen peroxide, alkali metal peroxides, other inorganic peroxides, and organic peroxides, hydro-peroxides or peracids. In general, a peroxide compound chosen from hydrogen peroxide, sodium peroxide and their mixture is used. Good results are obtained using hydrogen peroxide.
- the amount of peroxide compounds used calculated as pure hydrogen peroxide is generally between 0.1 and 10% and preferably between 0.2 and 5% of the weight of dry pulp.
- the mixture subjected to stage P is maintained at a basic pH, generally between 9 and 13 and more often between 10 and 12.5.
- alkalis are added to the mixture, which can be of very diverse natures.
- hydroxides or carbonates of alkali metals, alkaline earth metals or ammonium, and more particularly sodium hydroxide are added to the mixture.
- the amount of alkali used depends on the type of peroxide compound used and more particularly on its possible alkaline character.
- the peroxidized compound is hydrogen peroxide, generally 0.2 to 15% by weight of alkali is added relative to the weight of dry pulp. Good results are obtained using 0.5 to 10% alkali. These amounts are reduced when the peroxidized compound contains sodium peroxide.
- the densities of the pastes subjected to the peroxide treatment are generally between 2 and 25%.
- the temperatures are generally between room temperature and the boiling temperature of the mixture. Good results are obtained at temperatures between 333 and 353 K.
- additives can be used in stage O, without this being essential, such as organic or inorganic stabilizers, surfactants, complexing agents, pH regulating agents, etc.
- magnesium salts such as magnesium sulfate and silicates such as water glass are used.
- agents generally chosen from organic compounds containing nitrogen and / or phosphorus such as nitrilotriacetic, ethylene-diamine-tetraacetic, diethylenetriamine-pentaacetic acids and their salts, polyhyroxycarboxylic acids and their salts such as sodium poly-hydroxyacrylate and hydroxycarboxylic acids and their salts such as sodium gluconate.
- the peroxide treatment can take place in various types of apparatus known per se, such as towers or batteries.
- the paste resulting from the peroxide treatment is then subjected to one or more concentration stages, possibly after one or more prior dilutions.
- Concentration can be done according to various techniques known in themselves such as spinning in a rotary filter or in various types of press. This concentration brings the dough to a density generally greater than 10%.
- the effluents from the concentration stages following the peroxide treatment are recycled at least in part to stage 0 according to the invention. They can be returned directly to the device where the oxygen treatment is carried out, or even mixed with stage O effluents intended to be recycled there.
- stage P The part of the effluents of stage P which is not recycled in stage 0 is advantageously recycled in stage P or also used to dilute the pulp resulting from stage P before its concentration.
- a particularly suitable method consists in diluting the paste resulting from the peroxide treatment, in concentrating it on one or more apparatuses suitable for wringing, in collecting the effluents from these wrings which constitute the effluents of the method according to the invention, in using 30 to 95% of these effluents for the step of diluting the pulp resulting from the peroxide treatment and recycling the balance of these effluents to the oxygen treatment.
- the devices used for wringing the dough from the peroxide treatment can also be supplied with a small amount of fresh water or an aqueous solution.
- the quantity of water or aqueous solution used is substantially equal to the quantity of effluents from the oxygen treatment sent to the recovery boilers.
- Stage P of the process according to the invention can, depending on the desired degree of whiteness, be subjected to one or more additional bleaching treatments. These are generally chosen from treatments with peroxide, chlorine dioxide (also called stages D), hypochlorite (also called stages H), carboxylic peracids (also called stage P / J and chlorine (called also stages C) or alkaline extractions (also called stage E) Certain specific sequences of subsequent treatments have given good results: these are the CED, CEH, CHH, CPD, CPH, DED, DHD and DPD sequences.
- Example 2 was carried out by way of comparison in the absence of recycling.
- Example 1 Bleaching of a pine kraft pulp
- a pine kraft paste (initial whiteness 27.6 ° ISO, kappa index 39.6) was subjected to a treatment in five stages comprising a first oxygen treatment and a second peroxide treatment with recycling of the effluent from the peroxide stage to the oxygen stage.
- the operating conditions are given below.
- the percentages of the reactants are given relative to the dry paste.
- the final viscosity of the paste from the last step measured according to the TAPPI T 230 standard is 12.0 mPa.s.
- Example 2 Whitening of a pine kraft pulp
- test 1 The same pine kraft pulp as that used for carrying out test 1 was subjected to a treatment in five stages comprising a first treatment with oxygen and a second treatment with peroxide without recycling of the effluent from stage with peroxide in the oxygen step.
- the other operating conditions are identical to those of test 1.
- the final viscosity of the paste at the end of the last step is 10.8 mPa.s.
- the cellulose pulp therefore underwent a greater depolymerization than when the method according to the invention was used.
Abstract
Description
La présente invention concerne un procédé séquentiel pour la délignification et le blanchiment de pâtes cellulosiques chimiques et semi-chimiques par action de l'oxygène comportant en outre un traitement ultérieur de blanchiment au peroxyde.The present invention relates to a sequential process for the delignification and bleaching of chemical and semi-chemical cellulosic pulps by the action of oxygen, further comprising a subsequent bleaching treatment with peroxide.
Le blanchiment des pâtes chimiques et semi-chimiques de cellulose destinées notamment à la fabrication du papier nécessite généralement plusieurs traitements de blanchiment successifs, éventuellement entrecoupés d'étapes de lavage, de dilution et/ou de concentration, pour parvenir au taux de lignine résiduelle et à la blancheur désirés.The bleaching of chemical and semi-chemical cellulose pulps intended in particular for the manufacture of paper generally requires several successive bleaching treatments, possibly interspersed with washing, dilution and / or concentration steps, in order to reach the level of residual lignin and to the desired whiteness.
Divers types d'agents de blanchiment sont couramment utilisés pour le traitement de pâtes cellulosiques. On a ainsi proposé de soumettre les pâtes chimiques et semi-chimiques à l'action de l'oxygène ou de l'air en milieu alcalin, et ensuite à des traitements de blanchiment comportant un traitement au peroxyde. Cependant l'élimination de la lignine et le gain de blancheur s'accompagnent de modifications importantes des caractéristiques physiques des pâtes cellulosiques et plus particulièrement d'une réduction sensible de la viscosité des pâtes ce qui traduit une dépolymérisation des chaînes cellulosiques. Au niveau industriel le rendement des procédés est réduit. En outre, la résistance des produits finis est amoindrie.Various types of bleaching agents are commonly used for the treatment of cellulosic pulps. It has thus been proposed to subject the chemical and semi-chemical pastes to the action of oxygen or air in an alkaline medium, and then to bleaching treatments comprising a peroxide treatment. However, the elimination of lignin and the gain in whiteness are accompanied by significant changes in the physical characteristics of the cellulose pastes and more particularly by a significant reduction in the viscosity of the pastes, which translates into depolymerization of the cellulosic chains. At the industrial level the yield of the processes is reduced. In addition, the resistance of the finished products is reduced.
L'invention a pour but de fournir un procédé qui permet de pallier les inconvénients des procédés connus cités ci-dessus et notamment d'éviter une dépolymérisation trop importante de la cellulose dans les pâtes chimiques et semi-chimiques. Le procédé selon l'invention permet en outre de produire les pâtes à papier avec de bons rendements. Les pâtes obtenues ont par ailleurs un bon degré de blancheur.The object of the invention is to provide a process which makes it possible to overcome the drawbacks of the known processes cited above and in particular to avoid excessive depolymerization of the cellulose in chemical and semi-chemical pastes. The method according to the invention also makes it possible to produce paper pulps with good yields. The pasta obtained also has a good degree of whiteness.
L'invention concerne à cet effet un procédé pour la délignification et le blanchiment de pâtes cellulosiques chimiques et semi-chimiques comportant un traitement à l'oxygène en milieu alcalin et un traitement ultérieur au moyen de peroxydes selon lequel les effluents du traitement au peroxyde sont recyclés au moins partiellement au traitement à l'oxygène.To this end, the invention relates to a process for the delignification and bleaching of chemical and semi-chemical cellulosic pulps comprising an oxygen treatment in an alkaline medium and a subsequent treatment using peroxides according to which the effluents from the peroxide treatment are at least partially recycled for oxygen treatment.
En général, une partie seulement des effluents du traitement au peroxyde, ne dépassant pas de préférence 80% de leur poids, est recyclée au traitement à l'oxygène (appelé également ci-après stade O). De bons résultats ont été obtenus, en recyclant au traitement à l'oxygène de 5 à 70 % du poids des effluents du traitement au peroxyde (appelé également ci-après stade P).In general, only part of the effluents from the peroxide treatment, preferably not exceeding 80% of their weight, is recycled to the oxygen treatment (hereinafter also called stage O). Good results have been obtained by recycling to the oxygen treatment from 5 to 70% of the weight of the effluents from the peroxide treatment (also called stage P below).
Le traitement à l'oxygène est en général réalisé à l'aide d'un gaz contenant de l'oxygène tel que t'oxygène ou l'air. D'autres mélanges de gaz contenant de l'oxygène peuvent également être utilisés. Les pressions partielles d'oxygène peuvent varier dans de larges limites. Elles sont en général comprises entre 100 kPa et 2 MPa. Les températures sont en général comprises entre 353 et 423 K et de préférence entre 373 et 503 K.The oxygen treatment is generally carried out using an oxygen-containing gas such as oxygen or air. Other mixtures of oxygen-containing gases can also be used. The partial pressures of oxygen can vary within wide limits. They are generally between 100 kPa and 2 MPa. The temperatures are generally between 353 and 423 K and preferably between 373 and 503 K.
Le traitement à l'oxygène s'effectue en présence d'une solution aqueuse alcaline. Divers types d'alcalis peuvent être utilisés à cet effet. En général, ils sont choisis parmi les hydroxydes, les bicarbonates et les carbonates de métaux alcalins et d'ammonium et leurs mélanges. De bons résultats sont obtenus en mettant en oeuvre un alcali contenant de l'hydroxyde de sodium. La quantité d'alcali mise en oeuvre peut varier dans de larges limites. Elle est en général comprise entre 0,1 et 20 %, et de préférence entre 1 et 15 % du poids de pâte sèche.The oxygen treatment is carried out in the presence of an alkaline aqueous solution. Various types of alkalis can be used for this purpose. In general, they are chosen from hydroxides, bicarbonates and carbonates of alkali metals and ammonium and their mixtures. Good results are obtained by using an alkali containing sodium hydroxide. The amount of alkali used can vary within wide limits. It is generally between 0.1 and 20%, and preferably between 1 and 15% of the weight of dry pulp.
La densité de la pâte mise en oeuvre au stade 0 est en général comprise entre 3 et 50 % et de préférence entre 5 et 40 %.The density of the paste used in stage 0 is generally between 3 and 50% and preferably between 5 and 40%.
Divers additifs peuvent être mis en oeuvre au stade 0, sans que cela soit indispensable, tels que des agents protecteurs de la cellulose, des agents de séquestration, des régulateurs de pH, etc. La teneur totale en additifs divers ne dépasse en général pas 10 % du poids de la pâte sèche.Various additives can be used in stage 0, without this being essential, such as cellulose protecting agents, sequestering agents, pH regulators, etc. The total content of various additives generally does not exceed 10% of the weight of the dry paste.
Les agents protecteurs sont en général choisis parmi les dérivés des métaux alcalino-terreux. Ces dérivés sont le plus souvent des sels de métaux alcalino-terreux et plus particulièrement des sels de magnésium. On peut ainsi mettre en oeuvre au cours du traitement à l'oxygène du carbonate, du sulfate, de l'oxyde ou de l'hydroxyde de magnésium.The protective agents are generally chosen from derivatives of alkaline earth metals. These derivatives are most often alkaline earth metal salts and more particularly magnesium salts. It is thus possible to use during the oxygen treatment of carbonate, sulphate, oxide or magnesium hydroxide.
Le traitement à l'oxygène peut être réalisé dans tout appareil connu en lui-même convenant pour la délignification et capable de résister aux pressions mises en ceuvre. On peut ainsi utiliser divers types d'autoclaves.The oxygen treatment can be carried out in any device known per se suitable for delignification and capable of withstanding the pressures used. Various types of autoclaves can thus be used.
Après le traitement à l'oxygène, la pâte est dégazée. Elle peut être envoyée telle quelle au traitement de blanchiment subséquent. On peut également soumettre la pâte à une ou plusieurs étapes de lavage ou de dilution, et éventuellement de concentration, avant de l'envoyer au traitement de blanchiment subséquent. Ces diverses étapes peuvent être réalisées dans divers types d'appareils connus en eux-mêmes. Les concentrations peuvent ainsi être réalisées dans divers types d'appareils permettant l'essorage de la pâte tels que des filtres rotatifs ou divers types de presse. Les effluents éventuels de ces étapes de lavage, de dilution et de concentration subséquentes au stade 0 peuvent être recyclés au stade 0 et/ou soumis à une incinération de manière à régénérer l'alcali. En général, au moins 10 % du poids de ces effluents sont envoyés aux chaudières de récupération pour y être incinérés.After the oxygen treatment, the dough is degassed. It can be sent as is to subsequent whitening treatment. The dough can also be subjected to one or more washing or dilution, and possibly concentration, stages before sending it to the subsequent bleaching treatment. These various steps can be carried out in various types of apparatus known in themselves. The concentrations can thus be carried out in various types of apparatus allowing the extraction of the dough such as rotary filters or various types of press. Any effluents from these washing, dilution and concentration stages subsequent to stage 0 can be recycled to stage 0 and / or subjected to incineration so as to regenerate the alkali. In general, at least 10% of the weight of these effluents is sent to recovery boilers for incineration.
La pâte obtenue peut ensuite subir éventuellement des traitements de blanchiment intermédiaires avant d'être envoyée au traitement au peroxyde. On peut ainsi soumettre la pâte issue du stade O, éventuellement après les étapes de lavage, dilution ou concentration précitées, à au moins un traitement intermédiaire choisi parmi les traitements aux peracides carboxyliques et à l'ozone. De tels traitements de blanchiment intermédiaires ne sont cependant pas indispensables. De bons résultats ont été obtenus en envoyant la pâte issue du traitement à l'oxygène, au traitement au peroxyde, sans traitement de blanchiment intermédiaire.The pulp obtained can then optionally undergo intermediate bleaching treatments before being sent to the peroxide treatment. It is thus possible to subject the paste obtained from stage O, optionally after the washing, dilution or concentration steps mentioned above, to at least one intermediate treatment chosen from treatments with carboxylic peracids and ozone. However, such intermediate bleaching treatments are not essential. Good results have been obtained by sending the pulp from the oxygen treatment to the peroxide treatment, without any intermediate bleaching treatment.
Le traitement au peroxyde s'effectue en présence de composés peroxydés de divers types. On peut ainsi utiliser le peroxyde d'hydrogène, les peroxydes de métaux alcalins, les autres peroxydes inorganiques, et les peroxydes, hydro- peroxydes ou peracides organiques. En général, on utilise un composé peroxydé choisi parmi le peroxyde d'hydrogène, le peroxyde de sodium et leur mélange. De bons résultats sont obtenus en utilisant le peroxyde d'hydrogène. La quantité de composés peroxydés mis en oeuvre calculée en peroxyde d'hydrogène pur est en général comprise entre 0,1 et 10 % et de préférence entre 0,2 et 5 % du poids de pâte sèche.The peroxide treatment is carried out in the presence of peroxidized compounds of various types. It is thus possible to use hydrogen peroxide, alkali metal peroxides, other inorganic peroxides, and organic peroxides, hydro-peroxides or peracids. In general, a peroxide compound chosen from hydrogen peroxide, sodium peroxide and their mixture is used. Good results are obtained using hydrogen peroxide. The amount of peroxide compounds used calculated as pure hydrogen peroxide is generally between 0.1 and 10% and preferably between 0.2 and 5% of the weight of dry pulp.
Le mélange soumis au stade P est maintenu à un pH basique, en général compris entre 9 et 13 et le plus souvent entre 10 et 12,5. Pour ce faire, on ajoute au mélange des alcalis qui peuvent être de natures très diverses. En général, on ajoute au mélange des hydroxydes ou des carbonates de métaux alcalins, de métaux alcalino-terreux ou d'ammonium et plus particulièrement de l'hydroxyde de sodium. La quantité d'alcali mise en oeuvre dépend du type de composé peroxydé mis en oeuvre et plus particulièrement de son caractère alcalin éventuel. Lorsque le composé peroxydé est le peroxyde d'hydrogène, on ajoute en général de 0,2 à 15 % en poids d'alcali par rapport au poids de pâte sèche. De bons résultats sont obtenus en utilisant de 0,5 à 10 % d'alcali. Ces quantités sont réduites lorsque le composé peroxydé contient du peroxyde de sodium.The mixture subjected to stage P is maintained at a basic pH, generally between 9 and 13 and more often between 10 and 12.5. To do this, alkalis are added to the mixture, which can be of very diverse natures. In general, hydroxides or carbonates of alkali metals, alkaline earth metals or ammonium, and more particularly sodium hydroxide, are added to the mixture. The amount of alkali used depends on the type of peroxide compound used and more particularly on its possible alkaline character. When the peroxidized compound is hydrogen peroxide, generally 0.2 to 15% by weight of alkali is added relative to the weight of dry pulp. Good results are obtained using 0.5 to 10% alkali. These amounts are reduced when the peroxidized compound contains sodium peroxide.
Les densités des pâtes soumises au traitement au peroxyde sont en général comprises entre 2 et 25 %. Les températures sont en général comprises entre la température ambiante et la température d'ébullition du mélange. De bons résultats sont obtenus à des températures comprises entre 333 et 353 K.The densities of the pastes subjected to the peroxide treatment are generally between 2 and 25%. The temperatures are generally between room temperature and the boiling temperature of the mixture. Good results are obtained at temperatures between 333 and 353 K.
Divers additifs peuvent être mis en oeuvre au stade O, sans que cela soit indispensable, tels que des stabilisants organiques ou inorganiques, des agents tensioactifs, des agents complexants, des agents régulateurs de pH, etc.Various additives can be used in stage O, without this being essential, such as organic or inorganic stabilizers, surfactants, complexing agents, pH regulating agents, etc.
Comme stabilisants, on utilise en général des composés choisis parmi les sels de magnésium tels que le sulfate de magnésium et les silicates tels que le verre soluble.As stabilizers, compounds generally chosen from magnesium salts such as magnesium sulfate and silicates such as water glass are used.
Comme agents complexants, on utilise en général des agents choisis parmi les composés organiques contenant de l'azote et/ou du phosphore tels que les acides nitrilotriacétique, éthylène-diamine-tétraacétique, diéthylènetriamine- pentaacétique et leurs sels, les acides polyhy- droxycarboxyliques et leurs sels tels que le poly- alpha-hydroxyacrylate de sodium et les acides hydroxycarboxyliques et leurs sels tels que le gluconate de sodium.As complexing agents, agents generally chosen from organic compounds containing nitrogen and / or phosphorus such as nitrilotriacetic, ethylene-diamine-tetraacetic, diethylenetriamine-pentaacetic acids and their salts, polyhyroxycarboxylic acids and their salts such as sodium poly-hydroxyacrylate and hydroxycarboxylic acids and their salts such as sodium gluconate.
Le traitement au peroxyde peut avoir lieu dans divers types d'appareils connus en eux-mêmes tels que des tours ou des piles.The peroxide treatment can take place in various types of apparatus known per se, such as towers or batteries.
La pâte issue du traitement au peroxyde est ensuite soumise à une ou plusieurs étapes de concentration, éventuellement après une ou plusieurs dilutions préalables.The paste resulting from the peroxide treatment is then subjected to one or more concentration stages, possibly after one or more prior dilutions.
La concentration peut se faire selon diverses techniques connues en elles-mêmes telles que l'essorage dans un filtre rotatif ou dans divers types de presse. Cette concentration amène la pâte à une densité en général supérieure à 10 %.Concentration can be done according to various techniques known in themselves such as spinning in a rotary filter or in various types of press. This concentration brings the dough to a density generally greater than 10%.
Les effluents issus des étapes de concentration faisant suite au traitement au peroxyde sont recyclés au moins en partie au stade 0 selon l'invention. Ils peuvent être renvoyés directement dans l'appareil où est réalisé le traitement à l'oxygène, ou encore être mélangés aux effluents du stade O destinés à y être recyclés.The effluents from the concentration stages following the peroxide treatment are recycled at least in part to stage 0 according to the invention. They can be returned directly to the device where the oxygen treatment is carried out, or even mixed with stage O effluents intended to be recycled there.
La partie des effluents du stade P qui n'est pas recyclée au stade 0 est avantageusement recyclée au stade P ou encore utilisée pour diluer la pâte issue du stade P avant sa concentration.The part of the effluents of stage P which is not recycled in stage 0 is advantageously recycled in stage P or also used to dilute the pulp resulting from stage P before its concentration.
Un procédé particulièrement adéquat consiste à diluer la pâte issue du traitement au peroxyde, à la concentrer sur un ou plusieurs appareils convenant pour l'essorage, à recueillir les effluents de ces essorages qui constituent les effluents du procédé selon l'invention, à utiliser de 30 à 95% de ces effluents pour l'étape de dilution de la pâte issue du traitement au peroxyde et à recycler le solde de ces effluents au traitement à l'oxygène.A particularly suitable method consists in diluting the paste resulting from the peroxide treatment, in concentrating it on one or more apparatuses suitable for wringing, in collecting the effluents from these wrings which constitute the effluents of the method according to the invention, in using 30 to 95% of these effluents for the step of diluting the pulp resulting from the peroxide treatment and recycling the balance of these effluents to the oxygen treatment.
Les appareils utilisés pour l'essorage de la pâte issue du traitement au peroxyde peuvent être également alimentés en une petite quantité d'eau fraîche ou d'une solution aqueuse. Dans ce cas, la quantité d'eau ou de solution aqueuse mise en oeuvre est sensiblement égale à la quantité d'effluents du traitement à l'oxygène envoyés aux chaudières de récupération.The devices used for wringing the dough from the peroxide treatment can also be supplied with a small amount of fresh water or an aqueous solution. In this case, the quantity of water or aqueous solution used is substantially equal to the quantity of effluents from the oxygen treatment sent to the recovery boilers.
Le stade P du procédé selon l'invention peut, selon le degré de blancheur désiré, être soumis à un ou plusieurs traitements de blanchiment supplémentaires. Ceux-ci sont choisis en général parmi les traitements au peroxyde, au dioxyde de chlore (appelés également stades D), à l'hypochlorite (appelés également stades H), aux peracides carboxyliques (appelés également stade P/J et au chlore (appelés également stades C) ou les extractions alcalines (appelées également stade E). Certaines séquences particulières de traitements ultérieurs ont donné de bons résultats : il s'agit des séquences CED, CEH, CHH, CPD, CPH, DED, DHD et DPD.Stage P of the process according to the invention can, depending on the desired degree of whiteness, be subjected to one or more additional bleaching treatments. These are generally chosen from treatments with peroxide, chlorine dioxide (also called stages D), hypochlorite (also called stages H), carboxylic peracids (also called stage P / J and chlorine (called also stages C) or alkaline extractions (also called stage E) Certain specific sequences of subsequent treatments have given good results: these are the CED, CEH, CHH, CPD, CPH, DED, DHD and DPD sequences.
Afin d'illustrer l'invention, on donne ci-après un exemple pratique de réalisation. L'exemple 2 a été réalisé à titre de comparaison en l'absence de recyclage.In order to illustrate the invention, a practical example is given below. Example 2 was carried out by way of comparison in the absence of recycling.
Une pâte kraft de pin (blancheur initiale 27,6 °ISO, indice kappa 39,6) a été soumise à un traitement en cinq étapes comportant un premier traitement à l'oxygène et un deuxième traitement au peroxyde avec recyclage de l'effluent de l'étape au peroxyde à l'étape à l'oxygène. Les conditions opératoires sont données ci-après. Les pourcentages des réactifs sont donnés par rapport à la pâte sèche.
La viscosité finale de la pâte issue de la dernière étape mesurée selon la norme TAPPI T 230 est de 12,0 mPa.s.The final viscosity of the paste from the last step measured according to the TAPPI T 230 standard is 12.0 mPa.s.
La même pâte kraft de pin que celle utilisée pour la réalisation de l'essai 1 a été soumise à un traitement en cinq étapes comportant un premier traitement à l'oxygène et un deuxième traitement au peroxyde sans recyclage de l'effluent de l'étape au peroxyde à l'étape à l'oxygène. Les autres conditions opératoires sont identiques à celles de l'essai 1.The same pine kraft pulp as that used for carrying out test 1 was subjected to a treatment in five stages comprising a first treatment with oxygen and a second treatment with peroxide without recycling of the effluent from stage with peroxide in the oxygen step. The other operating conditions are identical to those of test 1.
La viscosité finale de la pâte à l'issue de la dernière étape est de 10,8 mPa.s. La pâte cellulosique a donc subi une dépolymérisation plus importante que lors de l'utilisation du procédé selon l'invention.The final viscosity of the paste at the end of the last step is 10.8 mPa.s. The cellulose pulp therefore underwent a greater depolymerization than when the method according to the invention was used.
Claims (14)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT80200450T ATE2018T1 (en) | 1979-05-25 | 1980-05-14 | PROCESSES FOR DELIGNIFICATION AND BLEACHING OF CHEMICAL AND SEMI-CHEMICAL PULP. |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR7913554A FR2457339A1 (en) | 1979-05-25 | 1979-05-25 | PROCESS FOR THE DELIGNIFICATION AND BLEACHING OF CHEMICAL AND SEMI-CHEMICAL CELLULOSIC PASTA |
FR7913554 | 1979-05-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0019963A1 EP0019963A1 (en) | 1980-12-10 |
EP0019963B1 true EP0019963B1 (en) | 1982-12-15 |
Family
ID=9225939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP80200450A Expired EP0019963B1 (en) | 1979-05-25 | 1980-05-14 | Process for the delignification and bleaching of chemical and semichemical cellulose pulps |
Country Status (6)
Country | Link |
---|---|
US (1) | US4459174A (en) |
EP (1) | EP0019963B1 (en) |
AT (1) | ATE2018T1 (en) |
DE (1) | DE3061330D1 (en) |
ES (1) | ES491799A0 (en) |
FR (1) | FR2457339A1 (en) |
Families Citing this family (33)
Publication number | Priority date | Publication date | Assignee | Title |
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FR2566015B1 (en) * | 1984-06-15 | 1986-08-29 | Centre Tech Ind Papier | PROCESS FOR BLEACHING MECHANICAL PASTE WITH HYDROGEN PEROXIDE |
DE3802401A1 (en) * | 1988-01-28 | 1989-08-03 | Degussa | METHOD FOR PRODUCING SEMI-BLEACHED FUEL |
US4842877A (en) * | 1988-04-05 | 1989-06-27 | Xylan, Inc. | Delignification of non-woody biomass |
US5023097A (en) * | 1988-04-05 | 1991-06-11 | Xylan, Inc. | Delignification of non-woody biomass |
US5217574A (en) * | 1989-02-15 | 1993-06-08 | Union Camp Patent Holdings Inc. | Process for oxygen delignifying high consistency pulp by removing and recycling pressate from alkaline pulp |
US5173153A (en) * | 1991-01-03 | 1992-12-22 | Union Camp Patent Holding, Inc. | Process for enhanced oxygen delignification using high consistency and a split alkali addition |
US5409570A (en) * | 1989-02-15 | 1995-04-25 | Union Camp Patent Holding, Inc. | Process for ozone bleaching of oxygen delignified pulp while conveying the pulp through a reaction zone |
US5525195A (en) * | 1989-02-15 | 1996-06-11 | Union Camp Patent Holding, Inc. | Process for high consistency delignification using a low consistency alkali pretreatment |
US5085734A (en) * | 1989-02-15 | 1992-02-04 | Union Camp Patent Holding, Inc. | Methods of high consistency oxygen delignification using a low consistency alkali pretreatment |
US5188708A (en) * | 1989-02-15 | 1993-02-23 | Union Camp Patent Holding, Inc. | Process for high consistency oxygen delignification followed by ozone relignification |
US5211811A (en) * | 1989-02-15 | 1993-05-18 | Union Camp Patent Holding, Inc. | Process for high consistency oxygen delignification of alkaline treated pulp followed by ozone delignification |
US5011572A (en) * | 1989-05-19 | 1991-04-30 | Fmc Corporation | Two stage process for the oxygen delignification of lignocellulosic fibers with peroxide reinforcement in the first stage |
ATE97179T1 (en) * | 1989-06-06 | 1993-11-15 | Eka Nobel Ab | PROCESS FOR BLEACHING LIGNOCELLULOSE CONTAINING PULP. |
DE3923728A1 (en) * | 1989-07-18 | 1991-01-24 | Degussa | METHOD FOR STABILIZING THE VISCOSITY OF CELLS |
SE466061B (en) * | 1990-04-23 | 1991-12-09 | Eka Nobel Ab | Bleaching of chemical pulp by treatment with first a complexing agent and then a peroxide containing substance |
SE9001481L (en) * | 1990-04-23 | 1991-10-24 | Eka Nobel Ab | REDUCTION OF HALOGEN ORGANIC SUBSTANCES IN BLEACHING WASTE |
US5441603A (en) * | 1990-05-17 | 1995-08-15 | Union Camp Patent Holding, Inc. | Method for chelation of pulp prior to ozone delignification |
US5164044A (en) * | 1990-05-17 | 1992-11-17 | Union Camp Patent Holding, Inc. | Environmentally improved process for bleaching lignocellulosic materials with ozone |
US5164043A (en) * | 1990-05-17 | 1992-11-17 | Union Camp Patent Holding, Inc. | Environmentally improved process for bleaching lignocellulosic materials with ozone |
ES2049165B1 (en) * | 1990-08-10 | 1994-10-16 | Whites Martins Gases Ind S A | PROCEDURE FOR PRE-WHITENING OR DE-LIGNIFICATION OF KRAFT PASTA USING OXYGEN. |
BE1004674A3 (en) * | 1991-03-11 | 1993-01-12 | Interox Internat Sa | Method of laundering of chemical pulp and application of the method of laundering pulp kraft. |
SE468355B (en) * | 1991-04-30 | 1992-12-21 | Eka Nobel Ab | CHEMISTRY OF CHEMICAL MASS THROUGH TREATMENT WITH COMPLEX PICTURES AND OZONE |
US5554259A (en) * | 1993-10-01 | 1996-09-10 | Union Camp Patent Holdings, Inc. | Reduction of salt scale precipitation by control of process stream Ph and salt concentration |
US5672247A (en) * | 1995-03-03 | 1997-09-30 | Union Camp Patent Holding, Inc. | Control scheme for rapid pulp delignification and bleaching |
US5736004A (en) * | 1995-03-03 | 1998-04-07 | Union Camp Patent Holding, Inc. | Control scheme for rapid pulp delignification and bleaching |
US5656130A (en) * | 1995-04-28 | 1997-08-12 | Union Camp Holding, Inc. | Ambient temperature pulp bleaching with peroxyacid salts |
US5705216A (en) * | 1995-08-11 | 1998-01-06 | Tyson; George J. | Production of hydrophobic fibers |
BE1011129A4 (en) * | 1997-04-25 | 1999-05-04 | Solvay Interox | Delignification continuous process and / or money virgin pulp chemical or recycled. |
WO2003008120A2 (en) * | 2001-07-17 | 2003-01-30 | Zhi-Wei Liang | Oxidative thermochemical drying process for changing hydrophilic/hydrophobic characteristics of natural organic substances |
ATE386837T1 (en) * | 2004-06-14 | 2008-03-15 | Warwick Internat Group Ltd | ACTIVATOR FOR PULP BLEACHING |
US8138106B2 (en) | 2005-09-30 | 2012-03-20 | Rayonier Trs Holdings Inc. | Cellulosic fibers with odor control characteristics |
AU2008313142B2 (en) * | 2007-10-17 | 2013-05-23 | Nippon Steel & Sumikin Chemical Co., Ltd. | Production methods for solubilized lignin, saccharide raw material and monosaccharide raw material, and solubilized lignin |
FR2951096B1 (en) | 2009-10-09 | 2013-03-15 | Total Sa | PROCESS FOR OXIDATION OF ORGANIC COMPOUNDS |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FI45574C (en) * | 1970-05-11 | 1972-07-10 | Kymin Oy Kymmene Ab | Process for bleaching cellulosic materials. |
US4196043A (en) * | 1970-12-21 | 1980-04-01 | Scott Paper Company | Kraft pulp bleaching and recovery process |
CA966604A (en) * | 1970-12-21 | 1975-04-29 | Scott Paper Company | Kraft pulp bleaching and recovery process |
US3719552A (en) * | 1971-06-18 | 1973-03-06 | American Cyanamid Co | Bleaching of lignocellulosic materials with oxygen in the presence of a peroxide |
US4372812A (en) * | 1978-04-07 | 1983-02-08 | International Paper Company | Chlorine free process for bleaching lignocellulosic pulp |
-
1979
- 1979-05-25 FR FR7913554A patent/FR2457339A1/en active Granted
-
1980
- 1980-05-14 EP EP80200450A patent/EP0019963B1/en not_active Expired
- 1980-05-14 DE DE8080200450T patent/DE3061330D1/en not_active Expired
- 1980-05-14 AT AT80200450T patent/ATE2018T1/en not_active IP Right Cessation
- 1980-05-23 ES ES491799A patent/ES491799A0/en active Granted
-
1982
- 1982-07-21 US US06/400,380 patent/US4459174A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
ES8102237A1 (en) | 1980-12-16 |
DE3061330D1 (en) | 1983-01-20 |
ATE2018T1 (en) | 1982-12-15 |
EP0019963A1 (en) | 1980-12-10 |
FR2457339B1 (en) | 1982-09-17 |
ES491799A0 (en) | 1980-12-16 |
US4459174A (en) | 1984-07-10 |
FR2457339A1 (en) | 1980-12-19 |
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