EP0056263A1 - A method for improving the washing of cellulose pulps produced from lignocellulosic material - Google Patents

A method for improving the washing of cellulose pulps produced from lignocellulosic material Download PDF

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Publication number
EP0056263A1
EP0056263A1 EP82100102A EP82100102A EP0056263A1 EP 0056263 A1 EP0056263 A1 EP 0056263A1 EP 82100102 A EP82100102 A EP 82100102A EP 82100102 A EP82100102 A EP 82100102A EP 0056263 A1 EP0056263 A1 EP 0056263A1
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Prior art keywords
pulp
washing
mild mechanical
treatment process
mechanical treatment
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EP82100102A
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German (de)
French (fr)
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EP0056263B1 (en
Inventor
Jonas Arne Ingvar Lindahl
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Mo och Domsjo AB
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Mo och Domsjo AB
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-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
    • D21C9/02Washing ; Displacing cooking or pulp-treating liquors contained in the pulp by fluids, e.g. wash water or other pulp-treating agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21DTREATMENT OF THE MATERIALS BEFORE PASSING TO THE PAPER-MAKING MACHINE
    • D21D1/00Methods of beating or refining; Beaters of the Hollander type
    • D21D1/20Methods of refining
    • D21D1/40Washing the fibres

Definitions

  • the present invention relates to a method for washing cellulose pulps produced from lignocellulosic material more effectively than when applying known washing techniques, so as to improve the recovery of chemicals and combustible organic materials from the waste liquors.
  • cellulose pulp is meant primarily chemicals pulps, semi-chemical pulps and chemi-mechanical pulps produced from both softwood and hardwood.
  • the wood chips When producing cellulose pulps with a yield in excess of about 55%, the wood chips are normally mechanically defibrated to separate fibre form, prior to washing and/or screening the pulp. When screening the pulp, there is obtained a concentration of the non-defibrated wood residues, referred to as reject or tailings, which are normally defibrated in a separate stage to separate fibre form, and then returned to the pulp flow.
  • the pulp suspension obtained subsequent to delignifying the wood chips can be washed in accordance with a number of mutually differing methods known to the art.
  • the oldest method is one in which the pulp suspension is washed in so-called diffusers, i.e. a displacement wash which is carried out batchwise in large vessels.
  • the pulp suspension is washed on drum filters, normally in several stages. The number of drum filters may vary, although normally from three to four filters are used.
  • pulp is washed with the use of presses whereat greater volumes of liquid can be removed than when using filters, which results in a more effective recovery of chemicals and organic substances.
  • the present invention affords a solution to the aforementioned problems and makes possible an increase in the extent to which chemicals are recovered. Accordingly, the invention relates to a method for improving the washing of unbleached cellulose pulp produced from lignocellulosic material, in which the starting material is chemically delignified (cooking) and, subsequent to being optionally mechanically defibrated is washed in a known manner in a plurality of stages, while charging water thereto.
  • the method is characterized in that, after having been partially washed, the pulp between a pair of the washing stages or between several of said washing stages is subjected to a mild mechanical working treatment in a device adapted for high-consistency treatment and provided with relative to each other rotating screws at an energy input of from 7 to 200 kWh per ton of pulp.
  • the cleansing effect obtained has been found to be particularly good when at least 10% of the impurities originally present in the pulp suspension are removed in the partial wash preceding the mild mechanical treatment process.
  • at least 10% of the dry solids content of the cooking waste liquor should be washed out prior to subjecting the pulp suspension to the mild mechanical treatment process.
  • pulp dry solids content prior to the mild mechanical treatment process it has also been found particularly suitable to increase the pulp dry solids content prior to the mild mechanical treatment process, to between 10% and 50%, preferably to between 14 and 40%, and suitably to between 20 and 35%.
  • the pulp suspension is diluted to a pulp consistency of between 0.5 and 13%, in conjunction with mixing with wash liquid in the subsequent washing step.
  • the most suitable pulp consistency lies between 0.5 and 6%, while washing-dewatering in, for example, a press is suitably performed at an input pulp consistency of between 2 and 13%.
  • the mild mechanical treatment process according to the invention can be carried out at all temperatures normally used in practice.
  • a particularly suitable temperature range is 20-l10°C, while a preferred range is 35-90°C.
  • mild mechanical treatment is meant here a process in which pulp suspensions of the aforementioned dry solids contents are subjected to a repeated pressing, kneading and shearing treatment, whereat the input of electrical energy for carrying out said treatment is held within the range of 7 to 200 kWh per ton of bone-dry pulp, and preferably within the range of 10 to 100 kWh per ton of bone-dry pulp.
  • a screw-type defibrator of the kind comprising two rotatable, bladed screws which are arranged parallel to one another in a housing provided with an inlet and outlet, and which are in adjustable meshing engagement with one another, to provide the mild mechanical treatment of the material, as before described.
  • the screw blades of the rotatable screws also exhibit concave portions at the periphery of at least some of the screw turns, to form teeth-like protrusions between said concave portions.
  • Screw defibrators of the aforedescribed kind are sold by MoDoMekan AB under the registered trademark FROTAPULPEF®.
  • the novel method according to the invention in which the pulp suspension is mechanically treated in a mild fashion between two or more of the stages of a washing sequence, has been surprisingly found to provide a cleaner pulp and to result in higher chemical recovery, a lower discharge of impurities to the surroundings and a higher dry solids content of the effluent washing water than was previously the case, when applying conventional washing techniques.
  • the present invention affords the important advantage of enabling a purer pulp to be obtained. This is manifested, inter alia, by a considerable lowering of the extractive content of the pulp and its kappa number.
  • the advantages afforded by the method according to the invention also include the possibility of increasing the dry solids content of the liquor departing from the pulp-washing stage, i.e. the amount of organic materials contained by said liquor, and also the amount of inorganic chemicals contained thereby.
  • This increases the fuel value of the washing liquid, representing a valuable saving on energy.
  • the amount of environmentally harmful substances contained in the effluent is less than would otherwise be the case, which is an important advantage, and also desirable from an environmental aspect. Consequently, the cost involved in the treatment and destruction of environmentally harmful substances in the effluent can be reduced when applying the invention.
  • a further advantageous and surprising effect afforded by the invention is that the consumption of bleaching chemicals, such as chlorine, chlorine dioxide, hypochlorite, hydrogen peroxide and oxygen gas is markedly reduced when bleaching the washed pulp.
  • bleaching chemicals such as chlorine, chlorine dioxide, hypochlorite, hydrogen peroxide and oxygen gas
  • Another surprising effect obtained by the inclusion of the mild mechanical treatment process according to the invention is that the dewatering of the resultant pulp suspension is markedly improved a fact which affords decisive advantages when further treating the pulp.
  • the Figure illustrates schematically a suitable embodiment of the method according to the invention applied in washing tests with birch sulphate pulp and chemi-mechanical spruce pulp in three stages, each of said stages being equipped with a press.
  • a screw defibrator of the kind sold under the trademark FROTAPULPER®
  • Unbleached and unwashed birch sulphate pulp was introduced through a line 1 into a tank 2, in which the pulp suspension was diluted with press waste liquor supplied through a line 22, until a pulp consistency of about 8% was obtained.
  • the pulp suspension was passed from the tank 2 through a line 3 to a first washing stage 4, comprising a press, in which the pulp suspension was thickened to a dry solids content of 33.3% and then passed through a line 5, to a screw feeder 6, arranged to feed the pulp suspension through a line 7 and a line 8 to a screw defibrator 10 provided with two rotating screws whose blades exhibited concaved portions and in which the pulp suspension was subjected to a mild mechanical treatment process, whereafter said suspension was passed to a second screw feeder 12 through a line 11.
  • the temperature of the pulp suspension at the inlet to the screw defibrator 10 was measured as 68°C, and at the outlet of said defibrator as 71 0 C.
  • the amount of electrical energy consumed by the mild mechanical treatment process in the screw defibrator 10 was measured to 15 kWh per ton of bone-dry pulp.
  • the line 9 was closed while passing the pulp suspension through the defibrator 10.
  • the treated pulp suspension was diluted in the screw feeder 12 to a pulp consistency of 8%, by introducing press waste liquor to said feeder through a line 21, said waste liquor mixing effectively with the pulp suspension during its transport through the feeder 12.
  • the diluted pulp suspension was then passed through a line 13 to a second washing stage 14, comprising a press similar to that used in the first washing stage.
  • the pulp suspension was washed and again thickened in the press 14, to a dry solids content of 33.3%.
  • Waste liquor obtained from the press 14 was passed through a line 22 to the tank 2, where it was used to dilute incoming pulp suspension.
  • the pulp suspension, washed and thickened in the second washing stage was then passed through a line 15 to a screw feeder 16, and through a line 17 to a third washing stage equipped with a press 18 similar to the presses used in the two preceding washing stages.
  • the pulp suspension was diluted and mixed in the screw feeder 16. in a manner similar to that in the preceding screw feeder 12, although in this case with pure water supplied through a line 20, to obtain a pulp-consistency of 8%. Subsequent to washing the pulp suspension and thickening the same to a dry solids content of 33.3% in the press 18, the finally washed pulp suspension was removed through a line 19.
  • Example 1 The test described in Example 1 was repeated with chemi-mechanical spruce pulp cooked to a pulp yield of 73%, calculated on absolute dry wood. After washing the pulp suspension and thickening the same in the press 14 of the second washing stage, there was obtained in this test a dry solids content of 34%. A dry solids content of 34% was similarly obtained after washing and thickening the pulp in the press 18 of the third washing stage. The line 9 was closed when making this test.

Abstract

To provide a cleaner pulp and to obtain a higher chemical recovery during washing of chemically cooked and optionally defibrated cellulose pulp, the partially washed pulp is subjected to a mild mechanical treatment e.g. in a device (10) adapted for high-consistency treatment and provided with screwsrotat- ing relative to each other, said treatment taking place between at least one pair of conventional washing stages (4,14).

Description

    Technical field
  • The present invention relates to a method for washing cellulose pulps produced from lignocellulosic material more effectively than when applying known washing techniques, so as to improve the recovery of chemicals and combustible organic materials from the waste liquors. By cellulose pulp is meant primarily chemicals pulps, semi-chemical pulps and chemi-mechanical pulps produced from both softwood and hardwood.
  • Background art
  • In the chemical pulping of lignocellulosic material there is obtained a residue which contains inorganic chemicals and dissolved organic substances, said substances comprising mainly lignin and minor quantities of cellulose, together with extractive substances, such as resin. Undesirable residual material is washed away. The waste liquor and washing liquid obtained are evaporated and burned, normally so that the chemicals can be recovered. Thus, in order to facilitate recovery of the chemicals, a washing effluent having the highest possible dry solids content is constantly sought for, i.e. attemps are made to use the least possible amount of water during the washing process.
  • When producing cellulose pulps with a yield in excess of about 55%, the wood chips are normally mechanically defibrated to separate fibre form, prior to washing and/or screening the pulp. When screening the pulp, there is obtained a concentration of the non-defibrated wood residues, referred to as reject or tailings, which are normally defibrated in a separate stage to separate fibre form, and then returned to the pulp flow.
  • The pulp suspension obtained subsequent to delignifying the wood chips can be washed in accordance with a number of mutually differing methods known to the art. The oldest method is one in which the pulp suspension is washed in so-called diffusers, i.e. a displacement wash which is carried out batchwise in large vessels. In another method, which is common at present, the pulp suspension is washed on drum filters, normally in several stages. The number of drum filters may vary, although normally from three to four filters are used. In a further and more recent method, pulp is washed with the use of presses whereat greater volumes of liquid can be removed than when using filters, which results in a more effective recovery of chemicals and organic substances.
  • Disclosure of the invention Technical problem
  • When applying the aforedescribed washing techniques, however, significant quantities of residual chemicals and undesirable organic substances are left in the pulp, which, when the pulp is to be subsequently bleached, results in an unnecessarily high consumption of bleaching chemicals, and causes an undesirably high quantity of substances harmful to the environment to be discharged to the surroundings. Further, an increase in the extent to which chemicals used in the cellulose processes can be recovered is also highly desirable, both from an economic and environmental aspect.
  • Solution
  • The present invention affords a solution to the aforementioned problems and makes possible an increase in the extent to which chemicals are recovered. Accordingly, the invention relates to a method for improving the washing of unbleached cellulose pulp produced from lignocellulosic material, in which the starting material is chemically delignified (cooking) and, subsequent to being optionally mechanically defibrated is washed in a known manner in a plurality of stages, while charging water thereto. The method is characterized in that, after having been partially washed, the pulp between a pair of the washing stages or between several of said washing stages is subjected to a mild mechanical working treatment in a device adapted for high-consistency treatment and provided with relative to each other rotating screws at an energy input of from 7 to 200 kWh per ton of pulp.
  • When applying the method according to the invention, the cleansing effect obtained has been found to be particularly good when at least 10% of the impurities originally present in the pulp suspension are removed in the partial wash preceding the mild mechanical treatment process. In other words, at least 10% of the dry solids content of the cooking waste liquor should be washed out prior to subjecting the pulp suspension to the mild mechanical treatment process.
  • It has also been found particularly suitable to increase the pulp dry solids content prior to the mild mechanical treatment process, to between 10% and 50%, preferably to between 14 and 40%, and suitably to between 20 and 35%. Upon completion of the mild mechanical treatment process, the pulp suspension is diluted to a pulp consistency of between 0.5 and 13%, in conjunction with mixing with wash liquid in the subsequent washing step. When the pulp is washed on filters, the most suitable pulp consistency lies between 0.5 and 6%, while washing-dewatering in, for example, a press is suitably performed at an input pulp consistency of between 2 and 13%.
  • The mild mechanical treatment process according to the invention can be carried out at all temperatures normally used in practice. However, a particularly suitable temperature range is 20-l10°C, while a preferred range is 35-90°C.
  • By mild mechanical treatment is meant here a process in which pulp suspensions of the aforementioned dry solids contents are subjected to a repeated pressing, kneading and shearing treatment, whereat the input of electrical energy for carrying out said treatment is held within the range of 7 to 200 kWh per ton of bone-dry pulp, and preferably within the range of 10 to 100 kWh per ton of bone-dry pulp.
  • It has been found particularly suitable to effect the mild mechanical treatment process according to the invention in a screw-type defibrator of the kind comprising two rotatable, bladed screws which are arranged parallel to one another in a housing provided with an inlet and outlet, and which are in adjustable meshing engagement with one another, to provide the mild mechanical treatment of the material, as before described. Conveniently, the screw blades of the rotatable screws also exhibit concave portions at the periphery of at least some of the screw turns, to form teeth-like protrusions between said concave portions. Screw defibrators of the aforedescribed kind are sold by MoDoMekan AB under the registered trademark FROTAPULPEF®.
  • Advantages
  • The novel method according to the invention, in which the pulp suspension is mechanically treated in a mild fashion between two or more of the stages of a washing sequence, has been surprisingly found to provide a cleaner pulp and to result in higher chemical recovery, a lower discharge of impurities to the surroundings and a higher dry solids content of the effluent washing water than was previously the case, when applying conventional washing techniques.
  • Thus, the present invention affords the important advantage of enabling a purer pulp to be obtained. This is manifested, inter alia, by a considerable lowering of the extractive content of the pulp and its kappa number.
  • The advantages afforded by the method according to the invention also include the possibility of increasing the dry solids content of the liquor departing from the pulp-washing stage, i.e. the amount of organic materials contained by said liquor, and also the amount of inorganic chemicals contained thereby. This increases the fuel value of the washing liquid, representing a valuable saving on energy. Because:moTe contaminants are brought to evaporation and burning, and a greater amount of chemicals are recovered, the amount of environmentally harmful substances contained in the effluent is less than would otherwise be the case, which is an important advantage, and also desirable from an environmental aspect. Consequently, the cost involved in the treatment and destruction of environmentally harmful substances in the effluent can be reduced when applying the invention.
  • A further advantageous and surprising effect afforded by the invention is that the consumption of bleaching chemicals, such as chlorine, chlorine dioxide, hypochlorite, hydrogen peroxide and oxygen gas is markedly reduced when bleaching the washed pulp.
  • Another surprising effect obtained by the inclusion of the mild mechanical treatment process according to the invention, is that the dewatering of the resultant pulp suspension is markedly improved a fact which affords decisive advantages when further treating the pulp.
  • The advantages afforded by the method according to the invention are further illustrated by the examples shown in the description.
  • Brief description of the drawing
  • The Figure illustrates schematically a suitable embodiment of the method according to the invention applied in washing tests with birch sulphate pulp and chemi-mechanical spruce pulp in three stages, each of said stages being equipped with a press. In the tests there was installed between the first and second washing stages a screw defibrator of the kind sold under the trademark FROTAPULPER®
  • Best mode of carrying out the invention
  • The following examples set forth experiments carried out in accordance with a preferred embodiment of the described method, together with the results obtained.
  • In the following tests, which were carried out in parallel, birch sulphate pulp and chemi-mechanical spruce pulp were washed in three stages, partly in accordance with the invention, incorporating said mild mechanical treatment process between the first and second washing stages (Examples 1 and 2), and partly in accordance with conventional techniques (Controls 1 and 2), in which the pulp suspensions were not subjected to any form of mechanical treatment between the different stages of the washing sequence.
  • The process diagram illustrated in the Figure was utilized in all tests, and hence the reference numerals below refer to corresponding references in the Figure.
  • Example 1
  • Unbleached and unwashed birch sulphate pulp was introduced through a line 1 into a tank 2, in which the pulp suspension was diluted with press waste liquor supplied through a line 22, until a pulp consistency of about 8% was obtained. The pulp suspension was passed from the tank 2 through a line 3 to a first washing stage 4, comprising a press, in which the pulp suspension was thickened to a dry solids content of 33.3% and then passed through a line 5, to a screw feeder 6, arranged to feed the pulp suspension through a line 7 and a line 8 to a screw defibrator 10 provided with two rotating screws whose blades exhibited concaved portions and in which the pulp suspension was subjected to a mild mechanical treatment process, whereafter said suspension was passed to a second screw feeder 12 through a line 11. The temperature of the pulp suspension at the inlet to the screw defibrator 10 was measured as 68°C, and at the outlet of said defibrator as 710C. The amount of electrical energy consumed by the mild mechanical treatment process in the screw defibrator 10 was measured to 15 kWh per ton of bone-dry pulp. The line 9 was closed while passing the pulp suspension through the defibrator 10.
  • The treated pulp suspension was diluted in the screw feeder 12 to a pulp consistency of 8%, by introducing press waste liquor to said feeder through a line 21, said waste liquor mixing effectively with the pulp suspension during its transport through the feeder 12. The diluted pulp suspension was then passed through a line 13 to a second washing stage 14, comprising a press similar to that used in the first washing stage. The pulp suspension was washed and again thickened in the press 14, to a dry solids content of 33.3%. Waste liquor obtained from the press 14 was passed through a line 22 to the tank 2, where it was used to dilute incoming pulp suspension. The pulp suspension, washed and thickened in the second washing stage, was then passed through a line 15 to a screw feeder 16, and through a line 17 to a third washing stage equipped with a press 18 similar to the presses used in the two preceding washing stages.
  • The pulp suspension was diluted and mixed in the screw feeder 16. in a manner similar to that in the preceding screw feeder 12, although in this case with pure water supplied through a line 20, to obtain a pulp-consistency of 8%. Subsequent to washing the pulp suspension and thickening the same to a dry solids content of 33.3% in the press 18, the finally washed pulp suspension was removed through a line 19.
  • Press waste liquors were removed from the lines 21 and 22 during the tests, for analysis purposes'. Samples of the finally washed pulp were also taken from the line 19. The analysis results are shown in Table 1. Waste liquor from the press in the first washing stage 4 was taken through a line 23 and passed to a recovery plant (not shown in the drawing), where said waste liquor was evaporated and burned. Because the washing liquid was passed in counter-flow to the flow of pulp suspension, and because of the mechanical treatment to which the pulp suspension was subjected, the press waste liquor had a high organic-substance content (about 13%) and, at the same time, a high fuel value.
  • Control test 1
  • In this test there was washed a birch sulphate pulp taken from the same batch as the pulp used in Example 1 and treated in the same apparatus, although with the difference that the pulp suspension was not subjected to a mild mechanical treatment process between the first and second washing stages. Thus, all flow of pulp suspension through the line 8 was stopped, so that the pulp suspension passed instead directly to the second screw feeder 12, through the line 9.
  • Subsequent to washing and thickening the pulp suspension in the press 14 of the second washing stage, there was obtained in this case a dry solids content of 26%. After washing and thickening the suspension in the press 18 of the third washing
    stage, there was also obtained a dry solids content of 26%. It will be noted that the consistency of the pulp suspension at the inlets to presses 14 and 18 respectively was also 8% in this test, and that the pressure exerted by the presses was the same as that in
  • Example 1.
  • Analysis samples were removed in this test at the same locations as in the test according to Example 1. The analysis results are shown in Table 1 below.
    Figure imgb0001
  • As will be seen from the Table, when applying the method according to the invention quite surprisingly a considerably better washing was obtained than can be obtained when washing in accordance with known techniques. Thus has for example despite the fact that the mild mechanical treatment process was carried out on a pulp suspension which had only been partially washed, the method according to the invention surprisingly resulted in a pulp with a much lower extractives content than can be obtained when conventionally ' washing pulp without mechanically treating the pulp between washing stages.
  • One important advantage with respect to energy afforded by the increased extent to which organic substances are washed from the pulp is that the fuel value of the waste liquor is also increased. Further a higher percentage of the cooking chemicals are recovered.
  • Example 2
  • The test described in Example 1 was repeated with chemi-mechanical spruce pulp cooked to a pulp yield of 73%, calculated on absolute dry wood. After washing the pulp suspension and thickening the same in the press 14 of the second washing stage, there was obtained in this test a dry solids content of 34%. A dry solids content of 34% was similarly obtained after washing and thickening the pulp in the press 18 of the third washing stage. The line 9 was closed when making this test.
  • Control test 2
  • In this test a similar type of chemi-mechanical spruce pulp was washed, and treated in the same plant as that used in Example 2, although with the difference that the pulp suspension was not subjected to any form of mild mechanical treatment between any of the washing stages. Thus all flow of pulp suspension through the line 8 was stopped, so that the pulp suspension instead passed directly to the second screw feeder 12, through the line 9. Subsequent to passing the press 14 of the second washing stage, the dry solids content was found to be 30a. The dry solids content was also found to be 30% after passing the press 18 of the third washing stage.
  • When making a comparison between washing the pulp in accordance with known techniques and washing the pulp in accordance with the present invention, it can be concluded that more water is removed and more chemicals recovered when practicing the method according to the invention. This conclusion is based on the fact that the volume of waste liquor recovered when applying the present invention was greater, despite the fact that the consistencies of the pulp suspensions entering the presses, in both tests, were maintained constant at 7%. According to measurements taken, the washing water in Example 2 also contained slightly larger quantities of'dry solids than the washing water in Control test 2. Thus, it can be established that the fuel values of the liquors obtained when applying the method according to the invention are higher than the fuel values of corresponding liquors obtained when washing chemi-mechanical pulp in accordance with conventional techniques.

Claims (5)

1. A method for improving the washing of unbleached cellulose pulp when producing cellulose pulps from lignocellulosic material, in which the starting material is chemically delignified and, subsequent to being optionally mechanically defibrated, is washed, in a known manner, in a plurality of stages while supplying water thereto, characterized in, that the pulp, after having been partially washed, between a pair of the washing stages or between several of said washing stages is subjected to a mild mechanical working treatment in a device adapted for high-consistency treatment and provided with relative to each other rotating screws at an energy input of from 7 to 200 kWh per ton of pulp.
2. A method according to Claim 1,
characterized in, that at least 10% of the dry solids content of the cooking waste liquor is removed during the partial washing step preceding the mild mechanical treatment process.
3. A method according to Claims 1 and 2,
characterized in, that the mild mechanical treatment process is carried out at a pulp dry solids content of between 10 and 50%, preferably between 14 and 40% and suitably between 20 and 35%.
4. A method according to Claims 1-3,
characterized in, that the electrical energy input to the mild mechanical treatment process is held within the range of 10 to 100 kWh/ton.
5. A method according to Claims 1-4,
characterized in, that the mild mechanical treatment process is carried out in a screw defibrator of the kind comprising two rotatable, bladed screws which are arranged parallel to one another in a housing provided with an inlet and an outlet and which engage in each other for mildly treating the material, and the screw blades of which exhibit concave portions on the periphery of at least some screw turns to form tooth-like protrusions between said concave portions;
EP82100102A 1981-01-14 1982-01-08 A method for improving the washing of cellulose pulps produced from lignocellulosic material Expired EP0056263B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT82100102T ATE14762T1 (en) 1981-01-14 1982-01-08 PROCESS FOR IMPROVING WASHING OF CELLULOSIC PULP MADE FROM LIGNOCELLULOSIC MATERIAL.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8100179A SE443383C (en) 1981-01-14 1981-01-14 PROCEDURE FOR WASHING CELLULOSAMASSA
SE8100179 1981-01-14

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EP0056263A1 true EP0056263A1 (en) 1982-07-21
EP0056263B1 EP0056263B1 (en) 1985-08-07

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AT (1) ATE14762T1 (en)
AU (1) AU548277B2 (en)
CA (1) CA1164704A (en)
DE (1) DE3265116D1 (en)
FI (1) FI69656C (en)
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SE (1) SE443383C (en)

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* Cited by examiner, † Cited by third party
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EP0315737A1 (en) * 1987-11-11 1989-05-17 A. Ahlstrom Corporation Method and apparatus for treating pulp
WO2002033164A2 (en) * 2000-10-17 2002-04-25 James Hardie Research Pty Limited Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
EP1574614A2 (en) 2000-10-17 2005-09-14 James Hardie International Finance B.V. Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
US7727329B2 (en) 2000-03-14 2010-06-01 James Hardie Technology Limited Fiber cement building materials with low density additives
US7815841B2 (en) 2000-10-04 2010-10-19 James Hardie Technology Limited Fiber cement composite materials using sized cellulose fibers
US7942964B2 (en) 2003-01-09 2011-05-17 James Hardie Technology Limited Fiber cement composite materials using bleached cellulose fibers
US7993570B2 (en) 2002-10-07 2011-08-09 James Hardie Technology Limited Durable medium-density fibre cement composite
US8209927B2 (en) 2007-12-20 2012-07-03 James Hardie Technology Limited Structural fiber cement building materials
WO2015199604A1 (en) * 2014-06-26 2015-12-30 Valmet Ab Arrangement and system for a treatment process

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE445051B (en) * 1980-04-10 1986-05-26 Sca Development Ab SET FOR MANUFACTURING MECHANICAL, MAINLY HEART-FREE CELLULOSAMASSA
FI77063B (en) * 1986-12-17 1988-09-30 Ahlstroem Oy FOERFARANDE FOER EFFEKTIVERING AV FIBERSUSPENSIONSTVAETT.
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
EP1368285B1 (en) 2001-03-09 2007-04-11 James Hardie International Finance B.V. Fiber reinforced cement composite materials using chemically treated fibers with improved dispersibility
US7998571B2 (en) 2004-07-09 2011-08-16 James Hardie Technology Limited Composite cement article incorporating a powder coating and methods of making same
NZ571874A (en) 2006-04-12 2010-11-26 Hardie James Technology Ltd A surface sealed reinforced building element
DE102007036377A1 (en) * 2007-07-31 2009-02-05 Voith Patent Gmbh Use of washing and screw presses for raw material and pulp washing

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0017544A1 (en) * 1979-03-22 1980-10-15 Creusot-Loire Process for preparing a paper pulp

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0017544A1 (en) * 1979-03-22 1980-10-15 Creusot-Loire Process for preparing a paper pulp

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Tappi Journal of the Technical Association of the Pulp and Paper Industry, Vol. 62, No. 8, August 1979 Atlanta, GA, US B. VIKSTROM: "Defibration in Highyield Kraft Pulping. Influence of Degree of Washing on the Physical Properties of Cooked Wood Chips and on the Results of Defibration" pages 69-72 * entire Article * *

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EP0315737A1 (en) * 1987-11-11 1989-05-17 A. Ahlstrom Corporation Method and apparatus for treating pulp
US4952314A (en) * 1987-11-11 1990-08-28 A. Ahlstrom Corporation Apparatus for treating pulp
US8182606B2 (en) 2000-03-14 2012-05-22 James Hardie Technology Limited Fiber cement building materials with low density additives
US7727329B2 (en) 2000-03-14 2010-06-01 James Hardie Technology Limited Fiber cement building materials with low density additives
US7815841B2 (en) 2000-10-04 2010-10-19 James Hardie Technology Limited Fiber cement composite materials using sized cellulose fibers
KR100865807B1 (en) * 2000-10-17 2008-10-28 제임스 하디 인터내셔널 파이낸스 비.브이. Method and Apparatus for Reducing Impurities in Cellulose Fibers for Manufacture of Fiber Reinforced Cement Composite Materials
EP1574614A3 (en) * 2000-10-17 2005-11-16 James Hardie International Finance B.V. Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
AU2001296904B2 (en) * 2000-10-17 2007-08-30 James Hardie Technology Limited Method and apparatus for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
EP1574614A2 (en) 2000-10-17 2005-09-14 James Hardie International Finance B.V. Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
WO2002033164A3 (en) * 2000-10-17 2002-07-04 James Hardie Res Pty Ltd Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
AU2001296904B8 (en) * 2000-10-17 2002-04-29 James Hardie Technology Limited Method and apparatus for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
WO2002033164A2 (en) * 2000-10-17 2002-04-25 James Hardie Research Pty Limited Method for reducing impurities in cellulose fibers for manufacture of fiber reinforced cement composite materials
US7993570B2 (en) 2002-10-07 2011-08-09 James Hardie Technology Limited Durable medium-density fibre cement composite
US7942964B2 (en) 2003-01-09 2011-05-17 James Hardie Technology Limited Fiber cement composite materials using bleached cellulose fibers
US8333836B2 (en) 2003-01-09 2012-12-18 James Hardie Technology Limited Fiber cement composite materials using bleached cellulose fibers
US8209927B2 (en) 2007-12-20 2012-07-03 James Hardie Technology Limited Structural fiber cement building materials
WO2015199604A1 (en) * 2014-06-26 2015-12-30 Valmet Ab Arrangement and system for a treatment process
US10047408B2 (en) 2014-06-26 2018-08-14 Valmet Ab Arrangement and system for a treatment process

Also Published As

Publication number Publication date
NO160219B (en) 1988-12-12
NO160219C (en) 1989-03-22
SE443383C (en) 1987-07-14
FI69656B (en) 1985-11-29
DE3265116D1 (en) 1985-09-12
FI820005L (en) 1982-07-15
JPS63557B2 (en) 1988-01-07
FI69656C (en) 1991-12-24
ATE14762T1 (en) 1985-08-15
SE8100179L (en) 1982-07-15
CA1164704A (en) 1984-04-03
SE443383B (en) 1986-02-24
JPS57139591A (en) 1982-08-28
AU548277B2 (en) 1985-12-05
NO820095L (en) 1982-07-15
EP0056263B1 (en) 1985-08-07
AU7917582A (en) 1982-07-22

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