• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a process for the continuous digestion of finely divided cellulosic material, such as wood chips. The finely divided material is passed, in a liquid-filled vessel (11), in the form of a continuous column of chips through an intake zone (B), a heating and impregnating zone (C), a digestion zone (D) and a washing zone (E), the temperature in the heating and impregnating zone (C) being kept lower than that in the digestion zone (D). In order to maintain a stable temperature profile and a stable chemical profile in these zones, the liquid (41) fed in with the chips is caused to flow through the column of chips in the intake zone (B) in the feeding direction of the chips at such a velocity, before the said liquid is drawn off (21), that the said column of chips is passed through the downstream impregnating zone (C), where impregnating liquid (42) is adjusted in counter-current to the column of chips moving forward in such a way that the heat capacity flux of the said impregnating liquid is at least equal to the heat capacity flux of the column of chips moving forward (Fig. 1). <IMAGE>
    公开号:SU1475491A3
    申请号:SU833677056
    申请日:1983-12-13
    公开日:1989-04-23
    发明作者:Хокан Эстман Пер
    申请人:Эконо Ой (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to a method for continuous cooking of chips and can be used in the pulp and paper industry in the production of various types of paper and cardboard.
    The purpose of the invention is to intensify the process by reducing energy costs.
    The proposed method of continuous cooking of chips includes the transportation of chips in series through the zones of the first direct processing, countercurrent impregnation, the second direct processing of the cooking liquor with increasing temperature in each subsequent zone and washing, while transporting the chips through the counter-.
    Sequence impregnation is carried out in a turbulent mode, which is created by a differential pressure before entering the impregnation zone, adjusting the speed of extracting the cooking liquor from the first treatment zone or adjusting the level of chips in the same zone. The drawing shows a scheme for implementing the method.
    The chips are metered into the loading hopper 1 with the ability to maintain a chip column of such height above the liquid level so that the chips are squeezed into the discharge device (not shown) for further transfer. Through the pipe 2 to the feeder 3 together with the liquid that
    ate
    four
    WITH

    about

    31
    It enters the named hopper through the buoy 4 using a circulation pump 5. In the chip feeder, it is transferred to the pipe 6 for supplying the first feed-through treatment of the brewing unit through connection 7 together with a liquid that is supplied to the sluice feeder by means of a circulation pump 8. The cooking liquid that is introduced through the pipe 9 to circulate chips to the sluice feeder, and the feed liquid, which is transferred from the circulation line 10 to the circulation line 11, when the chips in the feeder are fed from pipe 2 to pipe 6, are transported through pipe 12 by means of a pump 13 to the suction side on Pump 8 for feeding chips from the feeder to the cooker. This fluid transfer is controlled by the fluid level in the feed hopper 1.
    Chips along with the charging fluid flow through the first grinding zone to the level 14 of the chips column where the loaded chips are packed and fed forward by creating a flow of loading liquid 15 under conditions of turbulent flow through the column of loaded chips in the direction of supply of the named column before than the said fluid is withdrawn from the periphery of the chips





    n te
    chips in the cooking unit-, the cross-section of the flow for
    the feed chips and fluid gradually increase from the feed point to the extraction filter 16 for the feed fluid 15.
    The flow rate of the impregnating liquid 18 through the countercurrent impregnation zone is controlled by changing the amount of liquid extracted from the filter 19.
    Then the selected impregnating fluid is circulated by the pump 20 through the heat exchanger 21 and enters the lower part of the impregnation zone 22. The heat exchanger heats the circulating fluid by means of a heat exchanger with the liquid 23 extracted from the zone of the second continuous treatment with the extracted liquid 24.
    Extractive substances 25 are separated by means of a device from the impregnating liquid 27.
    The impregnated chips and liquid, which is supplied from the impregnation zone to the zone of the second continuous processing (cooking), is heated to the cooking temperature by extracting the cooking liquid 28, heating the cooking liquid 29 and returning it to the inlet 30 of the second treatment zone.
    As the impregnating liquid can be used a mixture of liquid
    column 16 and pass through 35 bones 23 and 27. After the second zone
    cut the pipe 17 using the pump 8 back to the feeder.
    By adjusting the extraction rate through the filter 16 of this liquid, a pressure differential is created to provide a touring mode for the transportation of chips through the impregnation zone. The pressure drop can also be implemented by adjusting the level of chips in the zone of the first direct processing. five
    In this case, a high squeezing and feeding pressure is applied to the column in front of the impregnation zone, which is easily determined and adjusted. In this case, the pressure is evenly distributed over the entire cross section of the chip column and reaches its highest value at the entrance to the impregnation zone. In this case, mechanical deformation of the chips can be eliminated. tc
    In order to obtain a large supply pressure — even with a relatively small flow of feed liquid — and to facilitate the adjustment of the level of the winding treatment, the mass is washed and unloaded.
    The pulp obtained using sulphate cooking liquid at a final temperature of 170 ° C has the main indicators for starting toadina chips 2-6 mm: Permanent number,% 44.2 Yield,% 50.4
    Marriage,%, 0.4
    Viscosity, dm3 / kg 1170 for initial chips 4–10 mm thick Permanganate number,% 43.5 Yield,% 50.3
    Marriage,% 11,1
    Viscosity, dm3 / kg 1170 The proposed method provides the following advantages. All zones are present in one apparatus under pressure with loading from above, while sharp temperature boundaries between zones are maintained. It is possible to maintain high and
    I wash and unload the mass treatment.
    The pulp obtained using sulphate cooking liquid at the final temperature of 170 ° C has the main indicators for the starting chips of toadina 2-6 mm: Permanent number,% 44.2 Yield,% 50.4
    Marriage,%, 0.4
    Viscosity, dm3 / kg 1170 for initial chips 4–10 mm thick: Permanent number,% 43.5 Yield,% 50.3
    Marriage,% 11,1
    Viscosity, dm3 / kg 1170 The proposed method provides the following advantages. All zones are present in one pressurized unit with a top loading, while maintaining sharp temperature boundaries between zones. In the zone of impregnation it is possible to maintain high and

    a constant temperature without such a high rise in temperature so as to induce the onset of lignin dissolution. The energy consumption of the process is low only in heating the chips and the cooking liquid from the impregnation temperature to the cooking temperature. The mechanical deformation of the chips is reduced to a minimum.
    The heat consumption of the proposed method for cooking kraft pulp with traditional cooking parameters is 0.9 GJ / t pulp, and heat consumption under the same cooking conditions, the heat consumption by a known method is 1.8 GJ / ton pulp. .
    Less heat consumption is achieved due to a strong backflow in the counterflow zone, and the movement of chips down through the apparatus is carried out using hydraulic force.
    权利要求:
    Claims (2)
    [1]
    1. A method of continuous cooking of wood chips, including transportation of chips, successively through the zones of the first continuous treatment, countercurrent impregnation and the second continuous treatment of the cooking solution with increasing temperature in each subsequent zone and washing, in order to intensify the process by reducing energy costs, the transportation of chips through the countercurrent impregnation zone is realized in a turbulent mode, which is created by a pressure differential before entering the impregnation zone.
    [2]
    2. Method of claim 1, characterized in that the pressure drop is carried out by controlling the speed of extraction of the cooking liquor from the zone of the first grinding treatment or by adjusting the level of chips in the zone of the first grinding treatment.
    类似技术:
    公开号 | 公开日 | 专利标题
    US3298899A|1967-01-17|Method and arrangement for washing and cooling at the outlet end of a continuous cellulose digester
    US5080755A|1992-01-14|Process for the continuous digestion of cellulosic fiber material
    US4071399A|1978-01-31|Apparatus and method for the displacement impregnation of cellulosic chips material
    US2876098A|1959-03-03|Process of and apparatus for the continuous manufacture of cellulose or hemicellulose from cellulosic fibrous materials
    US3380883A|1968-04-30|Method and apparatus for performing prehydrolysis in a continuous counterflow digester
    US7112256B2|2006-09-26|Method for continuous cooking of chemical pulp to improve heat economy
    EP0477059B1|1995-07-12|Impregnation with black liquor prior to white liquor introduction
    US4123318A|1978-10-31|Three-vessel treatment system
    EP0502852A1|1992-09-16|Displacement heating in continuous digesters.
    JPH08508551A|1996-09-10|Cooking equipment for hardwood
    SU1475491A3|1989-04-23|Wooden chip continuous digestion process
    US6123807A|2000-09-26|Method for the continuous cooking of pulp
    US3427218A|1969-02-11|Method of performing counter-current continuous cellulose digestion
    US5192396A|1993-03-09|Process for the continuous digestion of cellulosic fiber material
    US3224358A|1965-12-21|Apparatus for recovering fermentable liquors
    US5300195A|1994-04-05|Continuous vertical digester apparatus
    US4104113A|1978-08-01|Two-stage digestion with between vessel heating
    FI78745C|1989-09-11|PUMPNING OCH FOERAEDLING AV SAOGSPAON.
    US2999784A|1961-09-12|Process and apparatus for the treatment of fibrous materials in the production of cellulose or semi-cellulose
    US3096234A|1963-07-02|Continuous digesting system
    US3441475A|1969-04-29|Continuous pulping apparatus
    US2789051A|1957-04-16|Method for continuous cooking of chips in the manufacture of pulp
    CN208943485U|2019-06-07|A kind of evaporator applied to DDGS production technology
    US2799579A|1957-07-16|Apparatus for presoaking lignocellulose material
    US2041597A|1936-05-19|Digesting process and apparatus
    同族专利:
    公开号 | 公开日
    JPS59137589A|1984-08-07|
    AU548448B2|1985-12-12|
    FI66215B|1984-05-31|
    FI824282A0|1982-12-14|
    SE8306853L|1984-06-15|
    ZA838909B|1984-07-25|
    JPS6347836B2|1988-09-26|
    FR2537621A1|1984-06-15|
    FI66215C|1984-09-10|
    ATA427983A|1987-05-15|
    AT384631B|1987-12-10|
    SE452175B|1987-11-16|
    AU2184783A|1984-06-21|
    SE452175C|1989-12-21|
    DE3344865A1|1984-06-14|
    NO161927B|1989-07-03|
    SE8306853D0|1983-12-12|
    CA1210907A|1986-09-09|
    NO834466L|1984-06-15|
    DE3344865C2|1985-09-19|
    FR2537621B1|1985-11-22|
    NO161927C|1989-10-11|
    BR8306977A|1984-07-24|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    RU2447216C1|2011-01-17|2012-04-10|Тарантин Сергей Анатольевич|Method of delignification of wood chips in manufacturing of cellulose|FR2001800A1|1968-02-13|1969-10-03|Sunds Ab|
    SE343344B|1970-06-29|1972-03-06|Kamyr Ab|
    CA1002361A|1973-01-03|1976-12-28|James R. Prough|Digester control process and apparatus|
    US4071399A|1976-09-01|1978-01-31|Kamyr, Inc.|Apparatus and method for the displacement impregnation of cellulosic chips material|SE506458C2|1996-02-09|1997-12-15|Kvaerner Pulping Tech|Continuous boiling of cellulosic material with heat exchange between boiler extraction and circulating boiling liquid|
    US5958181A|1997-08-07|1999-09-28|Ahlstrom Machinery, Inc.|Continuous cooking with a two-stage cool impregnation|
    US8852395B2|2011-03-25|2014-10-07|Valmet Ab|Method and arrangement for adding treatment liquors to cellulose material in a down flow vessel|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI824282A|FI66215C|1982-12-14|1982-12-14|SAETTING VIDEO CONTAINER UPPSLUTNING AV FINFOERDELAT CELLULOSAHALTIGT MATERIAL|
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