• 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:
    A method and apparatus in which the effects in multiple effect evaporation systems are separated into successive stages and the vapors in the stages of one effect are utilized as a heat source for the liquid in stages of a subsequent effect.
    公开号:SU1181520A3
    申请号:SU772451151
    申请日:1977-02-04
    公开日:1985-09-23
    发明作者:Огава Синсаку
    申请人:Асахи Касеи Когио Кабусики Кайся (Фирма)；
    IPC主号:
    专利说明:

    2. The method according to 1H and and so
    in it, the steps of the second building are heated by the secondary steam of the first step of the first building.
    The not steps are heated with a mixture of secondary vapors of all the steps of the first corps of Section 1, which distinguishes the liquid of the last 11,81520. 3. The method according to claim 1, is also distinguished by the fact that the liquid follows
    The invention relates to methods for concentrating liquids in multistage evaporators using secondary vapors from the first stages to heat the evaporated liquid from the subsequent stages of the evaporator. The purpose of the invention is to increase the efficiency of the process by maintaining the optimum temperature difference between the steps. The drawing shows a two-stage two-package evaporation plant, in which the proposed method of liquid concentration can be implemented. This principle can be used in installations with many stunty and buildings. The installation contains two-stage inflators 1 and 2. Stages 3-6 of the apparatus are separated from one another by walls 7 and 8. Each stage is equipped with a heater 9 12 for heating the fluid to be scalded. The coolant enters through pipelines 13 and 14, and the liquid flows through pipe 15 and circulates through pipe 16 and is discharged through pipe 17. Steam pipelines 20 and 21 are provided for supplying secondary steam from one stage to another. The liquid flows from the previous stage to the next through pipelines 22 and 23, and the condensate is discharged through pipe 21. When the process is discontinued, the liquid subjected to concentration enters the installation through the pipeline. 15 and passes sequentially through the installation steps. The steam, formed in stage 3, is used to heat the liquid in stage 6 of apparatus 2 and is supplied via steam line 19 to heater 12. Thus, in the installation there is a double-case recharge. Condensate formed in heaters 11 and 12 is removed from the installation through conduit 24. The vapors formed in steps 3 and 4 are removed from the installation through conduits 20 and 21. These vapors can be used as heat transfer fluid in other installation housings. Pressure The vapors from the solution in the first stage of the first hull are SAMEL high, since the solution in this stage is the least concentrated, and vice versa the concentration in the most recent stage is the highest. The result is that the temperature difference between the temperature of the liquid in the first stage of the first body and the last stage of the second body can be made large. Therefore, it is possible to reduce the heat transfer surface for the entire installation or to obtain a more concentrated solution. With the implementation of the method, the temperature of the liquid subjected to the concentration of YOD and the vapor decreases as they pass through a series of successive stages in the first building. These parameters increase as they pass through a series of successive stages in the second building. The system is designed so that the vapors from the first stage of the first building are used to heat the solution in the last stage of the second building, and thus the maximum efficiency is achieved.
    The efficiency of the method can be increased by adding a third body with multiple stages or steps. A characteristic advantage of the proposed method is that the high-temperature liquid can be used as a coolant without the characteristic drawbacks of a large temperature difference, usually associated with such a coolant.
    The proposed method can be implemented in installations with a standard type of apparatus (multi-stage evaporator, multi-unit evaporator, single-unit evaporator, etc.). Heaters 9-12 can use any heating system (natural or forced circulation or falling film).
    The proposed method is suitable for working with high boiling liquids due to the fact that
    15204
    the difference between the steps can be significantly increased and the method can be successfully used to concentrate aqueous solutions of soda, 5 potash liquor, sugar solutions and the like.
    The vapors from the latter can, for example, be cooled using conventional OX means: averages (for example, a cooling zod, barometric cooler, surface cooler, etc.). Pairs can be cooled either sequentially (in stages) or in parallel.
    The proposed method is also characterized by using the calorific value of the vapor coming from a stage characterized by a higher vapor pressure of one body to heat the liquid in another stage of the next one along the body. Furthermore, it is possible to connect pairs of adjacent stages in one body to heat one stage in the subsequent case.
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    权利要求:
    Claims (3)
    [1]
    1. METHOD OF CONCENTRATION
    LIQUIDS IN MULTI-HOUSING STEAM
    INSTALLATION, each case of which is divided into several stages, namely, that concentrated liquid is supplied sequentially through all stages, while the liquid is heated in the steps of each subsequent case by secondary steam generated in each stage of the previous case, characterized in that, in order to increase the efficiency of the process by maintaining the optimum temperature difference between the stages, the liquid of each subsequent stage of the second body is heated by secondary vapors of higher § high pressure than Fluid previous steps.
    Q
    1 181521 '
    [2]
    2. The method according to π. 1, characterized in that the liquid of the last stage of the second body is heated by the secondary steam of the first stage of the first body.
    [3]
    3. The method according to p. 1, characterized in that the liquid of the last stage is heated with a mixture of secondary vapors of all stages of the primary housing.
    类似技术:
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    US3261766A|1966-07-19|Multistage evaporation with absorption of distilled vapors
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    US4348261A|1982-09-07|Method for distilling a liquid
    US3783095A|1974-01-01|Process for recovering turpentine and heat in connection with the evaporation of black lye
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    SE8302881L|1983-11-29|VERMEATERVINNINGSFORFARANDE
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    CN108383189B|2021-05-11|High-temperature saline water self-heating concentration and fresh water separation system
    US4413669A|1983-11-08|Method of heat extraction from an aqueous carrier medium
    同族专利:
    公开号 | 公开日
    FR2340120A1|1977-09-02|
    NL168709C|1982-05-17|
    IT1076958B|1985-04-27|
    CA1054921A|1979-05-22|
    SE7701190L|1977-08-07|
    JPS5294874A|1977-08-09|
    NL7701143A|1977-08-09|
    NL168709B|1981-12-16|
    BR7700673A|1977-12-06|
    GB1576432A|1980-10-08|
    JPS5526882B2|1980-07-16|
    FR2340120B1|1982-10-22|
    DE2703429A1|1977-08-11|
    US4132588A|1979-01-02|
    DE2703429C2|1983-01-27|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    NO119205B|1965-08-19|1970-04-06|Rosenblads Patenter Ab|
    SE365008B|1971-11-19|1974-03-11|Mo Och Domsjoe Ab|
    JPS5436915B2|1974-05-31|1979-11-12|SE410822B|1977-09-12|1979-11-12|Saari Risto|PROCEDURE FOR DISTILLATION OF VETSKOR AND FACILITY FOR IMPLEMENTING THE PROCEDURE|
    WO1986000876A1|1985-04-18|1986-02-13|Sulzer-Escher Wyss Ag|Method and apparatus for preparing high-concentration alkali|
    FR2581982A1|1985-05-15|1986-11-21|Solvay|Process and plant for the concentration of aqueous alkali metal hydroxide solutions|
    EP1555243A1|2004-01-19|2005-07-20|GEA Messo AG|Process for treating an aqueous solution, particularly a caustic soda solution using multi-step evaporation|
    US7785744B2|2005-09-28|2010-08-31|Bloom Energy Corporation|Fuel cell water purification system and method|
    US8317994B2|2008-08-07|2012-11-27|Westlake Vinyl Corporation|Method of concentrating an aqueous caustic alkali using a catholyte heat recovery evaporator|
    DE102011108211A1|2011-07-21|2013-01-24|Thyssenkrupp Uhde Gmbh|A process for concentrating aqueous liquor and apparatus therefor|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP1123176A|JPS5526882B2|1976-02-06|1976-02-06|
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