• 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:
    1480428 Degassing liquid R SAARI 23 Oct 1974 [29 Oct 1973] 46471/74 Heading B1M Removal of gas dissolved in liquid is effected by lowering the liquid pressure so that the entrained gas forms bubbles, collecting the gas from the bubbles in a chamber 22, and reintroducing at 23 the gas as further bubbles to the liquid as it descends to a tank 26, the further bubbles having insufficient time to redissolve before escaping from the liquid in the tank 26. The pressure is lowered by increasing the flow velocity or hydrostatic head of the liquid. As shown the pressure of the liquid is lowered as it ascends to the chamber 22 during siphoning from a tank 20 to the tank 26. An ejector 23 through which the descending liquid flows at a velocity of 0.5 to 1.0 m/s is used to re-introduce the gas into the liquid. A form of ejector is shown in Fig. 3 and comprises a pipe 36 through which the descending liquid flows thereby to draw in the collected gas through a pipe 35. The above sequence of operations may be repeated in apparatus 27-31 in which the liquid siphons from the tank 26 to a tank 32. The upward flow of liquid may be produced by a pump instead of by siphoning. The tanks 26, 32 may be closed, the gas liberated therein then being withdrawn by suction. A vacuum distillation plant supplied with feed water de-aerated as above is described.
    公开号:SU940632A3
    申请号:SU742452650
    申请日:1974-10-29
    公开日:1982-06-30
    发明作者:Саари Ристо
    申请人:За витель；
    IPC主号:
    专利说明:

    The invention relates to methods for removing gases dissolved in it from a liquid.
    The closest in technical essence and the achieved result 5 to the proposed one is a method of multi-stage removal of gas from a liquid, including reducing the pressure by creating a difference in the hydrostatic levels of the mixture and degassed · 10 liquid and feeding the mixture into the rarefaction zone [1].
    The disadvantages of this method are the low productivity of the process t5 , low efficiency and reliability of the known method of degassing a liquid.
    The purpose of the invention is to increase efficiency and reliability.
    This goal is achieved by the fact that in the method of removing gases dissolved in it from a liquid, the gas released in the rarefaction zone is mixed with the liquid and fed to the separation at a final pressure that is higher than the pressure to the rarefaction zone.
    Moreover, the gas is cooled before mixing with the liquid.
    In addition, the final pressure in each subsequent stage is maintained above the pressure in the previous stage.
    In FIG. 1 is a diagram of the implementation of the proposed method, where the gases from the liquid are removed in several stages; in FIG. 2 is a diagram of an ejector of simple construction; in FIG. 3 ~ technological scheme of the vacuum distillation unit.
    According to FIG. Figure 1 includes tanks A and B, the difference between the liquid levels in which db.
    The size of the bubbles can be increased in that they are allowed to rise from the liquid into the gas phase of the containers 13 into which the liquid rises (respectively, through pipes 4-6. Gases from containers 1-3 are taken through pipes 7 * 9 into the 10-Ί2 ejectors and into in the form of bubbles are mixed with a falling liquid and sent through pipes ΟΙ 5 to the lower part of the tanks 16, 17, B.
    According to FIG. 3 installation includes 5 heat exchanger 18, pipelines 19'21, ejectors 22, distillation apparatus 23.
    The method is as follows.
    The gases dissolved in the liquid 10 are separated in vacuo, obtainable by hydrostatic pressure and vacuum are removed from this by mixing them in the form of bubbles with the descending liquid flow 15 Ko tory transports them to a higher pressure.
    The liquid heated in the heat exchanger 18 goes to the vacuum processing stage, and from there through the pipe 21 it enters 20 into the evaporators of the distillation apparatus 23, the gases separated at the gas removal stage are sent from the intermediate tanks through the pipe 19 to the liquid passing through the pipe 20, and mixed stitch with this liquid in the form of bubbles in the ejector 22.
    Thus, the gases dissolved in the distilled liquid are separated and pumped into the intermediate pressure region with the help of the liquid from which they are separated.
    The proposed method can significantly improve the reliability and efficiency of the process of separating gas from liquid.
    权利要求:
    Claims (2)
    [1]
    (5) METHOD FOR REMOVING FROM A LIQUID OF GAS DISSOLVED IN IT The invention relates to methods for the removal of gases dissolved in a liquid from a liquid. The closest in technical essence and the achieved result to the proposed is a method of multi-stage gas removal from a liquid, including pressure reduction by creating a difference of hydrostatic levels of the mixture and degassed liquid and supplying the mixture to the rarefaction zone 1. The disadvantages of this method are insignificant process performance, low efficiency and reliability of the known method of fluid degassing. The purpose of the invention is to increase efficiency and reliability. This goal is achieved by the fact that in the method of removing gases dissolved in a liquid from a liquid, the gas released in the dilution zone is mixed with the liquid and fed to the separation at a final pressure that is higher than the pressure to the rarefaction zone. Moreover, the gas is cooled before mixing with the liquid. In addition, the final pressure in each subsequent stage is maintained above the pressure in the previous stage. FIG. 1 is a flow chart of the proposed method, where gases from the liquid are removed in several stages; in fig. 2 - diagram of the ejector of a simple construction; in fig. 3 technological scheme of the vacuum distillation unit. According to FIG. Figure 1 includes tanks A and B, the difference between the fluid levels in which dB. The size of the bubbles can be increased by allowing them to rise from the liquid to the gas phase of the tanks 13, into which the liquid rises, respectively, through pipes 4-6. Gases from tanks 1-3 are taken through pipes into ejectors 10-12 and in the form of 3 bubbles are mixed with descending liquid and sent through pipes 15 to the lower part of tanks 16, 17, B. As shown in FIG. 3 installation includes 5 heat exchanger 18, pipelines, ejectors 22, distillation unit 23, The method is as follows. Gases dissolved in a liquid are separated under a vacuum obtained by a hydrostatic head and removed from this vacuum by mixing them in the form of bubbles with a descending stream of liquid that transports them to a higher pressure area. When heated in the heat exchanger 18, the liquid goes to the vacuum processing stage, and from there through the pipe 21 enters the 20 evaporators of the distillation unit 23, the gases separated in the gas removal stage are transferred from the intermediate tanks through the pipe 19 to the liquid passing through the pipe 20 and mixed - 5 are sutured with this liquid in the form of bubbles in the ejector 22. Thus, the gases dissolved in the distilled liquid are separated and pumped into the intermediate-zonal pressure region using a liquid from which they are separated. 4 The proposed method allows to significantly increase the reliability and efficiency of the process of separation of gas from liquid. Claim 1. A method of removing gases dissolved in a liquid from a liquid, including reducing the pressure by creating a difference in the hydrostatic levels of the mixture and the degassed liquid and feeding the mixture into the dilution zone, so that, in order to increase its efficiency and reliability, the selected in the zone-thinned gas, the gas is mixed with the liquid and fed to the separation at a final pressure that is higher than the pressure to the vacuum zone.
    [2]
    2. Method pop.1, distinguished by the fact that the gas is cooled before mixing with a liquid, 3- The method according to claim 1, is distinguished by the fact that the final pressure in each subsequent stage is maintained above the pressure in the preceding steps Sources of information taken into account in the examination 1. US patent No. 2966230, cl. 55-193, 19bO (prototype).
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    类似技术:
    公开号 | 公开日 | 专利标题
    SU940632A3|1982-06-30|Method for removing dissolved gases from liquid
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    同族专利:
    公开号 | 公开日
    FI50208C|1976-01-12|
    JPS5831480B2|1983-07-06|
    DE2451110C2|1985-11-21|
    ES431426A1|1976-10-16|
    FR2323905B1|1980-03-28|
    NL177387C|1985-09-16|
    US4002440A|1977-01-11|
    FR2323905A1|1977-04-08|
    JPS5074220A|1975-06-18|
    AT334505B|1976-01-25|
    SE407610B|1979-04-02|
    SE7413595L|1975-04-30|
    NL7413800A|1975-05-02|
    FI50208B|1975-09-30|
    ATA859674A|1976-05-15|
    NL177387B|1985-04-16|
    CA1033332A|1978-06-20|
    IT1025254B|1978-08-10|
    DE2451110A1|1975-09-04|
    GB1480428A|1977-07-20|
    FI334773A|1975-04-30|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE4225221A1|1992-07-30|1994-02-03|Siemens Ag|X=ray unit operation method - has circulating pump for fluid in housing with periodical gas extraction|US885301A|1904-08-27|1908-04-21|Johann Wilhelm Siepermann|Air-pump.|
    US1077771A|1911-05-03|1913-11-04|George Ellis Waggoner|Means for controlling fumes or smoke.|
    US1401101A|1920-06-05|1921-12-20|Elliott Co|System for removing air and gases from water|
    US2006985A|1926-03-13|1935-07-02|Claude George|Method and apparatus for obtaining power from sea water|
    FR924343A|1946-03-22|1947-08-01|Hydrodynamic compressor|
    US3154087A|1961-12-26|1964-10-27|Quadrant Engineering Corp|Means and method for purging a hydraulic system|
    DE1898279U|1962-03-30|1964-08-06|Agfa Ag|SUCTION LIFTS, IN PARTICULAR FOR SEWAGE DETOXIFICATION SYSTEMS|
    US3344584A|1964-07-29|1967-10-03|Saline Water Conversion Corp|Method and apparatus for degassing and distilling liquid|
    US3358425A|1966-06-14|1967-12-19|Sr Gerald E Burnham|Degassing apparatus|
    US3486297A|1967-10-06|1969-12-30|Exxon Production Research Co|Liquid and gas pumping unit|
    US3778969A|1972-04-12|1973-12-18|Chicago Bridge & Iron Co|Ejector vapor recovery system for stored volatile liquids|GB1603299A|1977-05-19|1981-11-25|Water Res Centre|Process and apparatus for the aerobic biological treatment of waste water|
    US4483826A|1980-08-12|1984-11-20|Phillips Petroleum Company|Combination reaction vessel and aspirator-mixer|
    JPS5814905A|1981-07-17|1983-01-28|Toray Ind Inc|Separation apparatus by reverse osmosis|
    JPS601485A|1983-06-16|1985-01-07|Mitsubishi Electric Corp|Electromagnetic valve for control of refrigerant flow|
    DE3428540C2|1984-08-02|1990-09-20|Helmut E. Prof. Dr.-Ing. 1000 Berlin De Siekmann|
    DE3428534C2|1984-08-02|1988-09-22|Uhde Gmbh, 4600 Dortmund, De|
    US5056323A|1990-06-26|1991-10-15|Natural Energy Systems|Hydrocarbon refrigeration system and method|
    DE4328424A1|1993-08-24|1995-03-02|Basf Ag|Distillation column for separating a liquid mixture into several pure fractions|
    AT190236T|1994-11-09|2000-03-15|Andrzej Golcz|METHOD AND DEVICE FOR GASIFIED SLUDGE|
    EP1074708A1|1999-06-25|2001-02-07|ABB Alstom PowerAG|Gas-liquid separating apparatus|
    NO20033331D0|2003-07-24|2003-07-24|Knutsen Oas Shipping As|Method and apparatus for removing gases from water|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI733347A|FI50208C|1973-10-29|1973-10-29|Process for removing gases dissolved in liquid from the liquid|
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