• 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:
    1517141 Horizontal Hg cathode cell COMMISSARIAT A L'ENERGIE ATOMIQUE 24 Jan 1977 [30 Jan 1976] 02762/77 Heading C7B The cell has a transversely sloping diaphragm 8a, 8b separating upper anode and lower cathode compartments and a plurality of longitudinally inclined, parallel Hg channels 6 in the cathode compartment which are vertically staggered so that a plane passing through their longitudinal midlines is parallel to the diaphragm. The anodes are also parallel to the diaphragm which latter may have a dihedral shape as shown. The transverse slope exceeds the longitudinal slope. A cell length: width ratio of at least 10 is preferred. A ceramic or ion exchange diaphragm is specified. A desired pressure balance across the diaphragm may be achieved by adjustable electrolyte overflows, e.g. vertically movable constant-head type pipes, whose movements may be automated via a flowmeter and inter-connected servo-mechanism. Reduction of U IV to U III (chloride) is exemplified.
    公开号:SU733520A3
    申请号:SU772444454
    申请日:1977-01-28
    公开日:1980-05-05
    发明作者:Илэр Пьер；Лоншамп Жорж
    申请人:Коммисариат А Л,Энержи Атомик (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to electrochemical production, in particular to the construction of electrolytic cells with a mercury cathode.
    A horizontal mercury cathode electrolyzer is known, which has an inclined surface for the flow of mercury and an inclined flat diaphragm 1 that is remote from the anodes.
    The diaphragm is designed to remove gas evolved at the cathode. To remove the gas, it is necessary to inform the diaphragm of a slope of at least 2%, however, such a slope of the surface over which mercury flows leads to a HIGH flow rate of mercury and undesirable mixing of the catholyte, i.e. lower current output during electrolysis.
    Also known is a horizontal mercury cathode electrolyzer containing an inclined surface for the flow of mercury and an inclined flat membrane or diaphragm that is remote from the anodes. The slope of the pore surface for the flow of mercury is made in the form of ledges, while the ledges are arranged with a common slope parallel to the slope of the membrane and anodes 2.
    The transfusion of mercury from the ledge to the ledge leads to the formation of dead zones, causes mixing of the catholyte and, as a result, a decrease in the current output from
    The aim of the invention is to increase the current efficiency by reducing the mixing of the catholyte.
    The goal is achieved by the fact that in a known horizontal electrolyzer inclined surfaces are made in the form of TRAYS parallel to each other with an inclination of 1-1.5%, shifted vertically relative to each other in such a way that the distance between the trays and anodes in the vertical is the same across the width the electrolyzer, in addition, the membrane or diaphragm may be located so that it forms a dihedral angle.
    权利要求:
    Claims (2)
    [1]
    The proposed difference allows the membrane to be given a sufficiently large slope to eliminate the formation of a gas bag under the membrane and at the same time ensure the flow of mercury across the surface with an inclination that ensures a uniform flow. As the mercury flows laminar, it does not cause the mixing of the catholyte moving in parallel. It is recommended to use an electrolyzer, in which the length to width is at least 10, and the inclination of the diaphragm or membrane is at least 2%. When using a membrane, there is no danger of mixing the anolyte with catholyte. When using a diaphra, it becomes necessary to regulate pressure in the anode and cathode spaces using drain pipes. In figures 1 and 2 shows the proposed electrolysis er. The electrolyzer includes case 1 of. corrosion resistant material. The inclined surface is made in the form of trays 2 connected to the current source. Mercury 3 flows through the trays, forming the cathode of the electrolysis. The membrane 4 is made in the form of a dihedral angle for better removal of gases, which are discharged through pipeline 5 and 6. Graphite anodes 7 are located above the membrane and are connected to a current source. Pipeline 8 is designed to remove the anode gas, the anolyte enters the anode space 9 through pipe 10, and exits through pipe 11. The height of the liquid is determined by the drain pipe 11, the catholyte enters the cathode space 12 through pipe 13 and is discharged through the drain pipe 14 in the chamber 15, the latter is communicated by the opening 16 with the cathode space 12. Mercury enters the electrolyzer through pipe 17 and is led out through pipe 18. The emptying of the electrolyzer is carried out by a crane 19.. Example. Electrolyzer used are used to prepare UCI from UCI, j. In the cathode space serves the solution. UCI4 concentration of 1.3 mo / l 1 H-HCI with a speed of 550 l / h. In the anode space serves a solution of HCI with a speed of 2500 l / h. When the current density on the membrane is 0.2 L / cm2, the voltage on the electrolyzer is 5.8 V, current output is 85%. When using the known electrolyzer under similar conditions, the current efficiency is 71%. Thus, the use of the proposed electrolyzer allows to increase the current efficiency. Claim 1. A horizontal mercury cathode electrolyzer containing inclined surfaces for the flow of mercury and an inclined flat membrane or diaphragm distant from the anodes, characterized in that, in order to increase the current efficiency by reducing the mixing of the catholyte, the inclined surfaces are made parallel to each other. to each other trays with a slope of 1-1.5%, shifted vertically relative to each other, and the distance between the tray and the anodes is the same PS along the entire width of the electrolyzer. 2. Electrolyser ps p.1, characterized in that the membrane or diaphragm is made in the form of a dihedral angle. Sources of information taken into account in the examination 1. Germany patent number 933027, cl. 12th 1/12, 15.09.55.
    [2]
    2. German patent W 701771, cl. 12 e 1/12, 01.23.41 (prototype).
    - -five . rh
    类似技术:
    公开号 | 公开日 | 专利标题
    GB1411928A|1975-10-29|Production of hypochlorite by electrolysis of sea water
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    US2468022A|1949-04-26|Electrolytic apparatus for producing magnesium
    US2629688A|1953-02-24|Electrolytic apparatus for production of magnesium
    ES479479A1|1979-07-16|Method for preparing chlorine by electrolysis of hydrochloric acid, and electrolytic cell therefor.
    US3907651A|1975-09-23|Method for the molten salt electrolytic production of metals from metal chlorides and electrolyzer for carrying out the method
    FR2162649B1|1977-01-14|
    US2749301A|1956-06-05|Mercury type, caustic, chlorine cell
    US4048046A|1977-09-13|Electrolytic cell design
    US1126627A|1915-01-26|Process for electrolyzing alkali-chlorid solution.
    SU716525A3|1980-02-15|Vertical mercury cathode electrolyzer
    US2744864A|1956-05-08|Apparatus for the electrolysis of aqueous alkali sulphate solutions
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    US1741290A|1929-12-31|Apparatus for electrolyzing chiefly alkaline chlorides
    US1983296A|1934-12-04|Arrangement in multicell electrolyzers
    US1092369A|1914-04-07|Process of making chlorates and apparatus therefor.
    US3445373A|1969-05-20|Mercury cathode electrolysis cell
    US3445374A|1969-05-20|Alkali chloride electrolytic mercury cells
    SU1708931A1|1992-01-30|Filter-press electrolyzer for obtaining hydrogen and oxygen
    US779383A|1905-01-03|Electrolytic apparatus.
    SU383758A1|1973-05-23|
    JPS5920481A|1984-02-02|Electrolytic cell
    JPS5550476A|1980-04-12|Salt water electrolytic cell for production of sodium hypochlorite
    同族专利:
    公开号 | 公开日
    GB1517141A|1978-07-12|
    SE7700945L|1977-07-31|
    AU2177577A|1978-08-03|
    SE415038B|1980-09-01|
    IT1076326B|1985-04-27|
    FI60244B|1981-08-31|
    DE2703485A1|1977-08-04|
    NL7700897A|1977-08-02|
    MX143040A|1981-02-23|
    NO145987C|1982-07-07|
    LU76657A1|1977-08-03|
    OA05553A|1981-04-30|
    US4101407A|1978-07-18|
    ZA77433B|1978-03-29|
    JPS5828354B2|1983-06-15|
    JPS52113377A|1977-09-22|
    CA1105882A|1981-07-28|
    BE850880A|1977-07-28|
    NO145987B|1982-03-29|
    FI60244C|1981-12-10|
    NZ183193A|1979-06-08|
    FR2339684A1|1977-08-26|
    BR7700557A|1977-10-18|
    ES455761A1|1978-01-01|
    FI770274A|1977-07-31|
    CH617723A5|1980-06-13|
    AU506633B2|1980-01-17|
    AR211563A1|1978-01-30|
    NO770288L|1977-08-02|
    FR2339684B1|1979-01-05|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US646313A|1899-03-18|1900-03-27|John Gustaf Adolf Rhodin|Apparatus for decomposing alkali sulfates.|
    US2230023A|1938-03-09|1941-01-28|American Enka Corp|Electrolytic cell|
    BE478669A|1947-01-10|
    US4002550A|1975-04-15|1977-01-11|Svetoslav Georgievich Smirnov|Electrolyzer for producing and refining metals|EP0077982B1|1981-10-22|1987-04-29|Kanegafuchi Kagaku Kogyo Kabushiki Kaisha|An electrolysis process and electrolytic cell|
    EP0110425A3|1982-12-06|1985-07-31|Kanegafuchi Kagaku Kogyo Kabushiki Kaisha|An electrolytic process of an aqueous alkali metal halide solution and electrolytic cell used therefor|
    JPS59193290A|1983-04-16|1984-11-01|Kanegafuchi Chem Ind Co Ltd|Electrolytic cell|
    JPS6342710B2|1983-09-13|1988-08-25|Kanegafuchi Chemical Ind|
    DE3425862A1|1984-07-13|1986-01-23|Hoechst Ag, 6230 Frankfurt|ELECTROLYSIS CELL WITH HORIZONTALLY ARRANGED ELECTRODES|
    US5258104A|1991-09-03|1993-11-02|Olin Corporation|Direct electrochemical reduction of catholyte at a liquid metal cathode|
    US5186804A|1991-09-05|1993-02-16|Olin Corporation|Liquid metal cathode electrochemical cell|
    US5185069A|1991-10-15|1993-02-09|Olin Corporation|Liquid metal cathode electrochemical cell and cathode frame|
    US5209836A|1991-12-19|1993-05-11|Olin Corporation|Baseplate for electrolytic cell with a liquid metal cathode|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FR7603015A|FR2339684B1|1976-01-30|1976-01-30|
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