• 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:
    An electrolytic cell of the filter-press type which comprises plate-like anodes (57,58), cathodes (51,52), and gaskets (53,54,55,56) of an electrically-insulating material, and an ion-exchange membrane (63,64,65) between each anode and adjacent cathode to form in the cell a plurality of anode compartments and cathode compartments, the gaskets (53,54,55,56), and optionally the anodes (57,58) and cathodes (51,52), each containing apertures therein which form headers from which liquors may be charged to the anode and cathode compartments of the cell and to which products of electrolysis may be removed from the anode and cathode compartments of the cell, and in which the gaskets (53,54,55,56), and optionally the anodes (57,58) and cathodes (51,52), each comprise an aperture therein which together form a compartment lengthwise of the cell which is in communication only with the anode compartments of the cell, or which is in communication only with the cathode compartments of the cell, and which serves as a balancing header.
    公开号:SU1662353A3
    申请号:SU864028441
    申请日:1986-10-21
    公开日:1991-07-07
    发明作者:Ричард Джеймс Стефен
    申请人:Империал Кемикал Индастриз Плс (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to electrochemical technology, in particular, to the construction of an electrolyzer designed to produce chlorine and alkali metal hydroxide by electrolysis of an aqueous solution of alkali metal chloride.
    The purpose of the invention is to increase the current output of the product due to the uniform distribution of electrolyte in the cells in both the anode and cathode groups of cells.
    Figure 1 shows the anode, the vertical section in figure 2 is the cathode, the vertical section J in figure 3 is the gasket plate, the vertical section; Fig. 4 shows a portion of an electrolytic cell including an anode, a cathode and gasket plates.
    The anode consists of a plate 1, having a central hole 2, which is blocked by a large number of vertically arranged strips 3 forming the active anode surface. The strips 3 lie in a plane parallel to the plane of the plate 1. A group of strips is located on each side of the plate 1. The plate 1 itself has four holes 4-7, which, within the electrolytic cell, form some part of the individual stretch dahs in the longitudinal direction of the collectors used for supplying electrolyte to the anode spaces and for removing the final electrolysis products from the anode spaces, for supplying fluid to the cathode spaces and for removing
    HS
    coke
    with

    s
    nor the final electrolysis products from the cathode spaces. The anode plate 1 also has two additional holes 8 and 9 which, within the electrolytic cell, form some part of the chambers extending in the longitudinal direction relative to the cell itself and which in this case perform the function of balancing collectors. The hole (8 is connected through channel 10, which is formed in the wall of the anode plate 1, with the central hole 2, and therefore also with the anode spaces of the electrolytic cell. The hole 9 does not connect with the same channel 11 and does not communicate with the central hole 2 and with the anode space of the cell. The anode plate 1 is also provided with a channel 12 and a protrusion 13, which is connected to the conductor 14 for subsequent connection to the electrical bus.
    The cathode (Fig. 2) is represented by a plate 15, provided with a central opening 16, which overlaps with a large number of vertically arranged strips 17 forming the active cathode surface. The strips 17 lie in a plane parallel to the plane of the plate 15. The latter has four holes 18-21, which together within the electrolytic cell together form some part of individual longitudinally extending collectors, by means of which liquid is supplied to the cathode spaces and the final electrolysis products removed from the cathode spaces; the electrolyte is supplied to the anode spaces, and the final electrolysis products are removed from the anode spaces. The cathode plate 15 has two additional openings 22 and 23 which, within the electrolytic cell, form some part of the chambers extending in the longitudinal direction of the electrolytic cell and which serves in this case as balancing collectors. The hole 23 through the channel 24, located in the wall of the cathode plate 15, communicates with the central hole 16, and hence with the cathode space of the cell. Hole 22 is not connected to said channel, and therefore,
    five
    0
    five
    0
    does not communicate with the central hole 16 and with the cathode spaces of the electrolytic cell. The cathode plate 15 also provides a channel
    25 which connects the opening 18 to the central opening 16 and the channel
    26, which connects the central hole 16 to the hole 19. The cathode plate 15 is also provided with a protrusion
    27, which is connected to conductor 28 to provide subsequent connection to the electrical bus.
    The gasket 29 of electrically insulating material (Fig. 3) has a central opening 30, which corresponds to a central opening 2 in the anode plate 1, and openings 31-36, which correspond to the openings 4-9 of the anode plate 1, but are slightly smaller than the similar ones holes in the anode plate 1. The holes 31-36 located in the gasket 29 include peripheral protrusions (not shown) which enter the holes 4-9 of the anode plate 1 or the holes 18-23 of the cathode plate 15 in the fully assembled electrolytic cell, and Depending on the specific circumstances, these protrusions may form the surface of an electrically insulating material in the openings of the anode plate 1 and the cathode plate 15.
    0
    five
    0
    five
    A part of the electrolytic cell (FIG. 4) consists of two cathodes 37 and 38, each of which has two gaskets 39, 40 and 41, 42 of elastomer material mounted on one of the sides of the cathode. In addition, a portion of the electrolytic cell also includes two anodes 43 and 44, each of which has two spacers 45, 46 and 47, 48 of elastomeric material, which are located on either side of the anode. Ion exchange membranes 49-51 are installed between each anode and the adjacent cathode. Membranes 49 and 50 form the boundaries of the anode space, and membranes 50 and 51 form the boundaries of the cathode space. The electrolytic cell is also provided with end plates (not shown) and a device (not shown) for loading or introducing fluids into the collectors and for removing the final electrolysis products from the collectors.
    The cell operates as follows
    in a way.
    i
    The electrolyte, for example an aqueous solution of alkali metal chloride, is supplied to a collector, the opening of which is located in the anode plate 1. The electrolyte passes through channel 11 and enters the anode space of the electrolytic cell, the opening 2 of which is located in the anode plate 1. Gaseous or liquid end products electrolysis exit from the anode space through the channel 12 and enter the collector, the opening 5 of which forms some part of the collectors, and exit from the electrolytic cell.
    A liquid, such as water or a dilute solution of an alkali metal hydroxide, is supplied to a collector, the opening 18 of which is located in the cathode plate 15. The liquid passes through the channel 25 and enters the cathode space of the cell, the opening 16 of which is located in the cathode plate 15. Gaseous or liquid end products The electrolysis leaves the cathode space through channel 26 and enters the collector, the opening 19 of which forms some part of the collectors and, therefore, leaves the electrolytic cell.
    Electrolytic in operation
    20
    25
    thirty
    the cathode space of the electrolytic cell will achieve uniform distribution of the fluid and maintain a constant pressure.
    It is necessary that the collectors that will communicate with the anode spaces of the electrolytic cell be electrically isolated from the collectors that will communicate with the cathode spaces of the same electrolytic cell. The necessary electrical insulation can be achieved by using frame-shaped elements of electrically insulating material, which should be installed in holes located in the anodes and cathodes and together form some part of the collectors. Frame-shaped elements may form some part of the gaskets, for example, a vertically standing frame-like part on the surface of the gasket.
    The presence of balancing reservoirs in the electrolyzer allows for an increase in the current efficiency, in particular when producing sodium hydroxide, by 1-2% compared with the known electrolyzer.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    Filterpress type electrolyzer for sodium hydroxide, including cell balancing collector, 5 alternating anode, cathode
    0
    five
    0
    the cathode space of the electrolytic cell will achieve uniform distribution of the fluid and maintain a constant pressure.
    It is necessary that the collectors that will communicate with the anode spaces of the electrolytic cell be electrically isolated from the collectors that will communicate with the cathode spaces of the same electrolytic cell. The necessary electrical insulation can be achieved by using frame-shaped elements of electrically insulating material, which should be installed in holes located in the anodes and cathodes and together form some part of the collectors. Frame-shaped elements may form some part of the gaskets, for example, a vertically standing frame-like part on the surface of the gasket.
    The presence of balancing reservoirs in the electrolyzer allows for an increase in the current efficiency, in particular when producing sodium hydroxide, by 1-2% compared with the known electrolyzer.
    Invention Formula
    A filterpress type electrolyzer for sodium hydroxide, including alternating anodic, cathodic
    The opening 8 of which is located in the anode plate 1 communicates with each of the anode spaces of the cell through the channels 10 located in the anode plate 1, so that the electrolyte flow freely passes between the anode spaces and ensures that uniform distribution is achieved in each anode space of the electrolytic cell. electrolyte and maintain constant pressure. The balancing collector, the opening 23 of which is located in the cathode plate 15, communicates with each cathode space of the electrolytic cell through the channels 24, located in the kaad and cathode plate 15, whereby the flow of fluid passes between the cathode spaces and ensures that
    0
    five
    0
    five
    and electroconductive gasket plates and ion exchange membranes placed between the anode and cathode plates to form anode and cathode chambers, with holes in the anode, cathode and gasket plates that form during assembly longitudinal electrically isolated channels communicated with the anode or cathode chambers to be fed into electrolyte and removal of electrolysis products, which is so that, in order to increase the current output of the product, in the anode, cathode and gasket plates are made additionally openings forming in the assembly of longitudinal electrically isolated channels, each communicated only with the anode or cathode chambers only from below the level of electrolyte therein.
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    Compiled by T.Gumenyuk Editor N.Tupitsa Tehred M. Morgantal
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    GB1595183A|1977-03-04|1981-08-12|Ici Ltd|Diaphragm cell|
    DE2821980C2|1978-05-19|1982-03-25|Hooker Chemicals & Plastics Corp., 14302 Niagara Falls, N.Y.|Electrolyte distribution device for electrolysis cells arranged like a filter press|
    EP0045148B1|1980-07-30|1985-05-08|Imperial Chemical Industries Plc|Electrode for use in electrolytic cell|
    US4371433A|1980-10-14|1983-02-01|General Electric Company|Apparatus for reduction of shunt current in bipolar electrochemical cell assemblies|
    US4605482A|1981-04-28|1986-08-12|Asahi Glass Company, Ltd.|Filter press type electrolytic cell|
    DE3130806A1|1981-08-04|1983-03-03|Uhde Gmbh, 4600 Dortmund|MONOPOLAR ELECTROLYTIC FILTER PRESS CELL|
    AT15818T|1981-11-24|1985-10-15|Ici Plc|ELECTROLYTIC FILTER PRESS CELL.|
    US4589968A|1983-03-21|1986-05-20|Reilly Tar & Chemical Corp.|Filter press electrochemical cell with improved fluid distribution system|
    GB8308187D0|1983-03-24|1983-05-05|Ici Plc|Electrolytic cell|
    GB8330322D0|1983-11-14|1983-12-21|Ici Plc|Electrolysis aqueous alkali metal chloride solution|GB8626629D0|1986-11-07|1986-12-10|Ici Plc|Electrolytic cell|
    US5322604A|1992-11-02|1994-06-21|Olin Corporation|Electrolytic cell and electrodes therefor|
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    法律状态:
    2007-09-20| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: MM4A Effective date: 20051022 |
    优先权:
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