• 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 fluidized bed reactor containing a heat exchange apparatus for conveying a heat transfer medium comprising at least one pipe which extends in a vertical direction from the top of the reaction chamber into the fluidized bed with one end of the vertical pipe which points in the direction of the gas flow having a conical tapered end and/or a jacket on the outside of the reactor wall in the form of a serpentine conduit having a rectangular cross section and a domed cover.
    公开号:SU990071A3
    申请号:SU782561452
    申请日:1978-01-05
    公开日:1983-01-15
    发明作者:Ганзауге Йост；Муши Йоханн；Фройдльшпергер Ханс
    申请人:Вакер-Хеми Гмбх (Фирма)；
    IPC主号:
    专利说明:

    one
    The invention relates to the design of a fluidized bed reactor and can be used to conduct exothermic reactions 5 in a gas-solid system.
    A fluidized bed or fluidized bed reactor for exothermic reactions in a gas-solid system is known, for example, to obtain silicon-halogen compounds by means of silicon-containing contact masses by direct synthesis. The known fluidized bed apparatus comprises a housing inside which heat exchange tubes are located, interconnected by means of a bridge 1.
    The disadvantage of the known reactor is the danger of erosion, which 20 is further increased when using solid particles with a strongly abrasive nature, as contact-containing silicon.
    The purpose of the invention is to increase the reliability of the reactor operation.
    The goal is achieved by the fact that in a fluidized bed reactor for the implementation of ec-jq
    Zoteric reactions — in a gas-solid system, for example, to obtain silicon halide compounds using silicon containing 1X contact masses, containing a housing inside which heat exchange tubes are located, interconnected by means of a bridge;
    In addition, the reactor is equipped with a jacket, made in the form of a spiral. with a lid, the lid is made concave or convex, and the spiral channel has the shape of a quadrilateral.
    The proposed heat exchanging device may consist either of only one pipe of the specified arrangement and clearance in the solution volume, or only of the jacket of the specified clearance on the outer side of the reactor walls, with a combination of at least one pipe and a jacket being preferred.
    权利要求:
    Claims (5)
    [1]
    The tip of the tube or pipes, preferably inside, is not designed as a tube, but from a compact or mass material so that it is not bound to a heat exchange medium. The tapering tip has a rounding outside, and it can be designed either as a truncated cone or as a hemispherical shape. A fluidized bed contact with a part creates minimal (slight i resistance to the gas flow directed towards and thus the pipe is actively protected against excessive wear.; If the heat exchanger is made up of several pipes, they are connected to each other bridges located between the tips, for which a slight resistance is also important in relation to the gas flow directed towards you. Therefore, these bridges are made in the form of perpendicular (vertically in the reactor volume plates, narrow, the sides of which are connected with conically narrowed parts, for which the vertically arranged flat material, which is narrowly welded transversely with the tips, is especially suitable. The pipes themselves are submersible, through heat exchanging medium with a variable flow direction. The thickness of the pipes, which is called their outer diameter, the number of pipes and the distance between the individual pipes, depends on the diameter of the reactor and is required for obsessed cooling surface reactor. The drawing standing from the rounded tips of the pipes to the blown bottom represents a randomly selected height. a mask that depends only on the cooling surface of the reactor contents. The spiral-running channel is formed by metal stripes spiral-shapedly welded along the longitudinal edge onto the walls of the reactor, at the expense of which the tetragonal cross-section is obtained, and is embedded on the outside by convex metal stripes. The length of the channel edges in this case is determined by the width and distance of the metal strips from each other on the walls of the reactor. It is preferable to weld the metal strips along the longitudinal crawd vertically onto the walls of the reactor. Outside, the channel is closed by a welded metal lid in the form of a strip with a convex concave or grooved different deflection. Thus, in the described construction, it is completely rational to have high stresses in the material, so that the channels, regardless of the type of heat exchanging medium used and the loads due to pressure and flow resistance, are more satisfied with the requirements for material loads than known with external non-convex coating. In addition, the proposed combination also eliminates the high shrinkage stresses caused by welding (when welding corners with folds, on which the material is subjected to severe deformation). Compared with the known welded semi-tubes with a semicircle cross-section, the proposed combination can be made in any size. All the heat transfer part is located in the walls of the reactor for heat transfer, while in the case of the welded pipes, it is. . The semi-tubular reactor surface relative to the heat-induced medium is smaller than the part of the reactor walls that is included in the thermal domain. FIG. 1 shows a fluidized bed (reactor) and a device for supplying a heat exchange medium, a longitudinal section; in FIG. 2, node 1 in FIG. one ; in fig. 3 is a section A-A in FIG. 2; in fig. 4 — node II in FIG. one ; in fig. 5 is a section BB in FIG. 1. A fluidized bed reactor encloses body 1 q with inlets 2, outlet 3 for solids, input 4 and outlet 5 for gas and purged bottom 6 for gas distribution, register tubes 7 immersed vertically from above into the fluidized bed located in the reactor and at the ends directed towards the flow of gas entering through the purged bottom b, are externally made in the form of rounded tips 8, which are connected to bridges 9. Inside the pipes 6 there are placed immersion pipes 10 to ensure a given heat flux. Shirt 11, which covers the entire outer surface of the walls of the reactor, inside of which there is a fluidized bed, has the form of a spiral-shaped channel in the form of transverse sections located one above the other. Outside rounded tips 8 consist of solid material. The heat exchange medium is supplied through the immersion pipe 10, which is centered due to the direction of the cam 12. The bridge 9 consists of a vertically flat material that is welded to the tips 8 on the side along the narrow sides. material (metal), welded along the longitudinal edge vertically on the walls of the reactor. The channel has a rectangular transverse section and is covered with a lid in the form of welded strips 14 of the sheet material (metal with a convex curvature). The reactor operates as follows: Heat exchanging medium (flow; supplied from the heating system or turnaround water supply system through the pipe. 16 the jacket 11 of the fluidized bed reactor, then through the pipeline 17 into the pipes of the register of pipes 7. The output pipes of the register are connected to flow indicators 18 and 19, thanks to which a uniform load is established from The pipeline sections 20 are transferred to system 15. The heat exchange medium is returned to system 15. With the help of the proposed heat exchanging fluidized-bed reactor equipment, especially heat exchange surfaces of any size can be made available, especially the pipes located in the reactor volume are slightly subject to erosion due to the strong movement of the bed, and the jacket on the inside is smooth and on the outside of the walls of the reactor is stressless in the mother le. The choice of dimensions of heat exchange surfaces is therefore not limited to tube wear in the reactor volume and the material load of the jacket, so that the capacity of the fluidized bed reactor increases significantly. Claims. 1. Fluidized bed reactor for carrying out exothermic reactions in a gas-solid system, for example, for obtaining halogen compounds with silicon-containing contact masses, comprising a housing inside which are heated pipes connected between the bridge, with a bridge. that, in order to increase the reliability of the reactor operation, each Heat Exchanger tube is provided with a tapering tip at the bottom.
    [2]
    2. The reactor according to claim 1, characterized in that it is provided with a jacket made in the form of a spiral channel with a lid.
    [3]
    3. Reactor on PP. 1 and 2, characterized in that the lid is concave.
    [4]
    4. Reactor on PP. 1-3, characterized in that the lid is made convex.
    [5]
    5. Reactor on PP. 1-4, characterized in that the spiral channel has the shape of a quadrilateral. Sources of information taken into account in the examination 1. US patent. 3,133,109, cl. 260-443.2, I960,
    类似技术:
    公开号 | 公开日 | 专利标题
    SU990071A3|1983-01-15|Fluidized-bed reactor
    US5035283A|1991-07-30|Nested-tube heat exchanger
    US4544544A|1985-10-01|Plate reactors for chemical syntheses under high pressure in gaseous phase and with heterogeneous catalysis
    US3982901A|1976-09-28|Heat transfer element and tuyere for fluidized bed reactor
    GB1568538A|1980-05-29|Fluid bed process heater
    KR100961597B1|2010-06-04|Heat exchanger
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    US5980838A|1999-11-09|Reactor head for a monolithic co-current or countercurrent reactor
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    US4204573A|1980-05-27|Heat exchanger with concentric flow tubes
    US2198555A|1940-04-23|Contact chamber
    JP2004531371A5|2005-12-22|
    US3682241A|1972-08-08|Heat exchanger, particularly for cooling fresh cracked and/or synthesis gases
    US3814178A|1974-06-04|Heat exchanger
    US3508606A|1970-04-28|Heat exchanger
    US3833051A|1974-09-03|Heat exchange
    US2452391A|1948-10-26|Heat exchanger
    US4276928A|1981-07-07|Superheater inlet/outlet header
    GB1243942A|1971-08-25|Heat exchanger of the tube and shell type
    CA3066818A1|2019-01-03|Heat exchanger for heating or cooling bulk solids
    US2219214A|1940-10-22|Contact chamber
    CA2969595A1|2018-12-02|Improved spiral plate heat exchanger
    US3173764A|1965-03-16|Apparatus for the exothermic and catalytic reforming of hydrocarbons
    EP0018745B1|1982-12-08|Heat exchanger
    SU992986A1|1983-01-30|Contact-type water heater
    同族专利:
    公开号 | 公开日
    FR2379786B1|1982-07-09|
    JPS53127396A|1978-11-07|
    DE2704975A1|1978-08-24|
    DE2704975C2|1982-12-23|
    CA1104797A|1981-07-14|
    US4176710A|1979-12-04|
    GB1581613A|1980-12-17|
    FR2379786A1|1978-09-01|
    BR7800691A|1978-09-26|
    BE863683A|1978-08-07|
    引用文献:
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    GB715789A|1951-07-31|1954-09-22|Bataafsche Petroleum|Heat-transmission process and apparatus therefor|
    FR1179572A|1957-07-11|1959-05-26|Pechiney|Method and apparatus for heating and cooling powders|
    US3174834A|1959-08-24|1965-03-23|Richard M Edwards|Fluidized bed reactor|
    US3253650A|1960-07-11|1966-05-31|Frank J Mcentee Jr|Heat-exchange apparatus|
    US3133109A|1960-11-28|1964-05-12|Gen Electric|Silicon compound process and apparatus|
    US3243282A|1963-04-24|1966-03-29|Aluminum Lab Ltd|Recovery of aluminum from gaseous aluminum monohalide|
    GB1415659A|1972-03-02|1975-11-26|Plessey Co Ltd|Heat exchange apparatus with gas chamber below heat exchange bed|
    DD116083A1|1974-04-11|1975-11-05|
    NL170458C|1975-05-20|1982-11-01|Ir Gustav Adolf Pieper|HEAT EXCHANGER, INCLUDING A GRANULATIC CONTAINER CONTAINING VERTICAL TUBES, AND METHOD FOR ITS COMPANY.|
    US3982901A|1975-06-25|1976-09-28|Dorr-Oliver Incorporated|Heat transfer element and tuyere for fluidized bed reactor|
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    US4582120A|1985-01-03|1986-04-15|Ashland Oil, Inc.|Apparatus for cooling fluid solid particles in a regeneration system|
    US4906441A|1987-11-25|1990-03-06|Union Carbide Chemicals And Plastics Company Inc.|Fluidized bed with heated liners and a method for its use|
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    DE102013212908A1|2013-07-02|2015-01-08|Wacker Chemie Ag|Analysis of the composition of a gas or gas stream in a chemical reactor and a process for the production of chlorosilanes in a fluidized bed reactor|
    US9404177B2|2014-08-18|2016-08-02|Rec Silicon Inc|Obstructing member for a fluidized bed reactor|
    WO2017178080A1|2016-04-15|2017-10-19|Wacker Chemie Ag|Method for organochlorosilane production in the fluidized bed process|
    US10782075B2|2017-07-06|2020-09-22|Technip Process Technology, Inc.|Catalyst heat removal cluster and tube design|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19772704975|DE2704975C2|1977-02-07|1977-02-07|Heat exchange device for fluidized bed reactors for carrying out gas / solid reactions, in particular for producing silicon-halogen compounds by means of silicon-containing contact masses|
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