• 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 methanation reactor, to be used preferably in an integrated urea-ammonia process for methanizing carbon oxides is disclosed, in which the catalyst bed and an underlying heat exchanger of the tube-bundle type make up a unit mounted centrally of the reactor casing with a gap left between the reactor casing inside wall and said centrally mounted unit. Fresh gases to be methanized enter the gap, then the heat exchanger from below and flow upwards to the catalyst bed, whereafter they flow down to the exchanger again. Incoming gases sweep the exchanger tubes from the outside, while the reacted gases flow in the interior of the tubes of the heat exchanging bundle. Insulation blankets and gland seals are provided.
    公开号:SU1056878A3
    申请号:SU782604247
    申请日:1978-04-14
    公开日:1983-11-23
    发明作者:Лагана Винченцо；Савьяно Франческо；Феррантино Станислао
    申请人:Снампрогетти С.П.А. (Фирма)；
    IPC主号:
    专利说明:

    This invention relates to converters for converting carbon oxides to methane and can be used to produce methane. . A converter for producing methane is known, comprising an outer case, an upper and a lower cover with nozzles, for supplying gases for conversion, an axially mounted axially spaced relative to the outer case, an inner case, with a toroidal catalyst bed and a tubular heat exchanger located under it, connected to the catalyst by means of a pipe coaxially with the inner casing, outside of which the insulating material is placed, and the sealing system, made in the form of two layers of stuffing box, between which is placed n annular insert with inlet soup, E y channels disadvantage of the known convertor is that having therein a upglotnitelna system does not prevent contamination of the interior of the gases of the reactor. The aim of the invention is to eliminate the leakage of gases from the converter. To achieve this goal, in the converter for producing methane, containing the outer case, the upper and lower covers with nozzles for supplying gases for conversion, axially spaced with respect to the outer case, the inner case with a toroidal catalyst bed and a tubular heat exchanger underneath, connected a catalyst layer by means of a pipe coaxially with the inner casing, outside of which the heat insulating material is placed, and the sealing system, made in the form of two layers of stuffing box abuts, between which is placed an annular liner with a SUPPRESSING channel, the inlet channel is U-shaped, the vertical branches of which are connected to the water supply source, the pressure in which exceeds the pressure in the converter. In this case, the converter is supplied with a supply pipe hot gases to the catalyst bed. FIG. 1 shows a converter, about a longitudinal section; in fig. 2 and 3 embodiments of the sealing system The converter includes a housing 1, to which a lid 3 is attached by means of bolts 2 In turn, the roofs of the ke 3 are strengthened: a pipe for feeding a fresh mixture of gases for conversion during normal operation of the device, a pipe 5 for feeding hot gases at the time of start-up of the converter and the deaf channel 6 for a thermocouple. Inside the case there is a toroidal layer of catalyst 7, which is located on a grid 8 and balls of alumina 9, under a catalyst there is a tubular heat exchanger 10, equipped with guide vanes 11 for improving heat transfer from hot to cold gases. There is a gap 12 between the converter housing 1 and the node consisting of a catalyst and a heat exchanger 12. The node is isolated by a layer of thermal insulating material 13, which can be glass wool, slag wool or asbestos powder. The inlet and outlet for gases have gland seals IV and 15 of woven material. The converter works as follows. The cold gases enter the converter to produce methane through pipe 4, pass through holes 16 through gap 12, and through hole 17 enter heat exchanger 10, where they are heated. The heated gas rises through the central tube 18 and passes down through the catalyst bed 7. The gaseous reaction products pass inside the tubes of the heat exchanger 10, cool therein and exit the converter through the tube 19. When the converter starts, in order for the reaction to start, it is necessary to feed it the amount of hot gases heated to the conversion temperature. Hot gases can flow through the pipe without heating the casing. For this, the hot gases to be converted go directly to the catalyst through pipe 5, and the cold gases through the pipe. To prevent the mixing of hot and cold gases, a wicker seal is provided (Fig. 2). The seal consists of a gasket 20, a support 21 and a gland cover 22, which presses the wicker gasket to the support, thus creating a hermetic seal for cold gases. There is also the problem of sealing the bottom of the converter, where, due to the thermal elongation of the pipe 19 that has been dragged down, it can occur; Detect leakage of gaseous reaction products at the point of contact of the pipe with the walls of the casing. To solve this problem, a sealing system with an intermediate hollow sleeve is provided, which allows forced circulation of water under pressure to avoid leakage of exhausted gases from the converter, B the tight system shown in FIG. 3 between the external wall of the pipe 19 and case 1, there is an asbestos wicker 23, compressed by the bottom of the converter 2k and stuffing box with flanges 25. The braided gasket is divided into two parts by sleeve 2b, which is connected by channel 27 to a water source under pressure 84 The topic cannot be leaked, because the hydraulic gates, formed by water under pressure exceeding the pressure in the converter, prevent the release of gaseous reaction products from the converter. The application of the proposed converter is particularly expedient in the complete urea-ammonia process, since it allows the conversion of carbon dioxide and carbon monoxide at the same pressure that is maintained in the synthesis reactor and ammonia. Thus, there is no need to compress the gas mixture converted to methane to synthesis pressure, which is a considerable advantage.
    1
    FIG. 2
    26
    Fig.Z
    gz ztt
    权利要求:
    Claims (2)
    [1]
    1. CONVERTER FOR PRODUCING METHANE, containing an outer casing, upper and lower covers with nozzles for supplying gases for conversion, installation * An axially mounted inner casing with a gap relative to the outer casing with a toroidal catalyst bed and a tubular heat exchanger located below it, connected to the catalyst layer by means of a pipe coaxial with the inner casing, on the outside of which heat-insulating material is placed, and a sealing system made in the form of two layers stuffing box, between which there is an annular liner with a supply channel, except that in order to eliminate leakage of gases from the converter, the supply channel is made P-obraznoyformy vertical branches of which communicate with a source of feed water under a pressure greater than the pressure in the converter.
    [2]
    2. The converter according to claim 1, with the exception that it is equipped with a pipe passing through the upper lid to supply hot gases to the catalyst bed.
    sy) SU w! 056878
    1 1056878 2
    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    DE2816062A1|1978-10-19|
    MX147851A|1983-01-24|
    FR2387077B1|1982-04-09|
    FR2387077A1|1978-11-10|
    IE780732L|1978-10-15|
    ES469695A1|1979-01-16|
    CS219339B2|1983-03-25|
    JPS60260526A|1985-12-23|
    SE7804267L|1978-10-16|
    JPS53130606A|1978-11-14|
    YU84478A|1982-08-31|
    IN148154B|1980-11-08|
    BR7802393A|1979-11-27|
    NO149629B|1984-02-13|
    IT1075397B|1985-04-22|
    GB1602801A|1981-11-18|
    IE46867B1|1983-10-19|
    DK160778A|1978-10-16|
    AT361508B|1981-03-10|
    DE2816062B2|1979-07-12|
    JPS6124371B2|1986-06-10|
    NO781277L|1978-10-17|
    NO149629C|1987-10-28|
    LU79436A1|1978-07-12|
    BE866007A|1978-10-16|
    DD136342A5|1979-07-04|
    BG33152A3|1982-12-15|
    YU39285B|1984-10-31|
    HU182918B|1984-03-28|
    US4252771A|1981-02-24|
    US4323252A|1982-04-06|
    DE2816062C3|1980-03-13|
    NL7804023A|1978-10-17|
    ATA263178A|1980-08-15|
    PL206020A1|1979-01-02|
    PL108933B1|1980-05-31|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT22499/77A|IT1075397B|1977-04-15|1977-04-15|METHANATION REACTOR|
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