Reactor

专利摘要:
In an ammonia synthesis column, the combination of a tube bundle heat exchanger and a boiler with two superposedly arranged catalyst beds permits to recover considerable amounts of reaction heat, the flow of the gases being reacted running in a radial direction.
公开号:SU791203A3
申请号:SU762380907
申请日:1976-07-15
公开日:1980-12-23
发明作者:Пагани Джорджо
申请人:Снампрогетти С.П.А. (Фирма)；
IPC主号:

专利说明:

The invention relates to chemical reactor designs and can be used in ammonia synthesis processes. The ammonia synthesis reactor contains a vertical cylindrical body with a lid and a bottom, in which a high pressure chamber is placed, placed vertically coaxially in the case, the upper and lower horizontal partitions are fixed inside the shell and dividing it into upper and lower catalytic zones, located in the lower part of the shell a tubular heat exchanger, catalytic baskets, The external gas channels located in the catalytic zones and separating the external gas channels from the shell, and the boiler mounted on the lid along the housing axis, made in the form of I-shaped heat exchanging trunks} - The disadvantages of this reactor are insufficient process efficiency and the absence of reaction heat recovery. The purpose of the invention is to intensify the process and recover the heat of reaction. The goal is achieved by the fact that the reactor is equipped with a cylindrical shell with holes in its lid and an upper horizontal partition outside the boiler, with openings in the lower part, a branch pipe connecting the upper catalytic zone with a housing and catalytic baskets made in the form of fixed on horizontal partitions perforated coaxial cylinders; in the horizontal partitions along the axis of the casing there are central openings connecting the casing with the lower catalytic thereof, and a lower catalytic zone - with a tubular heat exchanger, respectively, wherein the reactor is provided with a regulating valve mounted on a pipe between the top of the catalyst zone and the casing. FIG. 1 shows a schematic overview of the reactor, a longitudinal section; in fig. 2 - seal the upper end of the boiler in the flange. The ammonia synthesis reactor contains a vertical cylindrical body 1 with a lid 2 and a bottom 3, in which a high pressure chamber 4 is made,
not placed in the case coaxially vertical cylindrical shell 5, the upper and lower horizontal partitions b and 7, fixed inside the shell 5 and dividing it into upper and lower catalytic zones 8 and 9, located in the lower part of the shell 5 tubular heat exchanger 10, catalytic baskets 11 and 12 placed in the catalytic zones 8 and 9 and separating the outer channels 13 for gas from the shell 5, mounted on the lid 2 along the housing axis 14, made in the form of i-shaped heat exchange tubes, fixed with their ends to the roofs e 2 and the upper horizontal partition 6 outside the boiler 14, a cylindrical casing 15 with openings 16 in its lower part and a nozzle 17 connecting the upper catalytic zone 8 to the casing 15. The catalytic baskets 11 and 12 are made in the form of fixed on the horizontal partitions coaxial perforated cylinders. In the horizontal partitions and 7 along the axis of the housing there are central holes 18 and 19 connecting the casing 15 with the lower catalytic zone 9 and the lower catalytic zone 9 with the tubular heat exchanger 10, respectively. Additionally, the reactor is equipped with a control valve 20 installed on the pipe 17 between the upper catalytic zone 8 and the casing 5.
The reactor operates as follows.
The feed gas, preheated in the tubes of the heat exchanger 10, flows through the channel 13 of an annular cross-section into the first catalytic zone 9 filled with a catalyst, flows radially through it and the reaction occurs. Reaction products and unreacted gases flow through and out of the channel 21 partially through the holes 16 and partly through the pipe 17 into the casing 15 of the tubular boiler 14.
Both streams are combined at the bottom of the boiler 14 and from there flow through the second catalytic zone 8 through the second channel 22 with an annular cross-section. Reagents and reaction products flow out radially through the second zone 9 and are collected in the central channel 23 of the second zone 9, from where they protrude and come into contact with the outer (outer) surface of the tubes of the heat exchanger 10.
The outer casing 1 is made of alloyed steel with a hook 2 at the upper end, with a central channel through which the boiler 24 passes, formed by a bundle of pipes U or a bayonet type, directly attached to the lid 2 of the reactor by means of flanges 25 and is thus easily removed. Water. The pipes of the Zoiler come through the inlet 26, and the steam exits through the fitting 27. The casing 15 of the boiler 14 is a cylindrical pipe welded in the lower part to the partition 6 and preferably equipped with a butt 28
thermal expansion. The length of the casing 15 is set in such a way that when the cover is attached to the boiler, the top of the casing 15 is depressed. into a specially provided groove or groove formed on
5 of the lower surface of the flange 25 of the boiler, so that an internal closure is formed between the cold gas washing the outside of the casing wall and the hot gas inside the boiler.
0 into the gap 29. Between the casing 15 and the flange 25, the edge of the casing 15 is inserted into the groove 30 of the flange 25 provided with a sealing material 31. A tight shutter is provided outside
5 lenticular epiploon (stuffing) 32
The boiler is equipped with a regulating CC. barrel 20 operating outside and allowing varying flow rates
gas to the boiler. The boiler casing is provided at the lower end with a set of holes 16, which allow part of the gas to pass when the valve 20 is completely open. Cold gas enters the reactor through channel 33 into the space above the catalyst and from there enters through the annular channel 4 into the heat exchanger tubes 10 and from the last to the first layer ( catalyst) and then to the second, as shown
0 above.
The hot gases formed during the reaction flow into the boiler through channel 4, which is also provided with a thermal expansion joint.
5 In the toroidal position i around the boiler and inside the space bounded by the outer surface of the boiler and the cylindrical wall coaxial to the housing, the channel 4 of the annular section through which the gas passes is limited and the first layer of catalyst is located. The latter is actually located from the outer surface of the boiler and the inner surface of the aforementioned
cylindrical wall

权利要求:
Claims (1)
[1]
Invention Formula
An ammonia synthesis reactor containing a vertical cylindrical body with a lid and a bottom in which a high-pressure chamber is made, which is located coaxially in the body
vertical cylindrical shell

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同族专利:

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AU502947B2|1979-08-16|

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ES450403A1|1977-08-01|

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ZA763987B|1977-05-25|

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DE2631898B2|1980-07-31|

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MX146607A|1982-07-15|

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IL50030A|1979-01-31|

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IN145037B|1978-08-12|

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PT65365B|1978-01-09|

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RO69368A|1981-06-30|

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CH607983A5|1978-12-15|

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DE2631898A1|1977-01-20|

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GB1549708A|1979-08-08|

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NL7607750A|1977-01-18|

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TR18747A|1977-08-02|

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NL177305B|1985-04-01|

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IL50030D0|1976-09-30|

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MY8100039A|1981-12-31|

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ZM9276A1|1977-07-21|

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HU182046B|1983-12-28|

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BE844160A|1977-01-17|

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FR2318111B1|1979-09-21|

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PH14424A|1981-07-16|

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CS221262B2|1983-04-29|

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AT344198B|1978-07-10|

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DE2631898C3|1981-05-21|

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NL177305C|1985-09-02|

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FR2318111A1|1977-02-11|

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EG12014A|1978-06-30|

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IE43795L|1977-01-15|

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PL116376B1|1981-06-30|

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AR207420A1|1976-09-30|

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BR7605720A|1977-08-23|

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PT65365A|1976-08-01|

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IT1041778B|1980-01-10|

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SE7608062L|1977-01-16|

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DK317476A|1977-01-16|

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BG28252A3|1980-03-25|

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SE426476B|1983-01-24|

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YU172676A|1982-05-31|

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LU75376A1|1977-02-25|

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IE43795B1|1981-06-03|

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ATA517576A|1977-11-15|

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US4101281A|1978-07-18|

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JPS5211199A|1977-01-27|

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CA1074084A|1980-03-25|

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AU1574876A|1978-01-12|

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DD125341A5|1977-04-13|

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DE102015104911A1|2015-03-30|2016-10-06|Thyssenkrupp Ag|Flow guidance of a fluid in a flow container|

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CN105013408B|2015-08-25|2017-05-17|南京聚拓化工科技有限公司|Quasi-full-radial fixed bed reactor|

法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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IT25421/75A|IT1041778B|1975-07-15|1975-07-15|RADIAL FLOW REACTOR FOR AMMONIA SYNTHESIS WITH HIGH THERMAL LEVEL STEAM PRODUCTION|

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