CN2291201Y - Radial fixed bed catalytic reactor for co-producing steam - Google Patents
Radial fixed bed catalytic reactor for co-producing steam Download PDFInfo
- Publication number
- CN2291201Y CN2291201Y CN 97234399 CN97234399U CN2291201Y CN 2291201 Y CN2291201 Y CN 2291201Y CN 97234399 CN97234399 CN 97234399 CN 97234399 U CN97234399 U CN 97234399U CN 2291201 Y CN2291201 Y CN 2291201Y
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- tube
- reactor
- shunting
- water cooling
- fixed bed
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Abstract
The utility model designs a radial fixed bed catalytic reactor for co-producing steam. A group of water-cooled pipes is arranged in the radial reactor, high-temperature reaction heat generated by reaction is used for heating cooling water so that the cooling water can be vaporized for co-producing the steam, and the purpose of recovering energy is achieved. The reactor has the advantages of little resistance of a bed layer, high space speed, large production capacity and reasonable energy utilization, and the utility model is a more promising fixed bed catalytic reactor. The utility model can be widely used for ammonia synthesis, methanol synthesis, the process of carbon monoxide conversion, the hydrogenation process of organic compounds and the process of other strong exothermic reactions.
Description
The utility model relates to a kind of fixed bed catalytic reactor.
Fixed bed catalytic reactor is a kind of reactor commonly used in chemical industry and the petrochemical industry, is widely used in the hydrogenation process of synthetic, the carbon monodixe conversion process of synthetic, the methyl alcohol of ammonia, organic compound and other reversible exothermic reaction processes.For this reason, many scientific workers have designed numerous various types of fixed bed catalytic reactors, at present, the reactor of industrial use can be divided into two classes from liquid form: Radial Flow and axial flow also can be divided into two classes from heat exchange in form: external-cooling type and self-cooled.Deutsche Bundespatent (DE2123950) and Japan Patent (J63123433) disclose a kind of synthetic tower of axial flow byproduct steam respectively, this synthetic tower energy byproduct steam, the energy utilization is comparatively reasonable, but bed resistance is big, be difficult to improve air speed, production capacity is not high, Danish Patent (WO9009234) discloses a kind of radially synthetic tower, such synthetic tower, overcome the big shortcoming of axial flow reactor beds layer resistance, production capacity increases substantially, but fails rationally to recover energy, can not byproduct steam, cause effective loss of energy.For this reason, a kind of new fixed bed reactors of people's phase developmental research are to satisfy industrial needs.
The purpose of this utility model is to overcome the shortcoming of above-mentioned two kinds of fixed bed catalytic reactors, and the advantage of comprehensive two kinds of reactors designs a kind of radially byproduct steam fixed bed catalytic reactor, and it is big to reach production capacity, rationally utilizes energy, the purpose of byproduct steam.
Design of the present invention is such:
Usually, fixed bed catalytic reactor by the urceolus that bears high pressure and only bear pressure reduction internals---basket is constituted.The utility model is provided with one group of water cooling tube in the basket of radial fixed-bed reactor, the high-temperature reaction heat that is produced when the reacting gas radial flow is crossed bed is by the water cooling in the water cooling tube, and water heating back vaporization produces steam, reclaim high-temperature reaction heat, reach the purpose of rationally utilizing energy.Said reactor combines the advantage of radial reactor and axial byproduct steam reactor, will be a kind of very promising fixed bed catalytic reactor.
According to above-mentioned design, the utility model has designed a kind of radially byproduct steam fixed bed catalytic reactor, further sets forth architectural feature of the present utility model below in conjunction with accompanying drawing.
Fig. 1 is byproduct steam fixed bed catalytic reactor structure chart radially
Fig. 2 shunts the local diagrammatic sketch of tube
Fig. 3 shunts the local diagrammatic sketch of a cross section
Fig. 4 collaborates the central tube cross-sectional view
Fig. 5 water cooling tube structure chart is wherein: 1---urceolus
2---the shunting tube
3---flow manifold
4---billet
5---the interflow central tube
6---internal layer
7---skin
8---lattice
9---water cooling tube
10---plenum chamber
11---main steam range
12---the gas access
13---steam (vapor) outlet
14---manhole
15---the shunting aperture
16---the internal layer aperture
17---outer aperture
18---distributive pipe
19---bottom plate
20---the mouth of a river
21---gas vent
22---unload the catalyst mouth
23---plate washer
A shunting tube (2) is set in the urceolus (1) of reactor, shunting tube (2) is gone up close shunting aperture (15) towards 2～ 3mm, percent opening 15～20%, the inwall of cylindrical shell (1) is fixed in shunting tube (2) lower end, but upper end free wxpansion, form the flow manifold (3) that 3-20mm is wide between shunting tube (2) and the cylindrical shell (1), the sectional area of flow manifold (3) is identical with the sectional area of gas reactor inlet (12), the outside of shunting tube (2) is welded with stainless steel billet (4), to keep the width of flow manifold (3), the middle part of reactor is an interflow central tube (5), constitute by internal layer (6) and outer (7), weldering lining stainless steel billet (4) between two-layer, be used to keep two-layer between certain clearance, outer (7) go up close outer aperture (17) towards 2～ 3mm, percent opening is 15～20%, internal layer (6) is gone up close internal layer aperture (16) towards 3～ 5mm, pitch of holes is 40～100mm, the top seal of central tube (5), the lower end is connected with gas vent (21) on placing cylindrical shell (1); Between shunting tube (2) and central tube (5) one group of water cooling tube (9) is set, the stainless steel tube tens that generally adopts 18～ 40mm is to thousands of, than huyashi-chuuka (cold chinese-style noodles)---and the cold pipe area of unit volume is 20～120m
2/ m
3Water cooling tube (9) bottom is summarized in distributive pipe (18), distributive pipe (18) is connected with water inlet (20), the top of water cooling tube (9) is a plenum chamber (10), be connected with steam (vapor) outlet (13) by main steam range (11), bottom plate (19) is welded in the bottom of cylindrical shell (1), be used for fixing distributive pipe (18) and water cooling tube (9), baffle plate (23) is arranged at the top of cylindrical shell (1), be used to prevent that catalyst from entering flow manifold (3), lattice (8) is used for fixing water cooling tube (9) and interflow central tube (5), catalyst then fills in shunting tube (1) by manhole (14), space segment between water cooling tube (9) and the central tube (5) can draw off cylindrical shell (1) by drawing off catalyst mouth (22) during maintenance.Unstripped gas enters flow manifold (3) after entering reactor by gas access (12), enters catalyst layer by shunting aperture (15) then, and reaction heat is taken away by the cooling water in the water cooling tube (9), and reacted gas is by interflow central tube (5) outflow reactor.
The advantage of the fixed bed catalytic reactor of said structure is fairly obvious, has both kept the radial reactor high-altitude The advantage of speed, big production capacity simultaneously again can byproduct steam, rationally recovers energy, and the loading and unloading catalyst is very convenient, and axially Flow reactor is compared, and reaches same output, and catalyst amount can reduce 20-30%, and energy efficiency improves 15～20%, can be used for that methyl alcohol is synthetic, ammonia synthesis, carbon monodixe conversion, organic compound hydrogenation and other reversible heat releases be anti-Answer process.
Claims (3)
1, a kind of radially byproduct steam fixed bed catalytic reactor, in cylindrical shell (1), be provided with the shunting tube (2) of a Mi Chong shunting aperture (15), form the flow manifold (3) that width is 3-20mm between cylindrical shell (1) and the shunting tube (2), the inwall of cylindrical shell (1) is fixed in shunting tube (2) lower end, baffle plate (23) is fixed in the top of cylindrical shell (1), topped in the top of shunting tube (1), the center of cylindrical shell (1) is an interflow central tube (5) that is made of internal layer (6) and outer (7), internal layer (6) is gone up close towards internal layer aperture (16), outer (7) go up close towards outer aperture (17), it is characterized in that: between shunting tube (2) and interflow central tube (5), one group of water cooling tube (9) is set, the top of water cooling tube (9) is a plenum chamber (10), plenum chamber (10) is connected with steam (vapor) outlet (13) by main steam range (11), the bottom of water cooling tube (9) is summarized in distributive pipe (18), and is connected with water inlet (20).
2,, it is characterized in that the ratio huyashi-chuuka (cold chinese-style noodles) of water cooling tube (9) is 20-120m according to the described reactor of claim 1
2/ m
3
3,, it is characterized in that water cooling tube (9) is the stainless steel tube of 18～ 40mm, tens to thousands of according to the described reactor of claim 1-2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 97234399 CN2291201Y (en) | 1997-04-28 | 1997-04-28 | Radial fixed bed catalytic reactor for co-producing steam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 97234399 CN2291201Y (en) | 1997-04-28 | 1997-04-28 | Radial fixed bed catalytic reactor for co-producing steam |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2291201Y true CN2291201Y (en) | 1998-09-16 |
Family
ID=33945766
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 97234399 Expired - Fee Related CN2291201Y (en) | 1997-04-28 | 1997-04-28 | Radial fixed bed catalytic reactor for co-producing steam |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2291201Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100335158C (en) * | 2004-11-26 | 2007-09-05 | 湖南安淳高新技术有限公司 | Water-piping isothermal methanol reactor |
| CN100443462C (en) * | 2005-05-12 | 2008-12-17 | 中国石油天然气股份有限公司 | Radial reactor for preparing ethylene (propylene) carbonate |
| CN101301597B (en) * | 2007-05-11 | 2012-10-31 | 曼德韦有限公司 | Cooling pipe reactor |
| CN103071431A (en) * | 2013-02-07 | 2013-05-01 | 中石化宁波工程有限公司 | Axial and radial reactor structure for sulfur-tolerant conversion process |
| CN110201624A (en) * | 2019-07-09 | 2019-09-06 | 青岛科技大学 | A kind of contiguous segmentation charging reactor for synthetic reaction |
-
1997
- 1997-04-28 CN CN 97234399 patent/CN2291201Y/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100335158C (en) * | 2004-11-26 | 2007-09-05 | 湖南安淳高新技术有限公司 | Water-piping isothermal methanol reactor |
| CN100443462C (en) * | 2005-05-12 | 2008-12-17 | 中国石油天然气股份有限公司 | Radial reactor for preparing ethylene (propylene) carbonate |
| CN101301597B (en) * | 2007-05-11 | 2012-10-31 | 曼德韦有限公司 | Cooling pipe reactor |
| CN103071431A (en) * | 2013-02-07 | 2013-05-01 | 中石化宁波工程有限公司 | Axial and radial reactor structure for sulfur-tolerant conversion process |
| CN103071431B (en) * | 2013-02-07 | 2015-10-28 | 中石化宁波工程有限公司 | A kind of axial-radial flow reactor structure for sulfur resistant conversion process |
| CN110201624A (en) * | 2019-07-09 | 2019-09-06 | 青岛科技大学 | A kind of contiguous segmentation charging reactor for synthetic reaction |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |