CN201454504U - Hydrocyanic acid reactor body - Google Patents

Hydrocyanic acid reactor body Download PDF

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Publication number
CN201454504U
CN201454504U CN2009201273528U CN200920127352U CN201454504U CN 201454504 U CN201454504 U CN 201454504U CN 2009201273528 U CN2009201273528 U CN 2009201273528U CN 200920127352 U CN200920127352 U CN 200920127352U CN 201454504 U CN201454504 U CN 201454504U
Authority
CN
China
Prior art keywords
tube
heat exchanger
heat exchange
exchanger tube
perforated plate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2009201273528U
Other languages
Chinese (zh)
Inventor
王辉
陈恩泽
朱西建
杨博
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Zhongrong Petrochemical Machinery Manufacturing Co Ltd
Original Assignee
Chongqing Zhongrong Petrochemical Machinery Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chongqing Zhongrong Petrochemical Machinery Manufacturing Co Ltd filed Critical Chongqing Zhongrong Petrochemical Machinery Manufacturing Co Ltd
Priority to CN2009201273528U priority Critical patent/CN201454504U/en
Application granted granted Critical
Publication of CN201454504U publication Critical patent/CN201454504U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

The utility model discloses a hydrocyanic acid reactor body, in the technical scheme, a heat exchange tube (2) and an upper tube plate (3) are arranged in a shell (1), wherein the upper surface of the upper tube plate (3) is provided with fire clay and catalyst (4), a through hole is arranged at the position, which corresponds to the heat exchange tube (2), on the upper tube plate (3), the hole wall of the through hole is extended downwards to form an annular boss (5) which is fixed with the top end of the heat exchange tube (2) via a transition joint (6), an insertion tube (7) is penetrated into the through hole, the lower end of the insertion tube (7) is extended into the transition joint (6), and the top end of the insertion tube (7) surpasses the top surface of the fire clay and the catalyst (4). The utility model changes the connection mode of the heat exchange tube and the upper tube plate so that the tube head of the heat exchange tube cannot be directly connected with high temperature, thereby effectively preventing the heat exchange tube from being damaged by high temperature, guaranteeing the performances and the service life of the heat exchange tube, and the utility model has the advantages of reasonable design, easy implementation, reliable performance and the like.

Description

Hydrogen cyanide reactor body
Technical field
The utility model relates to a kind of reactor, specifically, relates in particular to the body of hydrogen cyanide reactor.
Background technology
The hydrogen cyanide reactor is one of core apparatus in the hydrogen cyanide technological process of production, generates the hydrogen cyanide mist by this equipment.Its operation principle is: three kinds of raw materials (ammonia, natural gas, air etc.) that will mix are under computer control, enter the hydrogen cyanide reactor, in equipment, under the catalytic action of catalyst, carry out chemistry (heat release) reaction continuously, produce the hydrogen cyanide mist.The reactor body is the stage casing part of hydrogen cyanide reactor.In the traditional structure, be provided with some heat exchanger tubes in housing, the via hole on the upper perforated plate is passed in the upper end of this heat exchanger tube, and exceeds the end face of fire clay, carries out fillet welding at the place, aperture of via hole between heat exchanger tube and the upper perforated plate and fixes.Because mixed gas burns at upper perforated plate, temperature is up to more than 1000 ℃, and the heat exchanger tube tube head directly contacts high temperature, and scaling loss takes place easily for Yin Gaowen and excessive temperature differentials, thereby influences structural behaviour and service life.
The utility model content
Technical problem to be solved in the utility model is to provide a kind of hydrogen cyanide reactor body that can effectively prevent the heat exchanger tube scaling loss.
The technical solution of the utility model is as follows: a kind of hydrogen cyanide reactor body, in housing, be provided with heat exchanger tube and upper perforated plate, the upper surface of upper perforated plate is provided with fire clay and catalyst, and the position of corresponding heat exchanger tube offers via hole on the upper perforated plate, its key is: the hole wall of described via hole extends downwards, form annular boss, this annular boss is fixed by the top of transit joint and heat exchanger tube, in described via hole, be equipped with and insert pipe, the lower end of this insertion pipe is stretched in the transit joint, and the upper end of inserting pipe exceeds the end face of fire clay and catalyst.
Adopt above technical scheme, adopt transit joint to be connected good manufacturability, dependable performance between heat exchanger tube and the upper perforated plate; Insert pipe and adopt high temperature resistant material to make, make the tube head of heat exchanger tube directly not contact high temperature, effectively alleviated high temperature and excessive temperature differentials and the scaling loss tendency that produces.
For simplified structure, convenient for assembly, the upper end and the annular boss of above-mentioned transit joint connect, and be fixing by welding, and connects with heat exchanger tube after closing up in the lower end of transit joint, also fixing by welding; The step surface that closing in forms in the described transit joint is spacing to the lower end of inserting pipe, and this internal diameter that inserts pipe equates with the internal diameter of heat exchanger tube.
Be provided with cooling tube below above-mentioned upper perforated plate, this cooling tube offers fluid hole near the position of transit joint.The cooling fluid that flows in the cooling tube can further reduce the temperature difference of upper perforated plate wall to transit joint and upper perforated plate spray by fluid hole.
Beneficial effect: the utility model is by changing the connected mode between heat exchanger tube and the upper perforated plate, make the tube head of heat exchanger tube directly not contact high temperature, thereby effectively prevented heat exchanger tube generation scaling loss, ensure the performance and the service life of heat exchanger tube, had reasonable in design, characteristics such as enforcement is easy, dependable performance.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the connection diagram between heat exchanger tube and the upper perforated plate in the utility model.
Fig. 3 is the B portion enlarged drawing of Fig. 1.
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples:
As Fig. 1, shown in Figure 3, the utility model is between reactor epimere 10 and reactor hypomere 11, and the housing 1 in the utility model partly is made of barrel-type casing 1a, expansion joint 1b, conical shell 1c, shell pipe nipple 1d, U bend 1e and pipe nipple 1f etc.Be fixed with lower perforated plate 9 in the lower end of barrel-type casing 1a, the upper end of barrel-type casing 1a links to each other with the lower end of conical shell 1c by expansion joint 1b, the upper end of conical shell 1c connects shell pipe nipple 1d, the inboard of this shell pipe nipple 1d has pipe nipple 1f, be connected by U bend 1e between the top of pipe nipple 1f and shell pipe nipple 1d, at the bottom of pipe nipple 1f welding upper perforated plate 3, the upper surface of upper perforated plate 3 is provided with one deck fire clay and catalyst 4.
As Fig. 1, Fig. 2, shown in Figure 3, in housing 1, be provided with some heat exchanger tubes 2, lower perforated plate 9 is passed in the lower end of this heat exchanger tube 2, and fixes with lower perforated plate 9.The position of corresponding heat exchanger tube 2 offers via hole on described upper perforated plate 3, is equipped with in the via hole to insert pipe 7, inserts pipe 7 and is preferably stainless steel tube, and the upper end of inserting pipe 7 exceeds the end face of fire clay and catalyst 4.The hole wall of described via hole extends downwards, forms annular boss 5, and the upper end of the bottom of this annular boss 5 and transit joint 6 connects, and is fixing by welding.Top with heat exchanger tube 2 after closing up in the lower end of transit joint 6 connects, and is also fixing by welding.The step surface of the described transit joint 6 interior formation of closing up is spacing to the lower end of inserting pipe 7, and internal diameter of this insertion pipe 7 equates with the internal diameter of heat exchanger tube 2.Also be provided with cooling tube 8 below described upper perforated plate 3, this cooling tube 8 offers fluid hole near the position of transit joint 6.

Claims (4)

1. hydrogen cyanide reactor body, in housing (1), be provided with heat exchanger tube (2) and upper perforated plate (3), the upper surface of upper perforated plate (3) is provided with fire clay and catalyst (4), and the position that upper perforated plate (3) is gone up corresponding heat exchanger tube (2) offers via hole, it is characterized in that: the hole wall of described via hole extends downwards, form annular boss (5), this annular boss (5) is fixed by the transit joint (6) and the top of heat exchanger tube (2), in described via hole, be equipped with and insert pipe (7), the lower end of this insertion pipe (7) is stretched in the transit joint (6), and the upper end of inserting pipe (7) exceeds the end face of fire clay and catalyst (4).
2. hydrogen cyanide reactor body according to claim 1, it is characterized in that: the upper end of described transit joint (6) and annular boss (5) connect, fixing by welding, after closing up, the lower end of transit joint (6) connects with heat exchanger tube (2), and also fixing by welding; The step surface that closing in forms in the described transit joint (6) is spacing to the lower end of inserting pipe (7), and this inserts the internal diameter of managing (7) and equates with the internal diameter of heat exchanger tube (2).
3. hydrogen cyanide reactor body according to claim 1 and 2 is characterized in that: described insertion pipe (7) is a stainless steel tube.
4. hydrogen cyanide reactor body according to claim 1 is characterized in that: be provided with cooling tube (8) in the below of described upper perforated plate (3), this cooling tube (8) offers fluid hole near the position of transit joint (6).
CN2009201273528U 2009-05-18 2009-05-18 Hydrocyanic acid reactor body Expired - Fee Related CN201454504U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009201273528U CN201454504U (en) 2009-05-18 2009-05-18 Hydrocyanic acid reactor body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009201273528U CN201454504U (en) 2009-05-18 2009-05-18 Hydrocyanic acid reactor body

Publications (1)

Publication Number Publication Date
CN201454504U true CN201454504U (en) 2010-05-12

Family

ID=42381849

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009201273528U Expired - Fee Related CN201454504U (en) 2009-05-18 2009-05-18 Hydrocyanic acid reactor body

Country Status (1)

Country Link
CN (1) CN201454504U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014003525A1 (en) * 2012-06-27 2014-01-03 Товарищество С Ограниченной Ответственностью "Туймекент" Method for producing hydrogen cyanide
CN113267076A (en) * 2021-06-04 2021-08-17 四川能投建工集团设计研究院有限公司 Hydrocyanic acid oxidation reactor and tube plate cooling structure thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014003525A1 (en) * 2012-06-27 2014-01-03 Товарищество С Ограниченной Ответственностью "Туймекент" Method for producing hydrogen cyanide
RU2603656C2 (en) * 2012-06-27 2016-11-27 Товарищество С Ограниченной Ответственностью "Туймекент" Method of producing hydrogen cyanide
CN113267076A (en) * 2021-06-04 2021-08-17 四川能投建工集团设计研究院有限公司 Hydrocyanic acid oxidation reactor and tube plate cooling structure thereof
CN113267076B (en) * 2021-06-04 2022-08-23 四川能投建工集团设计研究院有限公司 Hydrocyanic acid oxidation reactor and tube plate cooling structure thereof

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100512

Termination date: 20170518

CF01 Termination of patent right due to non-payment of annual fee