CN201558691U - Combined reactor - Google Patents
Combined reactor Download PDFInfo
- Publication number
- CN201558691U CN201558691U CN2009200484697U CN200920048469U CN201558691U CN 201558691 U CN201558691 U CN 201558691U CN 2009200484697 U CN2009200484697 U CN 2009200484697U CN 200920048469 U CN200920048469 U CN 200920048469U CN 201558691 U CN201558691 U CN 201558691U
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- Prior art keywords
- tank body
- heat
- reacting tank
- move
- pipe
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Abstract
The utility model relates to a combined reactor, which mainly solves the technical problems that the existing reactor is of an integral structure, is not beneficial to assembly and transportation of the reactor, maximization of the equipment and the like. The combined reactor is characterized in that the reaction tank body comprises a bearing cylinder, an upper cover and a lower cover; the bearing cylinder, the upper cover and the lower cover are fastened and sealed by bolts; and the two ends of the bearing cylinder are respectively provided with a baffle to lead the inside of the reaction tank body to form cold gas distributing chamber, a catalytic gas bed layer and an inert material chamber. The combined reactor has the benefits that the reaction tank body is changed into a split structure, not only can be convenient for processing of the reaction tank body, improve the working benefits when in assembly, reduce the production cost, simultaneously also can be convenient for transportation and maximization of the equipment and reduce the transportation cost.
Description
Technical field
The utility model relates to a kind of chemical reaction equipment, relates to a kind of combination type reactor in particular, is mainly used in petrochemical industry.
Background technology
At present, be applied in the reactor of petroleum chemical industry, such as fixed bed catalytic reactor, shell-and-tube water cooling reactor, heat-insulated pipe shell-type water cooling reactor etc., for guaranteeing the sealing property and the bearing capacity of reactor, therefore, the reacting tank body of existing all kinds of reactors all is structure as a whole, and then earlier parts such as heat exchanger is installed in the reacting tank body when producing, and then is one with the reacting tank body welded seal; Adopt this structure, not only bad for the assembling of reactor, working efficiency is lower during its assembling, thereby has improved production cost; The installation when simultaneously, being unfavorable for also that the transportation of reactor and user use and the maximization of reactor.
Summary of the invention
In order to solve existing reactors is integral structure, is unfavorable for the technical problems such as maximization of assembling, transportation and the equipment of reactor; The utility model provides a kind of combination type reactor, and it is simple in structure, and is reasonable in design, can effectively solve the technical problems such as assembling, transportation and device maximization of reactor.
For solving above technical problem, the technical scheme that the utility model is taked is a kind of combination type reactor, it includes reacting tank body, described reacting tank body is provided with the inlet, outlet pipe outward and moves thermal medium into and out of tracheae, described reacting tank body includes cold air distributing chamber, catalysis air-bed floor and inert material chamber, described air inlet pipe is arranged on the top of reacting tank body and announces that with cold air the chamber communicates with moving the thermal medium escape pipe, described escape pipe and move bottom that the thermal medium air inlet pipe is arranged on reacting tank body and communicate with the inert material chamber; Be provided with heat exchanger tube in the described beds, this heat exchanger tube one end put announce indoor with cold air and with move the thermal medium escape pipe and be connected, its other end put indoor with inert material and with move the thermal medium air inlet pipe and be connected; It is characterized in that described reacting tank body includes pressure cylinder, loam cake and lower cover, described pressure cylinder and loam cake and lower cover seal by bolted; Described pressure cylinder two ends respectively are provided with a dividing plate, make and form separate cold air announcement chamber, catalysis air-bed floor and inert material chamber in the reacting tank body.
Further, described heat exchanger tube includes circle and moves heat pipe heat component and the rounded many groups of fan-shaped heat pipe heat components that move that are arranged in around it, and described circle is moved the heat pipe heat component and organized the fan-shaped heat pipe heat component that moves more and be connected successively and communicate.
Further, described fan-shaped move the heat pipe heat component be provided with four groups and be evenly distributed on circle move the heat pipe heat component around.
The beneficial effects of the utility model are to change reacting tank body into the branch body structure, not only can make things convenient for reacting tank body processing, and the working efficiency when improving assembling reduces production costs; Simultaneously, also can make things convenient for the transportation and the maximization of equipment, reduce cost of transportation.
Description of drawings
Fig. 1 is the sectional structure chart of a kind of combination type reactor of the utility model embodiment
Fig. 2 is an A-A place sectional structure chart among Fig. 1
Specific embodiments
Below in conjunction with accompanying drawing the utility model embodiment is described further:
Extremely shown in Figure 2 as Fig. 1, a kind of combination type reactor of the utility model, it includes reacting tank body 1, be provided with inlet, outlet pipe 11,12 and move thermal medium outside the described reacting tank body 1 into and out of tracheae 13,14, be provided with cold air distributing chamber 15, catalysis air-bed floor 16 and inert material chamber 17 in the described reacting tank body 1, described air inlet pipe 11 is arranged on the top of reacting tank body 1 and announces that with cold air chamber 15 communicates with moving thermal medium escape pipe 14, described escape pipe 12 and move bottom that thermal medium air inlet pipe 13 is arranged on reacting tank body 1 and communicate with inert material chamber 17; Be provided with heat exchanger tube 2 in the described beds 16, these heat exchanger tube 2 one ends put with in cold air is announced chamber 15 and with move thermal medium escape pipe 14 and be connected, its other end put with inert material chamber 17 in and with move thermal medium air inlet pipe 13 and be connected; In order to solve existing reactors is integral structure, the technical problems such as maximization that are unfavorable for assembling, transportation and the equipment of reactor, described reacting tank body 1 includes pressure cylinder 101, loam cake 102 and lower cover 103, and described pressure cylinder 101 seals by bolted with loam cake 102 and lower cover 103; Described pressure cylinder 101 two ends respectively are provided with a dividing plate 18 and make separate cold air announcement chamber 15, catalysis air-bed floor 16 and the inert material chamber 17 of formation in the reacting tank body 1; Change reacting tank body 1 into the branch body structure, not only can make things convenient for reacting tank body 1 processing, the working efficiency when improving assembling reduces production costs; Simultaneously, also can make things convenient for the transportation and the maximization of equipment, reduce cost of transportation.
In the present embodiment, for making things convenient for the processing assembling and transportation of heat exchanger tube 2, described heat exchanger tube 2 includes circle and moves heat pipe heat component 21 and rounded its many groups of fan-shaped heat pipe heat components 22 that move all around that are arranged in, described circle is moved the fan-shaped heat pipe heat component 22 that moves of heat pipe heat component 21 and many groups and is connected successively and communicates, heat exchanger tube 2 is made as the branch body structure, assembling and transportation that can more convenient reacting tank body 1, therefore, the embodiment of present embodiment be a preferred implementation.
In the present embodiment, for guaranteeing the heat exchange effect in the reacting tank body 1, described fan-shaped move heat pipe heat component 22 be provided with four groups and be evenly distributed on circle move heat pipe heat component 21 around, certainly, also can establish three groups or more, specifically being made as several groups can decide according to the actual requirements, and present embodiment is not further limited.
The foregoing description should not be considered as restriction of the present utility model, but any improvement of doing based on spirit of the present utility model, all should be within protection domain of the present utility model.
Claims (3)
1. combination type reactor, it includes reacting tank body, described reacting tank body is provided with the inlet, outlet pipe outward and moves thermal medium into and out of tracheae, described reacting tank body includes cold air distributing chamber, catalysis air-bed floor and inert material chamber, described air inlet pipe is arranged on the top of reacting tank body and announces that with cold air the chamber communicates with moving the thermal medium escape pipe, described escape pipe and move bottom that the thermal medium air inlet pipe is arranged on reacting tank body and communicate with the inert material chamber; Be provided with heat exchanger tube in the described beds, this heat exchanger tube one end put announce indoor with cold air and with move the thermal medium escape pipe and be connected, its other end put indoor with inert material and with move the thermal medium air inlet pipe and be connected; It is characterized in that described reacting tank body includes pressure cylinder and loam cake, lower cover, described pressure cylinder and loam cake and lower cover seal by bolted; Described pressure cylinder two ends respectively are provided with a dividing plate, make and form separate cold air announcement chamber, catalysis air-bed floor and inert material chamber in the reacting tank body.
2. a kind of combination type reactor according to claim 1, it is characterized in that described heat exchanger tube includes circle and moves heat pipe heat component and the rounded many groups of fan-shaped heat pipe heat components that move that are arranged in around it, described circle is moved the heat pipe heat component and is organized the fan-shaped heat pipe heat component that moves more and be connected successively and communicate.
3. a kind of combination type reactor according to claim 1 and 2, it is characterized in that described fan-shaped move the heat pipe heat component be provided with four groups and be evenly distributed on circle move the heat pipe heat component around.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200484697U CN201558691U (en) | 2009-10-22 | 2009-10-22 | Combined reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200484697U CN201558691U (en) | 2009-10-22 | 2009-10-22 | Combined reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201558691U true CN201558691U (en) | 2010-08-25 |
Family
ID=42623837
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200484697U Expired - Fee Related CN201558691U (en) | 2009-10-22 | 2009-10-22 | Combined reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201558691U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102059078A (en) * | 2010-11-19 | 2011-05-18 | 北京航天万源煤化工工程技术有限公司 | Isothermal radial converter |
-
2009
- 2009-10-22 CN CN2009200484697U patent/CN201558691U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102059078A (en) * | 2010-11-19 | 2011-05-18 | 北京航天万源煤化工工程技术有限公司 | Isothermal radial converter |
| CN102059078B (en) * | 2010-11-19 | 2013-06-19 | 航天长征化学工程股份有限公司 | Isothermal radial converter |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100825 Termination date: 20121022 |