CN206778435U - Strengthen stirring radiating reactor - Google Patents
Strengthen stirring radiating reactor Download PDFInfo
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- CN206778435U CN206778435U CN201720661747.0U CN201720661747U CN206778435U CN 206778435 U CN206778435 U CN 206778435U CN 201720661747 U CN201720661747 U CN 201720661747U CN 206778435 U CN206778435 U CN 206778435U
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Abstract
One kind strengthens stirring radiating reactor,Housing and several internal heat exchange pipelines including reactor,The both ends of the reactor are round end structure,Middle part is columnar structured,Several heat exchange pipeline both ends are connected to support disk body,Region is heat transfer zone between two support disk bodies and the middle part of reactor,It is material Flip Zone to support between disk body and the round end at reactor both ends,The support disk body at heat exchange pipeline both ends through both ends connects with the both ends material Flip Zone of reactor,Cylinder is provided with the round end of bottom,The cylinder one end is connected with support disk body,The cylinder other end through and out reactor round end and be connected thereto,The side wall that cylinder is located at the part in round end is provided with return port,Material extruding propeller is provided with the cylinder,The utility model is using shell-and-tube heat exchanger as agent structure,Increase motive force of the spiral propeller as extruding,Extruding material,Action of forced stirring is realized during upset,Stirring and radiating are integrated.
Description
Technical field
The technical field of the reactor in agricultural chemicals pharmaceutical equipment is the utility model is related to, strengthens stirring more particularly to one kind
Radiate reactor.
Background technology
In the prior art, the reactor of pharmaceutical purpose, it is largely the structure of pot type, its one agitator of internal increase is right
Reaction mass is stirred, and this kind of reactor is applicable generally be directed to the small material of some reaction caloric values, for some reactions
Caloric value it is big, it is necessary to which the material of timely radiating is just not suitable for, it is necessary to install the structure of radiating additional, be largely intercalated water sleeve
Structure, also there is the structure in reactor external heat exchanger, exist radiating rate it is slow, not in time the problem of, especially for one
A bit as the reaction mass of pureed, viscosity beats that big stirring difficulty is big, and radiating contact surface is small, and this kind of reactor can not be applied substantially,
Have much room for improvement.
Utility model content
To solve the above problems, the purpose of this utility model is to propose that a kind of strengthen stirs radiating reactor.
The technical solution of the utility model is as follows：One kind strengthens stirring radiating reactor, including the housing of reactor and interior
Several heat exchange pipelines in portion, it is characterized in that：The both ends of the reactor are round end structure, middle part be it is columnar structured, it is described
Several heat exchange pipeline both ends are connected to support disk body, and region is heat exchange between two support disk bodies and the middle part of reactor
Area, it is material Flip Zone to support between disk body and the round end at reactor both ends, and described heat exchange pipeline both ends pass through the branch at both ends
Support plate body is connected with the both ends material Flip Zone of reactor, and cylinder is provided with the round end of bottom, the cylinder one end and branch
Support plate body connect, the cylinder other end through and out reactor round end and be connected thereto, cylinder is located at the portion in round end
The side wall divided is provided with return port, and material extruding propeller is provided with the cylinder, promotes material to be entered by cylinder and changes
In heat pipe, the partial sidewall that cylinder is located at outside round end is provided with material inlet/outlet pipe and its valve, on the top of the round end on top
Provided with blast pipe and its valve.
Preferably, described extruding propeller is a spiral propeller, passes through bearing in the rotating shaft of the spiral propeller
The capping matched with described cylinder is set with, the external port of closed cylinder is capable of in capping.
Preferably, number of the number of the heat exchanger tube on the inside of described cylinder less than heat exchanger tube on the outside of cylinder.
Preferably, the both sides of the heat transfer zone of described reactor housing are respectively equipped with the inlet and outlet of heat transferring medium.
It is of the present utility model to have the technical effect that：
The reinforcing stirring radiating reactor of the utility model, pushed away using shell-and-tube heat exchanger as agent structure, increase spiral
Enter motive force of the device as extruding, material is realized action of forced stirring during extruding, upset, can when it passes through heat exchanger tube
Timely radiate, stirring and radiating are integrated.
Brief description of the drawings
Fig. 1 is the cross-sectional view of reinforcing stirring radiating reactor；
Fig. 1 materials Flip Zones, the round end of 2. reactors, the cylinder of 3. reactors, the heat transferring medium of 4. heat exchanger tube 5. enter
Mouth, 6. spiral propellers, 7. material import and exports, 8. cappings, the rotating shaft of 9. spiral propellers, 10. return ports, 11. cylinders, 12.
Support disk body, the outlet of 13. heat transferring mediums, 14. support disk bodies, 15. feed and exhaust tubes and its valve, 16. blast pipes and its valve.
Embodiment
It is new to this practicality below in conjunction with accompanying drawing 1 to make the purpose of this utility model, technical scheme and advantage clearer
Type embodiment is described in further detail.
Embodiment one：Referring to Fig. 1, one kind strengthens stirring radiating reactor, including the housing of reactor and internal some
Individual heat exchange pipeline, it is characterized in that：The both ends of the reactor are round end structure, and middle part is columnar structured, and several described change
Hot channel both ends are connected to support disk body, and region is heat transfer zone between two support disk bodies and the middle part of reactor, support
Be material Flip Zone between disk body and the round end at reactor both ends, described heat exchange pipeline both ends through both ends support disk body with
The both ends material Flip Zone connection of reactor, is provided with cylinder on the round end of bottom, and the cylinder one end connects with support disk body
Connect, the cylinder other end through and out reactor round end and be connected thereto, cylinder is located at the side wall of the part in round end
Return port is provided with, material extruding propeller is provided with the cylinder, promotes material to be entered by cylinder in heat exchanger tube, circle
The partial sidewall that cylinder is located at outside round end is provided with material inlet/outlet pipe and its valve, and the lower end of cylinder is provided with capping, screw propulsion
The rotating shaft of device passes the capping and installed by bearing, and blast pipe and its valve are provided with the top of the round end on top.
Described extruding propeller is a spiral propeller, in the rotating shaft of the spiral propeller by bearing holder (housing, cover) be equipped with
The external port of closed cylinder is capable of in the capping of described cylinder matching, capping.
The number of heat exchanger tube on the inside of described cylinder is less than the number of heat exchanger tube on the outside of cylinder, because outside heat exchanger tube is
Return duct, there is no power in reflux course, flow velocity reduces, it is necessary to which more pipelines could meet with middle part by spiral propeller
The flow matches of the pipeline of extruding.
The both sides of described heat transfer zone are respectively equipped with the inlet and outlet of heat transferring medium, and heat transferring medium flows through outside pipe, energy
It is enough to cool in time to pipe.
The course of work：
When the reactor works, first by the reaction mass of flow-like through in material inlet/outlet pipe input road reactor, beating simultaneously
Open the drain tap on top, discharge the gas in reactor, by being pressed into inside heat exchanger tube for lower part helical propeller,
Then enter the material Flip Zone of the other end of reactor through heat exchanger tube, when the material in area to be flipped is filled substantially with, close
Top air bleeding valve, when the material in area to be flipped reaches a certain amount of, its internal material will be back to down along the heat exchanger tube in outside
In the Flip Zone at end, action of forced stirring is carried out in itself to material during above-mentioned extruding and upset, material is fully contacted,
The reaction effect of improving material, then it is re-introduced into the extruding of spiral propeller position progress again through return port and promotes, such as
This can extrude and overturn repeatedly, and compulsory to material progress to be sufficiently stirred, material every time all can be with heat transferring medium by heat exchanger tube
Heat exchange is carried out, in time radiating, heat transfer rate can be controlled by adjusting the flow velocity for the heat transferring medium that flow through heat transfer zone.Treat anti-
After the completion of answering, stop spiral propeller, open the valve of the material inlet/outlet pipe of bottom, material under gravity, is flowed out, beaten
Open air bleeding valve above can supplies flow down.
Claims (4)
1. one kind strengthens stirring radiating reactor, including the housing of reactor and several internal heat exchange pipelines, it is characterized in that：
The both ends of the reactor are round end structure, and middle part is columnar structured, and several described heat exchange pipeline both ends are connected to
Disk body is supported, region is heat transfer zone between two support disk bodies and the middle part of reactor, support disk body and the circle at reactor both ends
It is material Flip Zone between head, described heat exchange pipeline both ends are overturn through the support disk body at both ends and the both ends material of reactor
Area is connected, and cylinder is provided with the round end of bottom, and the cylinder one end is connected with support disk body, and the cylinder other end is through simultaneously
Stretch out the round end of reactor and be connected thereto, the side wall that cylinder is located at the part in round end is provided with return port, in the cylinder
Material extruding propeller is provided with vivo, promotes material to be entered by cylinder in heat exchanger tube, cylinder is located at the part outside round end
Side wall is provided with material inlet/outlet pipe and its valve, and blast pipe and its valve are provided with the top of the round end on top.
2. according to claim 1 strengthen stirring radiating reactor, it is characterized in that：Described extruding propeller is a spiral
Propeller, the capping matched with described cylinder is equipped with the rotating shaft of the spiral propeller by bearing holder (housing, cover), and capping can seal
Close the external port of cylinder.
3. according to claim 1 strengthen stirring radiating reactor, it is characterized in that：Heat exchanger tube on the inside of described cylinder
Number of the number less than heat exchanger tube on the outside of cylinder.
4. according to claim 1 strengthen stirring radiating reactor, it is characterized in that：The heat transfer zone of described reactor housing
Both sides be respectively equipped with the inlet and outlet of heat transferring medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720661747.0U CN206778435U (en) | 2017-06-08 | 2017-06-08 | Strengthen stirring radiating reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720661747.0U CN206778435U (en) | 2017-06-08 | 2017-06-08 | Strengthen stirring radiating reactor |
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| Publication Number | Publication Date |
|---|---|
| CN206778435U true CN206778435U (en) | 2017-12-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720661747.0U Active CN206778435U (en) | 2017-06-08 | 2017-06-08 | Strengthen stirring radiating reactor |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113967455A (en) * | 2021-09-28 | 2022-01-25 | 杨建淅 | Methane hydrochlorination reactor |
| CN116764560A (en) * | 2022-03-15 | 2023-09-19 | 黄毅 | Methane hydrochlorination reactor |
| CN117816081A (en) * | 2024-02-28 | 2024-04-05 | 洛阳仁晟石化工程技术有限公司 | High-efficient reation kettle quick temperature regulating mechanism |
-
2017
- 2017-06-08 CN CN201720661747.0U patent/CN206778435U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113967455A (en) * | 2021-09-28 | 2022-01-25 | 杨建淅 | Methane hydrochlorination reactor |
| CN116764560A (en) * | 2022-03-15 | 2023-09-19 | 黄毅 | Methane hydrochlorination reactor |
| CN117816081A (en) * | 2024-02-28 | 2024-04-05 | 洛阳仁晟石化工程技术有限公司 | High-efficient reation kettle quick temperature regulating mechanism |
| CN117816081B (en) * | 2024-02-28 | 2024-05-14 | 洛阳仁晟石化工程技术有限公司 | High-efficient reation kettle quick temperature regulating mechanism |
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