CN202366704U - Heat exchange type stirring reaction kettle for processing calcium gluconate - Google Patents
Heat exchange type stirring reaction kettle for processing calcium gluconate Download PDFInfo
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- CN202366704U CN202366704U CN2011204858070U CN201120485807U CN202366704U CN 202366704 U CN202366704 U CN 202366704U CN 2011204858070 U CN2011204858070 U CN 2011204858070U CN 201120485807 U CN201120485807 U CN 201120485807U CN 202366704 U CN202366704 U CN 202366704U
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- kettle
- kettle body
- heat exchanger
- interlayer
- exchange type
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Abstract
The utility model discloses a heat exchange type stirring reaction kettle for processing calcium gluconate, which comprises a kettle body installed on a support. A barrel body integrally molded with the kettle body is installed on the circular wall of the kettle body, an interlayer is formed between the barrel body and the kettle body, heat conduction oil is filled in the interlayer, a heating rod is inserted in the heat conduction oil in the interlayer in reversed mode from the bottom, a motor is installed at the center of the top of the reaction kettle, the end of an output shaft of the motor is connected with a stirring shaft, a mansard stirring plate and a mansard stirring head are respectively installed at the upper end and the lower end of the stirring shaft, a feeding port is further arranged at the top of the kettle body, a discharging pipe is arranged at the bottom of the kettle body, and a control valve is installed on the discharging pipe. A heat exchanger which is lower than the height of the kettle body is installed on the support on one side of the kettle body, the upper portion of the heat exchanger is communicated with the side wall of the kettle body through a pipeline, and the bottom of the heat exchanger is communicated with the discharging pipe through a pipeline. The heat exchanger is installed on the outer side of the reaction kettle and matched with a clamping sleeve, thereby guaranteeing rapid and convenient heat exchange. In addition, a stirring device is reasonable in design and facilitates heat conduction.
Description
Technical field
The utility model relates to a kind of calcium gluconae processing technique field, specifically is that the exchange type stirred autoclave is used in a kind of calcium gluconae processing.
Background technology
Agitated reactor is the main devices that reacts between the raw material, and the reaction between the raw material usually is accompanied by the release of heat and absorbs heat from the external world to be carried out; For the common response still of needs coolings for generally being to cool off through chuck; And because the chuck area is limited, sometimes in some reactions, the heat exchange of this heat exchange reaction still requires not reach the reaction requirement; Temperature can not in time reduce; Bring many negative effects, usually by the effect of outer circulation pump with product pump in the container of outside, reach the purpose of cooling again.
In addition, in the agitated reactor the original design of agitating device unreasonable, cause the liquid heat conduction in the agitated reactor inhomogeneous, react insufficient.
Therefore, according to the demand in the actual process, the high agitated reactor of design one cover heat exchanger effectiveness is a problem demanding prompt solution.
The utility model content
The purpose of the utility model provides the processing of a kind of calcium gluconae to use the exchange type stirred autoclave, can solve that common response still heat exchange area is little, heat exchange efficiency is poor, stir inadequate problem.
The utility model technical solution problem provides following scheme:
The exchange type stirred autoclave is used in calcium gluconae processing, comprises the kettle that is installed on the support, and it is characterized in that: described kettle ring wall is equipped with the integrated cylindrical shell of kettle outward; Form interlayer between cylindrical shell and the kettle, falling heat-transfer oil has heating rod to be inserted into the conduction oil of interlayer from the bottom in the interlayer; Described kettle top center is equipped with motor; The output shaft end of motor is connected with shaft, and the upper and lower end of shaft outer wall is separately installed with the agitating plate and the stirring-head of broken line shape, and described kettle top also has charging aperture; Autoclave body bottom has discharge nozzle; Control valve is installed on the discharge nozzle, on the support of described kettle one side the heat exchanger that is lower than the kettle height is installed, heat exchanger top is connected through pipeline respectively with discharge nozzle with kettle sidewall, heat exchanger bottom.
The exchange type stirred autoclave is used in described calcium gluconae processing, it is characterized in that: the top of described agitated reactor also has looks the material hole.
The exchange type stirred autoclave is used in described calcium gluconae processing, it is characterized in that: evenly be furnished with pod apertures on the described agitating plate.
The advantage of the utility model:
The utility model is employed in the outer heat exchanger that is equipped with of agitated reactor, under the material in reactor effect of the temperature difference of portion within it, and produces a thermal cycle between the heat exchanger; Cooling reaches reaction requirements; Cooperate chuck, it is convenient and swift rapidly to guarantee simultaneously to heat up, in addition; Agitating device reasonable in design helps the conduction of heat more.
Description of drawings
Fig. 1 is the structural representation of the utility model.
The specific embodiment
Referring to accompanying drawing 1:
The exchange type stirred autoclave is used in calcium gluconae processing, comprises the kettle 2 that is installed on the support 1, and kettle 2 ring walls are equipped with the integrated cylindrical shell of kettle outward; Form interlayer 3 between cylindrical shell and the kettle, falling heat-transfer oil has heating rod 4 to be inserted into the conduction oil of interlayer 3 from the bottom in the interlayer 3; Kettle 2 top center are equipped with motor 5; The output shaft end of motor 5 is connected with shaft 6, and the upper and lower end of shaft 6 outer walls is separately installed with the agitating plate 7 and stirring-head 8 of broken line shape, and kettle 2 tops also have charging aperture 9; Kettle 2 bottoms have discharge nozzle 10; Control valve 11 is installed on the discharge nozzle 10, the heat exchanger 12 that is lower than the kettle height is installed on the support of kettle 2 one sides, heat exchanger 12 tops are connected through pipeline 13 respectively with discharge nozzle 10 with kettle 2 sidewalls, heat exchanger 12 bottoms.
The top of agitated reactor 2 also has looks material hole 14, is convenient to observe the liquid height in the kettle.
Evenly be furnished with pod apertures 15 on the agitating plate 7.
Claims (3)
1. the exchange type stirred autoclave is used in a calcium gluconae processing, comprises the kettle that is installed on the support, and it is characterized in that: described kettle ring wall is equipped with the integrated cylindrical shell of kettle outward; Form interlayer between cylindrical shell and the kettle, falling heat-transfer oil has heating rod to be inserted into the conduction oil of interlayer from the bottom in the interlayer; Described kettle top center is equipped with motor; The output shaft end of motor is connected with shaft, and the upper and lower end of shaft outer wall is separately installed with the agitating plate and the stirring-head of broken line shape, and described kettle top also has charging aperture; Autoclave body bottom has discharge nozzle; Control valve is installed on the discharge nozzle, on the support of described kettle one side the heat exchanger that is lower than the kettle height is installed, heat exchanger top is connected through pipeline respectively with discharge nozzle with kettle sidewall, heat exchanger bottom.
2. the exchange type stirred autoclave is used in calcium gluconae processing according to claim 1, it is characterized in that: the top of described agitated reactor also has looks the material hole.
3. the exchange type stirred autoclave is used in calcium gluconae processing according to claim 1, it is characterized in that: evenly be furnished with pod apertures on the described agitating plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204858070U CN202366704U (en) | 2011-11-30 | 2011-11-30 | Heat exchange type stirring reaction kettle for processing calcium gluconate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011204858070U CN202366704U (en) | 2011-11-30 | 2011-11-30 | Heat exchange type stirring reaction kettle for processing calcium gluconate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202366704U true CN202366704U (en) | 2012-08-08 |
Family
ID=46590429
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011204858070U Expired - Fee Related CN202366704U (en) | 2011-11-30 | 2011-11-30 | Heat exchange type stirring reaction kettle for processing calcium gluconate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202366704U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104492292A (en) * | 2015-01-08 | 2015-04-08 | 常州机电职业技术学院 | Random porous bent blade emulsifier for emulsified oil of diesel engine |
| CN106955657A (en) * | 2017-04-17 | 2017-07-18 | 姚莲琴 | A kind of Western medicine production and processing processes stirring reaction equipment with decoction |
-
2011
- 2011-11-30 CN CN2011204858070U patent/CN202366704U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104492292A (en) * | 2015-01-08 | 2015-04-08 | 常州机电职业技术学院 | Random porous bent blade emulsifier for emulsified oil of diesel engine |
| CN106955657A (en) * | 2017-04-17 | 2017-07-18 | 姚莲琴 | A kind of Western medicine production and processing processes stirring reaction equipment with decoction |
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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: 20120808 Termination date: 20141130 |
|
| EXPY | Termination of patent right or utility model |