CN202427432U - Temperature regulation system for reaction kettle - Google Patents
Temperature regulation system for reaction kettle Download PDFInfo
- Publication number
- CN202427432U CN202427432U CN2011205203339U CN201120520333U CN202427432U CN 202427432 U CN202427432 U CN 202427432U CN 2011205203339 U CN2011205203339 U CN 2011205203339U CN 201120520333 U CN201120520333 U CN 201120520333U CN 202427432 U CN202427432 U CN 202427432U
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- temperature
- temperature heat
- heat transfer
- heating furnace
- heat conductive
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Abstract
The utility model relates to a temperature regulation system for a reaction kettle. The temperature regulation system comprises a reaction kettle, a heating furnace, a cooling tower, an oil reservoir, pumps, valves and pipelines, wherein a temperature control coil is arranged in the reaction kettle; the inlet pipeline of the temperature control coil is connected with a high-temperature heat transfer oil inlet valve and a low-temperature heat transfer oil inlet valve; the high-temperature heat transfer oil inlet valve is connected with the heating furnace through one of the pumps; the heating furnace is connected with the oil reservoir; the low-temperature heat transfer oil inlet valve is connected with the oil reservoir through the other pump; the outlet pipeline of the temperature control coil is connected with a high-temperature heat transfer oil return valve and a low-temperature heat transfer oil return valve; the high-temperature heat transfer oil return valve is connected with a three-way device; the three-way device is connected with the heating furnace and the oil reservoir; the low-temperature heat transfer oil return valve is connected with the cooling tower; and the cooling tower is connected with the oil reservoir. The temperature regulation system has a scientific and reasonable structural design; high-temperature or low-temperature oil flows in the temperature control coil according to the requirement for internal temperature of the reaction kettle, so that the temperature control is more accurate and water resources are saved; and the energy utilization rate can be improved.
Description
Technical field
The utility model relates to the chemical plant installations field, particularly a kind of temperature of reaction kettle regulating system.
Background technology
Agitated reactor is that chemical enterprise is used comparatively general device, and various raw materials carry out chemical reaction, coupling is accomplished in agitated reactor mostly.At present a lot of agitated reactors adopts the naked lights heating, and the efficiency of heating surface is low and have a potential safety hazard; And have many agitated reactors just agitated reactor to be cooled off with outside spray, and cooling effect is poor, and agitated reactor internal temperature control accuracy is low, and water resource waste is more serious.
Summary of the invention
The purpose of the utility model is to overcome the deficiency of prior art, and a kind of reasonable in design is provided, and capacity usage ratio is high, the temperature of reaction kettle regulating system that agitated reactor internal temperature control accuracy is high.
The utility model solves its technical problem and realizes through following technical scheme:
A kind of temperature of reaction kettle regulating system comprises agitated reactor, it is characterized in that: also comprise heating furnace, cooling tower, oil storage pool, pump, valve, pipeline; In the agitated reactor set inside temperature control coil pipe is arranged; The inlet ductwork of temperature control coil pipe is connected with high temperature heat conductive oil inlet valve and low temperature heat conductive oil inlet valve, and the high temperature heat conductive oil inlet valve is connected with heating furnace through pump, and heating furnace is connected to oil storage pool; Low temperature heat conductive oil inlet valve is connected to oil storage pool through pump; Temperature control coil pipe export pipeline is connected with high temperature heat conductive oil return valve and low temperature conduction oil return valve, and the high temperature heat conductive oil return valve is connected to three-way device, and three-way device connects heating furnace and oil storage pool; Low temperature conduction oil return valve is connected to cooling tower, and cooling tower is connected to oil storage pool.
Advantage of the utility model and beneficial effect are:
The utility model scientific structure design is reasonable, needs according to the agitated reactor internal temperature, and the high and low temperature conduction oil that flows in the temperature control coil pipe, agitated reactor need not adopt traditional outside spray cooling, and the control of agitated reactor internal temperature is more accurate, has saved water resource; And on the high temperature heat conductive oil return line three-way device is set, and can as required high temperature heat conductive oil be back to heating furnace or oil storage pool, improved energy utilization ratio.
Description of drawings
Fig. 1 is the structural representation of the utility model.
The specific embodiment
Through specific embodiment the utility model is done further to detail below, following examples are descriptive, are not determinate, can not limit the protection domain of the utility model with this.
A kind of temperature of reaction kettle regulating system comprises agitated reactor 1, and its innovation part is: also comprise heating furnace 10, cooling tower 8, oil storage pool 12, pump 5, valve, pipeline 11; In described agitated reactor set inside temperature control coil pipe 2 is arranged; The inlet ductwork of temperature control coil pipe is connected with high temperature heat conductive oil inlet valve 3 and low temperature heat conductive oil inlet valve 4, and the high temperature heat conductive oil inlet valve is connected with heating furnace through pump, and heating furnace is connected to oil storage pool; Low temperature heat conductive oil inlet valve is connected to oil storage pool through pump; Temperature control coil pipe export pipeline is connected with high temperature heat conductive oil return valve 6 and low temperature conduction oil return valve 7, and the high temperature heat conductive oil return valve is connected to three-way device 9, and three-way device connects heating furnace and oil storage pool; Low temperature conduction oil return valve is connected to cooling tower, and cooling tower is connected to oil storage pool.In the time of need heating agitated reactor inside; Open high temperature heat conductive oil inlet valve and high temperature heat conductive oil return valve; Close low temperature heat conductive oil inlet valve and low temperature conduction oil return valve, what flowed this moment in the temperature control coil pipe is high temperature heat conductive oil, and the agitated reactor internal temperature can raise; Otherwise what flow in the temperature control coil pipe is the low temperature conduction oil, and the agitated reactor internal temperature can reduce.When heated agitated reactor inside, the three-way device on the high temperature heat conductive oil return line can be back to heating furnace or oil storage pool with high temperature heat conductive oil as required, has improved energy utilization ratio.This temperature of reaction kettle regulating system adopts the low temperature conduction oil that flows in the temperature control coil pipe that agitated reactor inside is cooled off, and outside spray type of cooling temperature control more in the past is more accurate, and has saved water resource.
Claims (1)
1. a temperature of reaction kettle regulating system comprises agitated reactor, it is characterized in that: also comprise heating furnace, cooling tower, oil storage pool, pump, valve, pipeline; In the agitated reactor set inside temperature control coil pipe is arranged; The inlet ductwork of temperature control coil pipe is connected with high temperature heat conductive oil inlet valve and low temperature heat conductive oil inlet valve, and the high temperature heat conductive oil inlet valve is connected with heating furnace through pump, and heating furnace is connected to oil storage pool; Low temperature heat conductive oil inlet valve is connected to oil storage pool through pump; Temperature control coil pipe export pipeline is connected with high temperature heat conductive oil return valve and low temperature conduction oil return valve, and the high temperature heat conductive oil return valve is connected to three-way device, and three-way device connects heating furnace and oil storage pool; Low temperature conduction oil return valve is connected to cooling tower, and cooling tower is connected to oil storage pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205203339U CN202427432U (en) | 2011-12-13 | 2011-12-13 | Temperature regulation system for reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205203339U CN202427432U (en) | 2011-12-13 | 2011-12-13 | Temperature regulation system for reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202427432U true CN202427432U (en) | 2012-09-12 |
Family
ID=46776909
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205203339U Expired - Fee Related CN202427432U (en) | 2011-12-13 | 2011-12-13 | Temperature regulation system for reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202427432U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103537240A (en) * | 2013-10-16 | 2014-01-29 | 科迈化工股份有限公司 | Rubber vulcanized accelerator 2-mercaptobenzothiazole MBT reaction temperature control device |
| CN107824129A (en) * | 2017-12-04 | 2018-03-23 | 陕西盟创纳米新型材料股份有限公司 | A kind of drying system of alcohol supercritical methanol technology production aeroge |
| CN110117360A (en) * | 2019-06-25 | 2019-08-13 | 福建中庚环境技术有限公司 | A kind of MC nylon industry metaplasia production complete set of equipments |
| CN112808168A (en) * | 2021-03-14 | 2021-05-18 | 北京四维天拓技术有限公司 | Composite heating hydrothermal reaction device and composite heating method thereof |
-
2011
- 2011-12-13 CN CN2011205203339U patent/CN202427432U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103537240A (en) * | 2013-10-16 | 2014-01-29 | 科迈化工股份有限公司 | Rubber vulcanized accelerator 2-mercaptobenzothiazole MBT reaction temperature control device |
| CN107824129A (en) * | 2017-12-04 | 2018-03-23 | 陕西盟创纳米新型材料股份有限公司 | A kind of drying system of alcohol supercritical methanol technology production aeroge |
| CN107824129B (en) * | 2017-12-04 | 2024-03-12 | 陕西盟创纳米新型材料股份有限公司 | Drying system for producing aerogel by alcohol supercritical method |
| CN110117360A (en) * | 2019-06-25 | 2019-08-13 | 福建中庚环境技术有限公司 | A kind of MC nylon industry metaplasia production complete set of equipments |
| CN112808168A (en) * | 2021-03-14 | 2021-05-18 | 北京四维天拓技术有限公司 | Composite heating hydrothermal reaction device and composite heating method thereof |
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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: 20120912 Termination date: 20121213 |