CN203043978U - Temperature adjustment system of defoamer reaction kettle - Google Patents
Temperature adjustment system of defoamer reaction kettle Download PDFInfo
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- CN203043978U CN203043978U CN 201320065460 CN201320065460U CN203043978U CN 203043978 U CN203043978 U CN 203043978U CN 201320065460 CN201320065460 CN 201320065460 CN 201320065460 U CN201320065460 U CN 201320065460U CN 203043978 U CN203043978 U CN 203043978U
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- temperature heat
- reaction kettle
- conduction oil
- heat conductive
- heat conduction
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Abstract
The utility model relates to the field of chemical engineering equipment, and discloses a temperature adjustment system of a defoamer reaction kettle. The temperature adjustment system comprises the reaction kettle 1, a temperature control coil pipe 2, a high temperature heat conduction oil inlet valve 3, a low temperature heat conduction oil inlet valve 4, a pump 5, a high temperature heat conduction oil backflow valve 6, a low temperature heat conduction oil backflow valve 7, a cooling tower 8, a T-joint device 9, a heating furnace 10, pipelines 11 and an oil storage pool 12, wherein the temperature control coil pipe 2 is arranged on the inner wall of the reaction kettle 1; and an inlet pipeline of the temperature control coil pipe 2 is connected with the high temperature heat conduction oil inlet valve 3 and the low temperature heat conduction oil inlet valve 4. By utilizing the technical scheme, giant energy can be generated in actual application; temperature in the reaction kettle is precisely controlled; the temperature in the defoamer reaction kettle is controlled by high temperature heat conduction oil and low temperature heat conduction oil which flow in the temperature control coil pipe; the conventional external spraying cooling mode is replaced; water resources are greatly saved; and the energy utilization rate is improved.
Description
Technical field
The utility model relates to the chemical industry equipment field, relates in particular to a kind of defoamer temperature of reaction kettle regulating system.
Background technology
Reactor is the important device in the defoamer production process, and defoamer is produced the required chemical reaction that carries out, coupling is finished in reactor mostly.At present most reactor adopts the naked light heating, and the efficiency of heating surface is low and have a potential safety hazard; And having many defoamer reactors to adopt outside spray that reactor is cooled off, cooling effect is poor, can't accurately control defoamer reactor temperature inside, thereby influence efficient and quality that defoamer is produced.
The utility model content
In order to solve above technical problem, the utility model provides a kind of defoamer temperature of reaction kettle regulating system, reactor, temperature control coil pipe, high temperature heat conductive oil inlet valve, low temperature heat conductive oil inlet valve, pump, high temperature heat conductive oil return valve, low temperature conduction oil return valve, cooling tower, three-way device, heating furnace, pipeline and oil storage pool.
Described reactor inwall is provided with temperature control coil pipe.
The inlet ductwork of described temperature control coil pipe is connected with high temperature heat conductive oil inlet valve and low temperature heat conductive oil inlet valve.
Described temperature control coil pipe export pipeline is connected with high temperature heat conductive oil return valve and low temperature conduction oil return valve.
Described high temperature heat conductive oil inlet valve is connected with heating furnace by pump.
Described low temperature heat conductive oil inlet valve is connected to oil storage pool by pump.
Described high temperature heat conductive oil return valve is connected to three-way device.
Described low temperature conduction oil return valve is connected to cooling tower.
Described three-way device connects heating furnace and oil storage pool.
Described cooling tower and heating furnace all are connected to oil storage pool.
The utility model compared with prior art has following beneficial effect:
The utility model provides a kind of defoamer temperature of reaction kettle regulating system, the control of reactor internal temperature is more accurate, control defoamer reactor temperature inside with the high and low temperature conduction oil that flows in the temperature control coil pipe, substitute the type of cooling of traditional outside spray, saved great amount of water resources; 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
Accompanying drawing described herein is used to provide further understanding of the present utility model, constitutes the application's a part, does not constitute to improper restriction of the present utility model, in the accompanying drawings:
Fig. 1 is the utility model structural representation;
The specific embodiment
Describe the utility model in detail below in conjunction with accompanying drawing and specific embodiment, be used for explaining the utility model in this illustrative examples of the present utility model and explanation, but not as to restriction of the present utility model.
Present embodiment provides a kind of temperature of reaction kettle regulating system, structure comprises reactor 1, temperature control coil pipe 2, high temperature heat conductive oil inlet valve 3, low temperature heat conductive oil inlet valve 4, pump 5, high temperature heat conductive oil return valve 6, low temperature conduction oil return valve 7, cooling tower 8, three-way device 9, heating furnace 10, pipeline 11 and oil storage pool 12 as shown in Figure 1.Described reactor 1 inwall is provided with temperature control coil pipe 2.The inlet ductwork of described temperature control coil pipe 2 is connected with high temperature heat conductive oil inlet valve 3 and low temperature heat conductive oil inlet valve 4.Described temperature control coil pipe 2 export pipelines are connected with high temperature heat conductive oil return valve 6 and low temperature conduction oil return valve 7.Described high temperature heat conductive oil inlet valve 3 is connected with heating furnace 10 by pump 5.Described low temperature heat conductive oil inlet valve 4 is connected to oil storage pool 12 by pump 5.Described high temperature heat conductive oil return valve 6 is connected to three-way device 9.Described low temperature conduction oil return valve 7 is connected to cooling tower 8.Described three-way device 9 connects heating furnace 10 and oil storage pool 12.Described cooling tower 8 all is connected to oil storage pool 12 with heating furnace 10.
In the time of need heating reactor 1 inside, open high temperature heat conductive oil inlet valve 3 and high temperature heat conductive oil return valve 6, close low temperature heat conductive oil inlet valve 4 and low temperature conduction oil return valve 7, the high temperature heat conductive oil that flowing at this moment in the temperature control coil pipe 2, reactor 1 internal temperature can raise; In the time of need be to reactor 1 internal cooling, open low temperature heat conductive oil inlet valve 4 and low temperature conduction oil return valve 7, close high temperature heat conductive oil inlet valve 3 and high temperature heat conductive oil return valve 6, the low temperature conduction oil that flowing in the temperature control coil pipe 2, reactor 1 internal temperature can reduce.During reactor 1 inner the heating, three-way device 9 can be back to high temperature heat conductive oil heating furnace 10 or oil storage pool 12 as required, has improved energy utilization ratio.This defoamer temperature of reaction kettle regulating system adopts the low temperature conduction oil that flows in the temperature control coil pipe that 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.
More than technical scheme that the utility model embodiment is provided be described in detail, used specific case herein principle and the embodiment of the utility model embodiment are set forth, the explanation of above embodiment only is applicable to the principle that helps to understand the utility model embodiment; Simultaneously, for one of ordinary skill in the art, according to the utility model embodiment, the part that on the specific embodiment and range of application, all can change, in sum, this description should not be construed as restriction of the present utility model.
Claims (4)
1. defoamer temperature of reaction kettle regulating system, reactor, temperature control coil pipe, high temperature heat conductive oil inlet valve, low temperature heat conductive oil inlet valve, pump, high temperature heat conductive oil return valve, low temperature conduction oil return valve, cooling tower, three-way device, heating furnace, pipeline and oil storage pool is characterized in that: described reactor inwall is provided with temperature control coil pipe.
2. a kind of defoamer temperature of reaction kettle regulating system according to claim 1 is characterized in that: the inlet ductwork of described temperature control coil pipe is connected with high temperature heat conductive oil inlet valve and low temperature heat conductive oil inlet valve; Described temperature control coil pipe export pipeline is connected with high temperature heat conductive oil return valve and low temperature conduction oil return valve.
3. a kind of defoamer temperature of reaction kettle regulating system according to claim 2, it is characterized in that: described high temperature heat conductive oil inlet valve is connected with heating furnace by pump, described low temperature heat conductive oil inlet valve is connected to oil storage pool by pump, described high temperature heat conductive oil return valve is connected to three-way device, and described low temperature conduction oil return valve is connected to cooling tower.
4. a kind of defoamer temperature of reaction kettle regulating system according to claim 3 is characterized in that: described three-way device connects heating furnace and oil storage pool, and described cooling tower and heating furnace all are connected to oil storage pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320065460 CN203043978U (en) | 2013-01-22 | 2013-01-22 | Temperature adjustment system of defoamer reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320065460 CN203043978U (en) | 2013-01-22 | 2013-01-22 | Temperature adjustment system of defoamer reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203043978U true CN203043978U (en) | 2013-07-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320065460 Expired - Fee Related CN203043978U (en) | 2013-01-22 | 2013-01-22 | Temperature adjustment system of defoamer reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203043978U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551079A (en) * | 2013-10-16 | 2014-02-05 | 科迈化工股份有限公司 | Reaction kettle device capable of controlling synthesis temperature of accelerant 2-mercaptobenzothiazole (MBT) |
| CN112958018A (en) * | 2021-03-03 | 2021-06-15 | 康盈红莓(中山)生物科技有限公司 | Electromagnetic reaction device, equipment and temperature control method thereof and device manufacturing method |
-
2013
- 2013-01-22 CN CN 201320065460 patent/CN203043978U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103551079A (en) * | 2013-10-16 | 2014-02-05 | 科迈化工股份有限公司 | Reaction kettle device capable of controlling synthesis temperature of accelerant 2-mercaptobenzothiazole (MBT) |
| CN112958018A (en) * | 2021-03-03 | 2021-06-15 | 康盈红莓(中山)生物科技有限公司 | Electromagnetic reaction device, equipment and temperature control method thereof and device manufacturing method |
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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: 20130710 Termination date: 20210122 |
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| CF01 | Termination of patent right due to non-payment of annual fee |