CN203018067U - Stratification heat type reaction kettle - Google Patents
Stratification heat type reaction kettle Download PDFInfo
- Publication number
- CN203018067U CN203018067U CN 201220671202 CN201220671202U CN203018067U CN 203018067 U CN203018067 U CN 203018067U CN 201220671202 CN201220671202 CN 201220671202 CN 201220671202 U CN201220671202 U CN 201220671202U CN 203018067 U CN203018067 U CN 203018067U
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- oil
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- flow control
- interlayer
- sensing device
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Abstract
The utility model relates to a stratification heat type reaction kettle and belongs to the field of chemical equipment. The stratification heat type reaction kettle comprises a kettle body 1 and a stirrer 2, wherein the kettle body 1 is provided with a plurality of interlayers which are annular hollow cavities; an oil conduit is spirally arranged in each hollow cavity; the oil conduit of each interlayer is connected to an oil amount control device of the kettle body 1; the oil amount control device is connected to a conduction oil heating device through a pipeline to form a conduction oil circulating system; and each interlayer in the kettle body 1 is provided with a temperature sensing device and is connected with the oil amount control device in a matching way. In the heating process, heat conduction oil is divided into multiple layers to heat the interior of the cavitiesy of the reaction kettle uniformly; and the stratification heat type reaction kettle is simple and reasonable in structure and efficient and energy-saving.
Description
Technical field
The utility model relates to a kind of layer of hot type reactor, and it belongs to the chemical industry equipment field.
Background technology
In chemical engineering industry the application of reactor is very extensive, need to carry out to reactor the reaction process of its material by different temperature.Open firing seriously polluted, the inequality of being heated, and electric heating equipment is complicated, in use, danger coefficient is larger.The applicable elements of above-mentioned dual mode has requirement, can not be to the heating of flammable materials.The heat conducting oil type mode of heating is heated evenly, the flames of anger, safety and environmental protection.But conduction oil need continue circulation, in heating process, the heat conducting oil pipe of reactor intraformational bed from top to bottom, or circulation from bottom to top causes reactor top and the bottom temperature uneven.
Summary of the invention
In view of the defective that prior art exists, order of the present utility model is to provide a kind of layer of hot type reactor, and in heating process, conduction oil is divided into multilayer and heats in the reactor chamber, and it is heated evenly, and is simple and reasonable, energy-efficient.
For achieving the above object, the technical solution that adopts of the utility model is
A kind of layer of hot type reactor, comprise kettle 1, agitator 2, kettle 1 is provided with several interlayers, interlayer is toroidal cavity, and the cavity inside turn arranges oil guide pipe, and the oil guide pipe of each interlayer is connected to the oil-flow control apparatus of kettle 1, oil-flow control apparatus is connected to hot oil heater by pipeline again, consists of the conduction oil circulatory system; In kettle 1, each interlayer is provided with temperature sensing device, and is connected supporting with oil-flow control apparatus.Described interlayer is divided into interlayer 5, middle interlayer 4, lower interlayer 3, temperature sensing device 5.1, middle temperature sensing device 5.2, lower temperature sensing device 5.3 are set separately, the upper oil-flow control apparatus 5.2 supporting with it, middle oil-flow control apparatus 4.2, lower oil-flow control apparatus 3.2 on it; Each oil-flow control apparatus access hot oil heater.Described temperature sensing device and oil-flow control apparatus access self-con-tained unit according to the temperature that temperature sensing device is measured, are controlled the flow of conduction oil by oil-flow control apparatus, adjust each subregion temperature.
After adopting such scheme, compared with prior art have following beneficial effect: in heating process of the present utility model, conduction oil is divided into multilayer and heats in the reactor chamber, and it is heated evenly, and is simple and reasonable, energy-efficient.
Description of drawings
Fig. 1 is the structural representation of a kind of layer of hot type reactor.
In figure: 1, kettle, 2, agitator, 3, lower interlayer, 3.1, lower temperature sensing device, 3.2, lower oil-flow control apparatus, 4, middle interlayer, 4.1, middle temperature sensing device, 4.2, middle oil-flow control apparatus, 5, upper interlayer, 5.1, upper temperature sensing device, 5.2, upper oil-flow control apparatus.
The specific embodiment
Following the utility model is described further in connection with embodiment:
A kind of layer of hot type reactor, comprise kettle 1, agitator 2, it is characterized in that: if kettle 1 is provided with three interlayers, interlayer is toroidal cavity, and the cavity inside turn arranges oil guide pipe, and the oil guide pipe of each interlayer is connected to the oil-flow control apparatus of kettle 1, oil-flow control apparatus is connected to hot oil heater by pipeline again, consists of the conduction oil circulatory system; Described interlayer is divided into interlayer 5, middle interlayer 4, lower interlayer 3, temperature sensing device 5.1, middle temperature sensing device 4.1, lower temperature sensing device 3.1 are set separately, the upper oil-flow control apparatus 5.2 supporting with it, middle oil-flow control apparatus 4.2, lower oil-flow control apparatus 3.2 on it; Each oil-flow control apparatus access hot oil heater.Described temperature sensing device and oil-flow control apparatus access self-con-tained unit according to the temperature that temperature sensing device is measured, are controlled the flow of conduction oil by oil-flow control apparatus, adjust each subregion temperature.
Reactor is in heating process, and conduction oil is divided into three layers and heats in the reactor chamber, and it is heated evenly, and is simple and reasonable, energy-efficient.
Claims (3)
1. layer hot type reactor, comprise kettle (1), agitator (2), it is characterized in that: kettle (1) is provided with several interlayers, interlayer is toroidal cavity, and the cavity inside turn arranges oil guide pipe, and the oil guide pipe of each interlayer is connected to the oil-flow control apparatus of kettle (1), oil-flow control apparatus is connected to hot oil heater by pipeline again, consists of the conduction oil circulatory system; In kettle (1), each interlayer is provided with temperature sensing device, and is connected supporting with oil-flow control apparatus.
2. a kind of layer of hot type reactor according to claim 1, it is characterized in that: described interlayer is divided into interlayer (5), middle interlayer (4), lower interlayer (3), temperature sensing device (5.1), middle temperature sensing device (4.1), lower temperature sensing device (3.1) are set separately, the upper oil-flow control apparatus (5.2) supporting with it, middle oil-flow control apparatus (4.2), lower oil-flow control apparatus (3.2) on it; Each oil-flow control apparatus access hot oil heater.
3. a kind of layer of hot type reactor according to claim 1, it is characterized in that: described temperature sensing device and oil-flow control apparatus access self-con-tained unit, according to the temperature that temperature sensing device is measured, control the flow of conduction oil by oil-flow control apparatus, adjust each subregion temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220671202 CN203018067U (en) | 2012-12-09 | 2012-12-09 | Stratification heat type reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220671202 CN203018067U (en) | 2012-12-09 | 2012-12-09 | Stratification heat type reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203018067U true CN203018067U (en) | 2013-06-26 |
Family
ID=48642085
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220671202 Expired - Fee Related CN203018067U (en) | 2012-12-09 | 2012-12-09 | Stratification heat type reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203018067U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102962022A (en) * | 2012-12-09 | 2013-03-13 | 大连创达技术交易市场有限公司 | Layered heating type reaction kettle |
| CN111772149A (en) * | 2020-04-16 | 2020-10-16 | 成都圣恩生物科技股份有限公司 | Energy-saving consumption-reducing hotpot condiment processing method |
-
2012
- 2012-12-09 CN CN 201220671202 patent/CN203018067U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102962022A (en) * | 2012-12-09 | 2013-03-13 | 大连创达技术交易市场有限公司 | Layered heating type reaction kettle |
| CN111772149A (en) * | 2020-04-16 | 2020-10-16 | 成都圣恩生物科技股份有限公司 | Energy-saving consumption-reducing hotpot condiment processing 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: 20130626 Termination date: 20141209 |
|
| EXPY | Termination of patent right or utility model |