CN206881716U - Chemical reaction kettle - Google Patents
Chemical reaction kettle Download PDFInfo
- Publication number
- CN206881716U CN206881716U CN201720852285.0U CN201720852285U CN206881716U CN 206881716 U CN206881716 U CN 206881716U CN 201720852285 U CN201720852285 U CN 201720852285U CN 206881716 U CN206881716 U CN 206881716U
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- CN
- China
- Prior art keywords
- kettle
- pipeline
- chemical reaction
- injector
- reaction kettle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
A kind of chemical reaction kettle, including kettle are the utility model is related to, liquid circulation chamber is set outside kettle；Middle part inside kettle sets charging coil pipe, feeds and is equipped with aperture on coil pipe；Top inside kettle sets injector, multiple spray heads are set on injector, and injector is connected to blender by pipeloop, and blender connects water cooling pond by pipeline, water cooling pond is returned by the second pipeline by the first pipeline connection liquid circulation chamber, liquid circulation chamber and is connected to water cooling pond；Autoclave body bottom connects pipeloop by pipeline.The utility model is simple in construction, easy to operate, increases the contact surface between material, material can be made effectively to react, and improves production efficiency, improves product quality, low cost, effectively reduces the temperature of reactor, and safety coefficient is high.
Description
Technical field
It the utility model is related to a kind of chemical reaction kettle.
Background technology
, it is necessary to using the reactor with agitating device in existing chemical industry equipment reaction, i.e., there is master in a kettle
Axle and the stirring vane that main axis is followed on main shaft is arranged on, low production efficiency, product quality in most of course of reaction
Difference, original production equipment is insufficient because stirring, and material contact surface is small, reacts bad, skewness, while cooling-down effect is poor,
The difficult control of temperature.The production of original agitating mode, during charging directly and material contact surface is small, stir uneven reaction slowly.It is original to stir
The mode of mixing produces, and when material liquid level is low, heat exchange coil contact surface is small in material and kettle, and cooling-down effect is poor；If material is few during heating,
Contacted with kettle internal jacket heat exchange area small, heating is slow.
Utility model content
The purpose of this utility model is to provide a kind of chemical reaction kettle, simple in construction, easy to operate, between increase material
Contact surface, material can be made effectively to react, improve production efficiency, improve product quality, low cost, effectively reduce reactor
Temperature, safety coefficient is high.
A kind of chemical reaction kettle described in the utility model, including kettle, kettle set liquid circulation chamber outside；Inside kettle
Middle part set charging coil pipe, feed coil pipe on be equipped with aperture；Top inside kettle sets injector, is set on injector
Multiple spray heads, injector are connected to blender by pipeloop, and blender connects water cooling pond by pipeline, and water cooling pond passes through
First pipeline connection liquid circulation chamber, liquid circulation chamber are returned by the second pipeline and are connected to water cooling pond；Autoclave body bottom is connected by pipeline
Connect pipeloop.
Kettle top sets feed pipe, and feed pipe connects with charging coil pipe.
Valve is respectively provided with each pipeline.
Autoclave body bottom sets discharging opening；Charging aperture is set at the top of kettle.
Agitating shaft is set inside kettle.
Kettle top sets motor.
Circulating pump is set on pipeloop.
First valve is set on the first pipeline.
Second valve is set on the second pipeline.
The material injector and charging coil pipe of kettle inner top, are well mixed material, fully reaction.It is and poor by pump pressure
Under, injector is atomized material, is sprayed downwards in kettle inner top, material achieving full-area contact, and reaction is more abundant, and material cooling is fast
It is fast effective, the more preferable controlling reaction temperature of energy and reaction pressure, improve production efficiency.
Water in the liquid and cooling bay of liquid circulation intracavitary forms circulation, effectively reduces temperature of reaction kettle, and simultaneously can
Reaction mass is enough set to provide water.
Compared with prior art, the utility model has the advantages that：
Chemical reaction kettle described in the utility model, it is simple in construction, it is easy to operate, increase the contact surface between material, energy
Enough material is effectively reacted, improve production efficiency, improve product quality, low cost, effectively reduce the temperature of reactor, pacify
Overall coefficient is high.
Brief description of the drawings
Fig. 1 structural representations of the present utility model；
In figure：1st, kettle, 2, injector, 3, motor, 4, liquid circulation chamber, 5, agitating shaft, 6, discharging opening, 7, circulation
Pump, 8, blending tank, 9, water cooling pond, the 10, second valve, the 11, first valve, 12, charging aperture, 13, feed pipe, 14, charging coil pipe,
15th, pipeloop, the 16, first pipeline, the 17, second pipeline.
Embodiment
With reference to embodiment, the utility model is described in further detail.
Embodiment 1
A kind of chemical reaction kettle described in the present embodiment, including kettle 1, kettle 1 set liquid circulation chamber 4 outside；In kettle 1
The middle part in portion sets charging coil pipe 14, feeds and is equipped with aperture on coil pipe 14；Top inside kettle 1 sets injector 2, injection
Multiple spray heads are set on device 2, and injector 2 is connected to blender 8 by pipeloop 14, and blender 8 is connected cold by pipeline
Pond 9, water cooling pond 9 connect liquid circulation chamber 4 by the first pipeline 16, liquid circulation chamber 4 returned by the second pipeline 17 be connected to it is cold
Pond 9；The bottom of kettle 1 connects pipeloop 15 by pipeline.
The top of kettle 1 sets feed pipe 13, and feed pipe 13 connects with charging coil pipe 14.
Valve is respectively provided with each pipeline.
The bottom of kettle 1 sets discharging opening 6；The top of kettle 1 sets charging aperture 12.
The inside of kettle 1 sets agitating shaft 5.
The top of kettle 1 sets motor 3.
Circulating pump 7 is set on pipeloop 15.
First valve 11 is set on first pipeline 16.
Second valve 10 is set on second pipeline 17.
Claims (7)
1. a kind of chemical reaction kettle, including kettle（1）, it is characterised in that kettle（1）Outer setting liquid circulation chamber（4）；Kettle
（1）Internal middle part sets charging coil pipe（14）, feed coil pipe（14）On be equipped with aperture；Kettle（1）Internal top is set
Injector（2）, injector（2）It is upper that multiple spray heads, injector are set（2）Pass through pipeloop（15）It is connected to blender（8）,
Blender（8）Water cooling pond is connected by pipeline（9）, water cooling pond（9）Pass through the first pipeline（16）Connect liquid circulation chamber（4）, liquid
Body circulation chamber（4）Pass through the second pipeline（17）Return and be connected to water cooling pond（9）；Kettle（1）Bottom connects pipeloop by pipeline
（15）.
2. chemical reaction kettle according to claim 1, it is characterised in that kettle（1）Top sets feed pipe（13）, charging
Pipe（13）With feeding coil pipe（14）Connection.
3. chemical reaction kettle according to claim 1, it is characterised in that be respectively provided with valve on each pipeline.
4. chemical reaction kettle according to claim 1, it is characterised in that kettle（1）Bottom sets discharging opening（6）；Kettle
（1）Top sets charging aperture（12）.
5. chemical reaction kettle according to claim 1, it is characterised in that kettle（1）Inside sets agitating shaft（5）.
6. chemical reaction kettle according to claim 1, it is characterised in that kettle（1）Top sets motor（3）.
7. chemical reaction kettle according to claim 1, it is characterised in that pipeloop（15）Upper setting circulating pump（7）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720852285.0U CN206881716U (en) | 2017-07-13 | 2017-07-13 | Chemical reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720852285.0U CN206881716U (en) | 2017-07-13 | 2017-07-13 | Chemical reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206881716U true CN206881716U (en) | 2018-01-16 |
Family
ID=61297123
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720852285.0U Expired - Fee Related CN206881716U (en) | 2017-07-13 | 2017-07-13 | Chemical reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206881716U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355596A (en) * | 2018-02-28 | 2018-08-03 | 中国天辰工程有限公司 | A kind of proportioner and proportioning process taking heat drop low temperature using raw material |
| CN110975784A (en) * | 2019-10-31 | 2020-04-10 | 黄冈师范学院 | Feeding device and feeding process of ethylene oxide in metronidazole hydroxylation reaction |
| CN111004710A (en) * | 2019-12-25 | 2020-04-14 | 吕梁学院 | Sterile plant tissue extractor based on transgenic technology |
| CN112387240A (en) * | 2019-08-12 | 2021-02-23 | 中国石油化工股份有限公司 | Vaporization mixer and pilot plant |
-
2017
- 2017-07-13 CN CN201720852285.0U patent/CN206881716U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355596A (en) * | 2018-02-28 | 2018-08-03 | 中国天辰工程有限公司 | A kind of proportioner and proportioning process taking heat drop low temperature using raw material |
| CN112387240A (en) * | 2019-08-12 | 2021-02-23 | 中国石油化工股份有限公司 | Vaporization mixer and pilot plant |
| CN110975784A (en) * | 2019-10-31 | 2020-04-10 | 黄冈师范学院 | Feeding device and feeding process of ethylene oxide in metronidazole hydroxylation reaction |
| CN111004710A (en) * | 2019-12-25 | 2020-04-14 | 吕梁学院 | Sterile plant tissue extractor based on transgenic technology |
| CN111004710B (en) * | 2019-12-25 | 2023-09-12 | 吕梁学院 | Plant tissue sterile extractor based on transgenic technology |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180116 Termination date: 20180713 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |