CN203764242U - Double jacketed reaction kettle - Google Patents
Double jacketed reaction kettle Download PDFInfo
- Publication number
- CN203764242U CN203764242U CN201420139918.XU CN201420139918U CN203764242U CN 203764242 U CN203764242 U CN 203764242U CN 201420139918 U CN201420139918 U CN 201420139918U CN 203764242 U CN203764242 U CN 203764242U
- Authority
- CN
- China
- Prior art keywords
- jacket
- chuck
- reaction kettle
- outlet
- tank
- 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
Links
- 238000006243 chemical reaction Methods 0.000 title abstract description 9
- 239000000463 material Substances 0.000 abstract description 7
- 239000007788 liquid Substances 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwLjAnIGhlaWdodD0nMzAwLjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMDAuNScgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5IPC90ZXh0Pgo8dGV4dCB4PScxMjYuMScgeT0nMTg2LjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID4yPC90ZXh0Pgo8dGV4dCB4PScxMzguMCcgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000498 cooling water Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
Abstract
The utility model provides a double jacketed reaction kettle which comprises a tank body (1) and a jacket arranged on the outer wall of the tank body. The reaction kettle is characterized in that the jacket comprises an upper jacket (2) and a lower jacket (3), wherein inlets and outlets positioned below the inlets are respectively formed in the upper jacket (2) and the lower jacket (3); an outlet of the upper jacket (2) is communicated with an inlet of the lower jacket (3); the lower jacket (3) is in a spiral shape; a steam trap is arranged at the outlet of the lower jacket (3). Two independent jacket systems are arranged on the reaction kettle, so that the problem that liquid in the jacket is in flow short circuit is solved, and materials in the kettles are uniformly heated. Meanwhile, a secondary heat source of the upper jacket enters the lower jacket to be continuously used, and an aim of reducing the steam consumption is achieved.
Description
Technical field
The utility model relates to technical field of chemical, particularly a kind of double jacket reactor.
Background technology
In chemical process, jacket type heat transfer synthesis process is widely used, and it adopts jacket type reactor, by chuck being passed into steam or hot water or cooling water, realizes the material in still is heated up or lowered the temperature.Because synthesis reaction vessel belongs to chemical reaction equipment, need to require to control according to reaction process the temperature of material in still.In prior art, the chuck layer of reactor is as a whole from top to bottom, steam or hot water or cooling water form liquid flow short circuit phenomenon after entering chuck, in still, material is heated inhomogeneous, have a strong impact on material reaction process and reaction control effect, the excess Temperature of the condensate water that chuck is got rid of simultaneously, is unfavorable for energy conservation.
Utility model content
The purpose of this utility model is to provide a kind of double jacket reactor, and described this reactor will solve temperature of reaction kettle in prior art and control the inhomogeneous and high problem of energy resource consumption.
The utility model is achieved through the following technical solutions:
A kind of double jacket reactor, comprise tank body (1) and be arranged on the chuck on tank wall, it is characterized in that: described chuck comprises chuck (2) and lower chuck (3), on upper chuck (2) and lower chuck (3), be respectively arranged with import and be positioned at the outlet of import below, the import of the outlet of upper chuck (2) and lower chuck (3) is communicated with.
Described lower chuck (3) is semi-canal type structure in the shape of a spiral.
The exit of described lower chuck (3) is provided with steam trap.
In the utility model, two chuck layers are separated to design, the outlet of upper chuck is connected with the import of lower chuck, and steam enters from upper chuck, enters lower chuck layer after the upper chuck of flowing through again, then by steam trap, get rid of condensate water, make reactor can adapt to the requirement of evenly intensification and steam saving consumption.
Compared to the prior art, its effect is actively with obvious to the utility model.The utility model arranges two independently chuck systems in the top and the bottom of reactor, solved like this liquid flow short circuit problem in chuck, and in still, material is heated evenly; The secondary heat source that goes up chuck enters lower chuck and continues to use simultaneously, reaches the object that reduces steam consumption quantity.
Accompanying drawing explanation
Fig. 1 is cutaway view of the present utility model;
Reactor-1 wherein, upper chuck-2, lower chuck-3, upper chuck import-21, upper JO-22, lower chuck import-31, lower JO-32.
The specific embodiment
Below in conjunction with accompanying drawing, by embodiment, the utility model is described in further details.
Comprise tank body (1) and be arranged on the chuck on tank wall, described chuck comprises chuck (2) and lower chuck (3), on upper chuck (2) and lower chuck (3), be respectively arranged with import and be positioned at the outlet of import below, the import of the outlet of upper chuck (2) and lower chuck (3) is communicated with.
Described lower chuck (3) in the shape of a spiral.
The exit of described lower chuck (3) is provided with steam trap.
The utility model arranges two independently chuck systems in the top and the bottom of reactor, solved like this liquid flow short circuit problem in chuck, and in still, material is heated evenly; The secondary heat source that goes up chuck enters lower chuck and continues to use simultaneously, reaches the object that reduces steam consumption quantity.
Claims (3)
1. a double jacket reactor, comprise tank body (1) and be arranged on the chuck on tank wall, it is characterized in that: described chuck comprises chuck (2) and lower chuck (3), on upper chuck (2) and lower chuck (3), be respectively arranged with import and be positioned at outlet, the outlet (22) of upper chuck (2) and the import (31) of lower chuck (3) connection of import below.
2. double jacket reactor as claimed in claim 1, is characterized in that: described lower chuck (3) in the shape of a spiral.
3. double jacket reactor as claimed in claim 1, is characterized in that: the exit of described lower chuck (3) is provided with steam trap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420139918.XU CN203764242U (en) | 2014-03-26 | 2014-03-26 | Double jacketed reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420139918.XU CN203764242U (en) | 2014-03-26 | 2014-03-26 | Double jacketed reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203764242U true CN203764242U (en) | 2014-08-13 |
Family
ID=51281490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420139918.XU Expired - Fee Related CN203764242U (en) | 2014-03-26 | 2014-03-26 | Double jacketed reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203764242U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105013407A (en) * | 2015-07-27 | 2015-11-04 | 陕西延长石油集团氟硅化工有限公司 | Organic fluorination reaction kettle device |
-
2014
- 2014-03-26 CN CN201420139918.XU patent/CN203764242U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105013407A (en) * | 2015-07-27 | 2015-11-04 | 陕西延长石油集团氟硅化工有限公司 | Organic fluorination reaction kettle device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| C14 | Grant of patent or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160330 Address after: 432500, salt chemical industrial park, Pu Pu town, dream county, Hubei, Xiaogan Patentee after: Hubei Huaxin silicone new material Co., Ltd. Address before: 432500, No. 55, Chengguan Town, Yunmeng County, Xiaogan City, Jianshe Road Province, Hubei Patentee before: Hubei Province's Yunmeng Hua Chang chemical industry Co., Ltd |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140813 Termination date: 20180326 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |