CN203044003U - Defoamer synthesis reaction kettle - Google Patents
Defoamer synthesis reaction kettle Download PDFInfo
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- CN203044003U CN203044003U CN 201320065459 CN201320065459U CN203044003U CN 203044003 U CN203044003 U CN 203044003U CN 201320065459 CN201320065459 CN 201320065459 CN 201320065459 U CN201320065459 U CN 201320065459U CN 203044003 U CN203044003 U CN 203044003U
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- Prior art keywords
- defoamer
- synthesis reaction
- heat exchanger
- reaction kettle
- exchanger tube
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Abstract
The utility model relates to the field of chemical engineering equipment, and discloses a defoamer synthesis reaction kettle. The defoamer synthesis reaction kettle comprises an outer shell 1 and an inner shell, wherein an interlayer cavity 2 is formed between the outer shell 1 and the inner shell; a reaction cavity 4 is formed in the inner shell 3; and eight vertical heat exchange pipes 5 are uniformly distributed in the reaction cavity 4 along the periphery of the inner wall of the inner shell 3; a paddle type stirrer 6 is arranged in the reaction cavity 4; and a cooling medium or heating medium inlet 7 and a cooling medium or heating medium outlet 8 are formed in the outer shell 1. By utilizing the technical scheme, materials can be uniformly heated or cooled; the defoamer synthesis reaction kettle is easy to mount and use; the heat exchange pipes are firmly mounted when being compared with coil pipes; a barrier can be formed and achieves a turbulent flow effect, so that circumferential motion of the reacted materials is avoided; and furthermore, a stirring mechanism is conveniently arranged in the reaction kettle. The defoamer synthesis reaction kettle is low in energy consumption and extremely high in heating and cooling speed and is safely and reliably operated and used, and the heat efficiency is improved.
Description
Technical field
The utility model relates to a kind of chemical industry synthesis device, relates in particular to a kind of defoamer synthesis reaction vessel.
Background technology
In many industrial production, foam is ubiquitous phenomenon and a problem, disturbs ordinary production, when serious even production can't be gone on.The removing method of foam mainly contains chemical method, physics method and Mechanical Method, and physics method and Mechanical Method are simple to operate, but effect is undesirable.So at present most popular is chemical froth breaking method, namely uses the formation of foam in the defoamer control production process and destroy established foam.In recent years, defoamer is applied in the industrial production such as petrochemical industry, pulping and paper-making, textile printing and dyeing, food processing, pharmacy fermentation, coating and printing ink, water treatment more and more widely.
The defoamer synthesis reaction vessel is vital equipment in the defoamer production technology, and the quality of equipment performance will directly influence production efficiency and the quality of defoamer.Existing defoamer synthesis reaction vessel processing and installation are complicated; The reactor effective heat exchange area causes production efficiency low for a short time; Coil pipe mainly is communicated with heating chamber by two ends and is fixed on the inwall, and this is difficult to support the weight of coil pipe, ruptures easily, causes stop work and production.
The utility model content
In order to solve above technical problem, the utility model provides a kind of defoamer synthesis reaction vessel, comprise shell body and inner housing, between shell body and the inner housing for adding the interlayer chamber, be reaction chamber in the inner housing, be provided with the heat exchanger tube of some in described reaction chamber along the periphery of inwall, two end interfaces of described heat exchanger tube are communicated with described interlayer chamber respectively; Rabbling mechanism also is installed in described reaction chamber.
Described heat exchanger tube evenly distributes along the periphery of inwall.
Described heat exchanger tube is along the axial setting of reaction chamber.
Two end interfaces of described heat exchanger tube are vertical corresponding the setting up and down.
The axis of described heat exchanger tube is positioned on the circumference of 1/3 to 2/3 radius of reaction chamber cross section.
Described heat exchanger tube is straight tube.
The quantity of described heat exchanger tube is 5～16.
Described rabbling mechanism is blade formula agitator.
The utility model compared with prior art has following beneficial effect:
The utility model provides a kind of defoamer synthesis reaction vessel, this reactor is more even to material heating or cooling, install and use easy, the installation of heat exchanger tube is more more firm than coil pipe, can also form barrier and play the flow-disturbing effect, to avoid reaction mass to move in a circle, simultaneously rabbling mechanism can also be set in reactor very easily.Because every heat exchanger tube is connected with the interlayer chamber separately, makes entire reaction chamber temperature when the needs alternating temperature can reach setting value quickly, and the alternating temperature amplitude uniformity of the interior each point of reaction chamber; Simultaneously, can also be more convenient increase or reduce heat exchanger tube quantity according to the needs of differential responses condition, even when a part of heat exchanger tube generation plugging fault is arranged wherein, all the other heat exchanger tubes still can play a role, and then keep basic reaction condition, avoid causing unnecessary loss.
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 a kind of cross-sectional view of synthesis reaction vessel;
Fig. 2 is the A-A cutaway view of Fig. 1.
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 defoamer synthesis reaction vessel, referring to Fig. 1, Fig. 2, comprise shell body 1 and inner housing 3, form between shell body 1 and the inner housing 3 and add interlayer chamber 2, be reaction chamber 4 in the inner housing 3, periphery along inner housing 3 inwalls in this reaction chamber 4 evenly is laid with eight vertical heat exchanger tubes 5, and the axis of each heat exchanger tube is positioned on the circumference of 1/2 radius of reaction chamber cross section, and two end interfaces of each heat exchanger tube are communicated with described interlayer chamber 2 respectively; Blade formula agitator 6 also is installed in described reaction chamber 4.Shell body 1 is provided with import 7 and the outlet 8 of refrigerant or heating agent.
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 (8)
1. defoamer synthesis reaction vessel, comprise shell body and inner housing, it is the interlayer chamber between shell body and the inner housing, be reaction chamber in the inner housing, it is characterized in that, be provided with the heat exchanger tube of some in described reaction chamber along the periphery of inwall, two end interfaces of described heat exchanger tube are communicated with described interlayer chamber respectively; Rabbling mechanism also is installed in described reaction chamber.
2. defoamer synthesis reaction vessel according to claim 1 is characterized in that, described heat exchanger tube evenly distributes along the periphery of inner housing inwall.
3. defoamer synthesis reaction vessel according to claim 2 is characterized in that, described heat exchanger tube vertically arranges.
4. defoamer synthesis reaction vessel according to claim 3 is characterized in that, two end interfaces of described heat exchanger tube are vertical corresponding the setting up and down.
5. defoamer synthesis reaction vessel according to claim 4 is characterized in that, the axis of described heat exchanger tube is positioned on the circumference of 1/3 to 2/3 radius of reaction chamber cross section.
6. defoamer synthesis reaction vessel according to claim 5 is characterized in that, described heat exchanger tube is straight tube.
7. defoamer synthesis reaction vessel according to claim 6 is characterized in that, the quantity of described heat exchanger tube is 5～16.
8. defoamer synthesis reaction vessel according to claim 7 is characterized in that, described rabbling mechanism is blade formula agitator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320065459 CN203044003U (en) | 2013-01-22 | 2013-01-22 | Defoamer synthesis reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320065459 CN203044003U (en) | 2013-01-22 | 2013-01-22 | Defoamer synthesis reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203044003U true CN203044003U (en) | 2013-07-10 |
Family
ID=48727004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320065459 Expired - Fee Related CN203044003U (en) | 2013-01-22 | 2013-01-22 | Defoamer synthesis reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203044003U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823432A (en) * | 2017-04-19 | 2017-06-13 | 长沙科力威蒸馏技术有限公司 | A kind of distilling apparatus |
-
2013
- 2013-01-22 CN CN 201320065459 patent/CN203044003U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106823432A (en) * | 2017-04-19 | 2017-06-13 | 长沙科力威蒸馏技术有限公司 | A kind of distilling apparatus |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130710 Termination date: 20210122 |