CN202398346U - Reaction kettle provided with metering device - Google Patents
Reaction kettle provided with metering device Download PDFInfo
- Publication number
- CN202398346U CN202398346U CN2011204437048U CN201120443704U CN202398346U CN 202398346 U CN202398346 U CN 202398346U CN 2011204437048 U CN2011204437048 U CN 2011204437048U CN 201120443704 U CN201120443704 U CN 201120443704U CN 202398346 U CN202398346 U CN 202398346U
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- China
- Prior art keywords
- reaction kettle
- agitated reactor
- solvent
- filter
- metering device
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Abstract
The utility model discloses a reaction kettle provided with a metering device. The reaction kettle comprises a first reaction kettle and a second reaction kettle; a filter is arranged on a pipeline between the first reaction kettle and the second reaction kettle; and a metering tank is arranged at the backward position of the filter. According to the amount of solvent required by an autoclave, the reaction kettle provided with the metering device can enable solvent to be filtered by the filter and flow to the metering tank automatically, and pump a corresponding amount of solvent after the solvent is metered by the metering tank, then the solvent cannot be influenced by the degree of vacuum in the autoclave and the pumping and filtration time, and the circumstance that the amount of solvent is unstable can be avoided, so that the production yield of products is stable.
Description
Technical field
The utility model relates to a kind of industrial processing equipment, or rather, is a kind of agitated reactor of industrial band metering device.
Background technology
Agitated reactor is the equipment that under high pressure carries out chemical reaction in a kind of industry, and having of having stirred or heat transfer unit (HTU), also is autoclave, generally is made up of reaction vessel, agitator and transmission system, cooling device, safety device, heating furnace etc.Existing agitated reactor, of Fig. 1, comprise first agitated reactor 1 and second agitated reactor 2, on the pipeline between first agitated reactor 1 and second agitated reactor 2, be provided with a filter 3.In the structure of this multi-stage reacting kettle, feed liquid directly gets into autoclave (second agitated reactor 2) through filter, because suction filtration asynchronism(-nization) and vacuum are high sometimes; Factor affecting such as low sometimes; The amount that feed liquid gets into autoclave has than big difference, causes the proportioning imbalance, and finally causes yield to descend.
The utility model content
The utility model mainly is to solve the existing in prior technology technical problem, thereby a kind of agitated reactor that can adjust the feed liquid inlet automatically is provided.
The above-mentioned technical problem of the utility model mainly is able to solve through following technical proposals: a kind of agitated reactor with metering device; Comprise first agitated reactor and second agitated reactor; On the pipeline between described first agitated reactor and second agitated reactor, be provided with a filter, be provided with a measuring tank in the downstream of described filter.
As the preferred embodiment of the utility model, the outlet of described filter is connected with the inlet of described measuring tank, and the outlet of described measuring tank is connected with the inlet of described second agitated reactor.
As the preferred embodiment of the utility model, described measuring tank is horizontal measuring tank, and described filter is a vertical filter.
Because the agitated reactor of the band metering device of the utility model can be voluntarily according to the required quantity of solvent of autoclave; After solvent is filtered from filter; To measuring tank, after the measuring tank metering, extract corresponding quantity of solvent out again, solvent does not just receive vacuum and the influence of suction filtration time in the autoclave like this; Few for a long time situation during appearance, thus make production, stable yield.
Description of drawings
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art; To do to introduce simply to the accompanying drawing of required use in embodiment or the description of the Prior Art below; Obviously, the accompanying drawing in describing below only is some embodiment of the utility model, for those of ordinary skills; Under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the structural representation of the agitated reactor of prior art;
Fig. 2 is the structural representation of agitated reactor of the band metering device of the utility model.
The specific embodiment
Below in conjunction with accompanying drawing the preferred embodiments of the present invention are set forth in detail, thereby protection scope of the present invention is made more explicit defining so that advantage of the present invention and characteristic can be easier to it will be appreciated by those skilled in the art that.
The utility model provides a kind of agitated reactor that can adjust the feed liquid inlet automatically.
As shown in Figure 2, a kind of agitated reactor with metering device comprises first agitated reactor 10 and second agitated reactor 20, on the pipeline between this first agitated reactor 10 and second agitated reactor 20, is provided with a filter 30, is provided with a measuring tank 40 in the downstream of this filter 30.
The outlet 302 of this filter 30 is connected with the inlet 401 of this measuring tank 40, and the outlet 402 of this measuring tank 40 is connected with the inlet 201 of this second agitated reactor 20.
This measuring tank 40 is horizontal measuring tank, and this filter 30 is a vertical filter.
The agitated reactor of this band metering device can be voluntarily according to the required quantity of solvent of autoclave; After solvent is filtered from filter; To measuring tank, after the measuring tank metering, extract corresponding quantity of solvent out again, solvent does not just receive vacuum and the influence of suction filtration time in the autoclave like this; Few for a long time situation during appearance, thus make production, stable yield.This Stability Analysis of Structures production improves yield, reduces unnecessary loss.
The mentality of designing of the utility model below only is described with an embodiment, and under the situation that system allows, the utility model can expand to external more function module simultaneously, thereby expands its function to greatest extent.
The above is merely the specific embodiment of the utility model, but the protection domain of the utility model is not limited thereto, and any variation or replacement of expecting without creative work all should be encompassed within the protection domain of the utility model.Therefore, the protection domain of the utility model should be as the criterion with the protection domain that claims were limited.
Claims (3)
1. agitated reactor with metering device; Comprise first agitated reactor (10) and second agitated reactor (20); On the pipeline between described first agitated reactor (10) and second agitated reactor (20), be provided with a filter (30); It is characterized in that, be provided with a measuring tank (40) in the downstream of described filter (30).
2. a kind of agitated reactor according to claim 1 with metering device; It is characterized in that; The outlet (302) of described filter (30) is connected with the inlet (401) of described measuring tank (40), and the outlet (402) of described measuring tank (40) is connected with the inlet (201) of described second agitated reactor (20).
3. a kind of agitated reactor with metering device according to claim 2 is characterized in that described measuring tank (40) is horizontal measuring tank, and described filter (30) is a vertical filter.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011204437048U CN202398346U (en) | 2011-11-09 | 2011-11-09 | Reaction kettle provided with metering device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011204437048U CN202398346U (en) | 2011-11-09 | 2011-11-09 | Reaction kettle provided with metering device |
Publications (1)
Publication Number | Publication Date |
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CN202398346U true CN202398346U (en) | 2012-08-29 |
Family
ID=46696024
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN2011204437048U Expired - Fee Related CN202398346U (en) | 2011-11-09 | 2011-11-09 | Reaction kettle provided with metering device |
Country Status (1)
Country | Link |
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CN (1) | CN202398346U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104162397A (en) * | 2014-08-05 | 2014-11-26 | 新乡市富邦科技有限公司 | Emulsion polymerization efficient-coating inhibitor reaction device for drilling fluid |
CN111974040A (en) * | 2020-07-30 | 2020-11-24 | 福建立亚化学有限公司 | Efficient washing and filtering method for chemical synthesis solid product |
-
2011
- 2011-11-09 CN CN2011204437048U patent/CN202398346U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104162397A (en) * | 2014-08-05 | 2014-11-26 | 新乡市富邦科技有限公司 | Emulsion polymerization efficient-coating inhibitor reaction device for drilling fluid |
CN111974040A (en) * | 2020-07-30 | 2020-11-24 | 福建立亚化学有限公司 | Efficient washing and filtering method for chemical synthesis solid product |
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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: 20120829 Termination date: 20141109 |
|
EXPY | Termination of patent right or utility model |