CN207307843U - A kind of flow reactor - Google Patents
A kind of flow reactor Download PDFInfo
- Publication number
- CN207307843U CN207307843U CN201721012152.9U CN201721012152U CN207307843U CN 207307843 U CN207307843 U CN 207307843U CN 201721012152 U CN201721012152 U CN 201721012152U CN 207307843 U CN207307843 U CN 207307843U
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- China
- Prior art keywords
- reaction kettle
- reaction
- connecting tube
- flow reactor
- kettle
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- 238000006243 chemical reaction Methods 0.000 claims abstract description 115
- 230000004087 circulation Effects 0.000 claims abstract description 8
- 238000009413 insulation Methods 0.000 claims description 4
- 230000002572 peristaltic effect Effects 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 11
- 230000004044 response Effects 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 3
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model discloses a kind of flow reactor, including the first reaction kettle, the second reaction kettle and the 3rd reaction kettle, the discharge port of first reaction kettle is connected to the feed inlet of the second reaction kettle by connecting tube, the discharge port of second reaction kettle connects the feed inlet of the 3rd reaction kettle by connecting tube, first circulation pump is provided with connecting tube between first reaction kettle and the second reaction kettle, second circulation pump is provided with the connecting tube between the second reaction kettle and the 3rd reaction kettle；Three reaction kettles are set, the material that chemical reaction mixes is needed first to be reacted in the first reaction kettle, reaction is reacted into the second reaction kettle after a certain period of time, enter the 3rd reaction kettle after a certain period of time in the reaction of the second reaction kettle, after three reaction kettles carry out circular response to material so that material reaction is more abundant, due to using continuous circular response, mixing time is also reduced while reaction effect is good, is improved work efficiency.
Description
Technical field
Technical field of chemical is the utility model is related to, more particularly to a kind of flow reactor.
Background technology
Need to use reaction kettle in chemical process and chemically reacted, existing reaction kettle include an autoclave body and
One agitating device.In chemistry, first material is put into autoclave body, restarts agitating device and is stirred.Existing reaction
The time that kettle needs when needing stirring longer time, especially material to swim in above liquid when being stirred is longer, makes
It is relatively low to obtain the work efficiency of existing reaction kettle, so as to improve production cost
Utility model content
The technical problem to be solved by the present invention is to provide one kind to chemically react fast efficient, relatively low reaction time cost
Flow reactor.
In order to solve the above-mentioned technical problem, the technical solution of the utility model is：A kind of flow reactor, including first is anti-
Answer kettle, the second reaction kettle and the 3rd reaction kettle, it is anti-that the discharge port of first reaction kettle by connecting tube is connected to described second
The feed inlet of kettle is answered, the discharge port of second reaction kettle connects the feed inlet of the 3rd reaction kettle by connecting tube, described
First circulation pump, second reaction kettle and described are provided with connecting tube between first reaction kettle and second reaction kettle
It is provided with second circulation pump in connecting tube between 3rd reaction kettle, the feed inlet of first reaction kettle passes through connecting pipe the
One storage tank and the second storage tank, first storage tank and the second storage tank in the connecting pipe of the first reaction kettle with being provided with
Peristaltic pump.
As a kind of preferred embodiment, set respectively on first reaction kettle, the second reaction kettle and the 3rd reaction kettle
There is agitating device, the agitating device includes motor, shaft is connected with the rotor of the motor, is set in the shaft
There is stirrer gear.
As a kind of preferred embodiment, the stirrer gear includes the first helical blade and the second helical blade, and described
The outside diameter of one helical blade is more than the outside diameter of the second helical blade.
As a kind of preferred embodiment, first reaction kettle and second reaction kettle, second reaction kettle and
Check-valves is additionally provided with connecting tube between 3rd reaction kettle.
As a kind of preferred embodiment, shaft coupling is provided between the motor and the shaft.
As a kind of preferred embodiment, set on the outer wall of first reaction kettle, the second reaction kettle and the 3rd reaction kettle
It is equipped with insulation jacket.
Had the beneficial effect that using what above-mentioned technical proposal the utility model obtained：Three reaction kettles are set, it is necessary to which chemistry is anti-
The material that should be mixed first reacts in the first reaction kettle, and reaction is reacted into the second reaction kettle after a certain period of time, second
Reaction kettle reaction enters the 3rd reaction kettle after a certain period of time, after three reaction kettles carry out circular response to material so that thing
Material reaction is more abundant, due to using continuous circular response, also reduces mixing time while reaction effect is good, improves
Work efficiency.
Brief description of the drawings
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, drawings in the following description are only
It is some embodiments of the utility model, for those of ordinary skill in the art, before not making the creative labor property
Put, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is the structure diagram of the utility model.
In figure：The first reaction kettles of 1-, the second reaction kettles of 2-, the 3rd reaction kettles of 3-, 4- first circulations pump, 5- second circulations
Pump, the first storage tanks of 6-, the second storage tanks of 7-, 8- peristaltic pumps, 9- motor, 10- shafts, 11- stirrer gears, 12- first are spiral
Blade, the second helical blades of 13-, 14- check-valves, 15- insulation jackets.
Embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings.It should be noted that
It is used to help understand the utility model for the explanation of these embodiments, but does not form the restriction to the utility model.This
Outside, as long as technical characteristic involved in each embodiment of the utility model disclosed below does not form conflict each other
It can be mutually combined.
The utility model is further described with reference to attached drawing, those skilled in the art is preferably implemented this practicality new
Type, a kind of flow reactor of the utility model embodiment, including the first reaction kettle 1, the second reaction kettle 2 and the 3rd reaction kettle 3, the
The discharge port of one reaction kettle 1 is connected to the feed inlet of the second reaction kettle 2 by connecting tube, and the discharge port of the second reaction kettle 2 passes through
Connecting tube connects the feed inlet of the 3rd reaction kettle 3, and the is provided with the connecting tube between the first reaction kettle 1 and the second reaction kettle 2
One circulating pump 4, second circulation pump 5, the first reaction kettle 1 are provided with the connecting tube between the second reaction kettle 2 and the 3rd reaction kettle 3
Feed inlet by connecting pipe the first storage tank 6 and the second storage tank 7, the first storage tank 6 and the second storage tank 7 and first anti-
Answer and peristaltic pump 8 is provided with the connecting pipe of kettle 1.
Stirring is respectively arranged with the utility model embodiment the first reaction kettle 1, the second reaction kettle 2 and the 3rd reaction kettle 3
Device, agitating device include motor 9, are connected with shaft 10 on the rotor of motor 9, stirrer gear 11 is provided with shaft 10；
Stirrer gear 11 includes the first helical blade 12 and the second helical blade 13, and the outside diameter of the first helical blade 12 is more than the second helical-blade
The outside diameter of piece 13；In connecting tube between first reaction kettle 1 and the second reaction kettle 2, the second reaction kettle 2 and the 3rd reaction kettle 3 also
It is provided with check-valves 14；Shaft coupling is provided between motor 9 and shaft 10；First reaction kettle 1, the second reaction kettle 2 and the 3rd
Insulation jacket 15 is provided with the outer wall of reaction kettle 3.
The utility model embodiment sets three reaction kettles, it is necessary to chemically react the material of mixing first in the first reaction kettle 1
Middle reaction, reaction are reacted into the second reaction kettle 2, react in the second reaction kettle 2 and enter after a certain period of time after a certain period of time
3rd reaction kettle 3, after three reaction kettles carry out circular response to material so that material reaction is more abundant, due to using
Continuous circular response, also reduces mixing time while reaction effect is good, improves work efficiency.
The embodiment of the utility model is explained in detail above in association with attached drawing, but the utility model is not limited to be retouched
The embodiment stated.For a person skilled in the art, it is right in the case where not departing from the utility model principle and spirit
These embodiments carry out a variety of change, modification, replacement and modification, still fall within the scope of protection of the utility model.
Claims (6)
- A kind of 1. flow reactor, it is characterised in that：Including the first reaction kettle, the second reaction kettle and the 3rd reaction kettle, described The discharge port of one reaction kettle is connected to the feed inlet of second reaction kettle, the discharge port of second reaction kettle by connecting tube The feed inlet of the 3rd reaction kettle, the connection between first reaction kettle and second reaction kettle are connected by connecting tube First circulation pump is provided with pipe, being provided with second in the connecting tube between second reaction kettle and the 3rd reaction kettle follows Ring pumps, and the feed inlet of first reaction kettle passes through the first storage tank of connecting pipe and the second storage tank, first storage tank Be provided with peristaltic pump in the connecting pipe of the second storage tank and the first reaction kettle.
- 2. flow reactor according to claim 1, it is characterised in that：First reaction kettle, the second reaction kettle and the 3rd Agitating device is respectively arranged with reaction kettle, the agitating device includes motor, is connected with and turns on the rotor of the motor Axis, is provided with stirrer gear in the shaft.
- 3. flow reactor according to claim 2, it is characterised in that：The stirrer gear includes the first helical blade and second Helical blade, the outside diameter of first helical blade are more than the outside diameter of the second helical blade.
- 4. flow reactor according to claim 3, it is characterised in that：First reaction kettle and second reaction kettle, Check-valves is additionally provided with connecting tube between second reaction kettle and the 3rd reaction kettle.
- 5. flow reactor according to claim 4, it is characterised in that：Connection is provided between the motor and the shaft Axis device.
- 6. flow reactor according to claim 5, it is characterised in that：First reaction kettle, the second reaction kettle and the 3rd Insulation jacket is provided with the outer wall of reaction kettle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721012152.9U CN207307843U (en) | 2017-08-14 | 2017-08-14 | A kind of flow reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721012152.9U CN207307843U (en) | 2017-08-14 | 2017-08-14 | A kind of flow reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207307843U true CN207307843U (en) | 2018-05-04 |
Family
ID=62434501
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721012152.9U Active CN207307843U (en) | 2017-08-14 | 2017-08-14 | A kind of flow reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207307843U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589899A (en) * | 2018-12-14 | 2019-04-09 | 浙江开化合成材料有限公司 | A kind of process for producing neutral ethyl orthosilicate |
| CN110124601A (en) * | 2019-05-22 | 2019-08-16 | 安徽红太阳新材料有限公司 | A kind of alkyl glycosides bleaching system |
-
2017
- 2017-08-14 CN CN201721012152.9U patent/CN207307843U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589899A (en) * | 2018-12-14 | 2019-04-09 | 浙江开化合成材料有限公司 | A kind of process for producing neutral ethyl orthosilicate |
| CN110124601A (en) * | 2019-05-22 | 2019-08-16 | 安徽红太阳新材料有限公司 | A kind of alkyl glycosides bleaching system |
| CN110124601B (en) * | 2019-05-22 | 2021-03-26 | 安徽红太阳新材料有限公司 | Alkyl glycoside bleaching device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A continuous reactor Effective date of registration: 20230814 Granted publication date: 20180504 Pledgee: Shandong Changyi rural commercial bank Limited by Share Ltd. Pledgor: WEIFANG RUN'AN CHEMICAL TECHNOLOGY CO.,LTD. Registration number: Y2023980052011 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20180504 Pledgee: Shandong Changyi rural commercial bank Limited by Share Ltd. Pledgor: WEIFANG RUN'AN CHEMICAL TECHNOLOGY CO.,LTD. Registration number: Y2023980052011 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right |