CN205517686U - Vertical reactor - Google Patents
Vertical reactor Download PDFInfo
- Publication number
- CN205517686U CN205517686U CN201620338708.2U CN201620338708U CN205517686U CN 205517686 U CN205517686 U CN 205517686U CN 201620338708 U CN201620338708 U CN 201620338708U CN 205517686 U CN205517686 U CN 205517686U
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- Prior art keywords
- vertical reactor
- distributor
- reactor
- reaction chamber
- hole
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- 239000000463 material Substances 0.000 claims description 19
- 238000007599 discharging Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 abstract description 4
- 239000007795 chemical reaction product Substances 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- 239000000376 reactant Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The utility model discloses a vertical reactor, including the body of reactor, locate the feed inlet of body on being close to the lateral wall at top, locate the discharge gate of body bottom, this internal being equipped with the inside collector that is divided into reaction chamber and blanking cavity of body, the reaction chamber is located blanking cavity's top, be equipped with the blanking hole on the collector, be equipped with the distributor in the lower part of collector, the surface of distributor evenly is provided with the homocline hole, owing to evenly set up the homocline hole on the distributor, will demonstrate even strip so follow the reaction product who comes out in the homocline hole, and then enter into down the process one from the discharge gate ejection of compact to the even degree of product has been improved.
Description
Technical field
This utility model relates to reactor technology field, more specifically, it relates to a kind of vertical reactor.
Background technology
Existing reactor or reactor, generally comprise housing, the agitating device being arranged on housing and be arranged on the discharging opening of housing bottom.Material, after entering reactor, reacts and is stirred by agitating device so that it reacts more uniformly, is then exited into down in reaction station together by discharging opening by the product after reaction.
Disclosed in the Chinese patent of as entitled in Publication No. CN202893349U " reactor ", it it is the above-mentioned reactor substantially described.But this reactor is owing to being that the product after reacting directly is discharged by discharging opening, then the product density ejected can be made to differ due to the change of discharging speed and reactor internal pressure, affect the following process quality of material.
Utility model content
The purpose of this utility model is to provide a kind of reactor that reactant is uniformly discharged.
Above-mentioned technical purpose of the present utility model has the technical scheme that a kind of vertical reactor, including reactor body, be located at body charging aperture on the sidewall at top, be located at the discharging opening of body bottom portion, body interior is divided into reaction chamber and the catcher in blanking chamber by described internal being provided with, described reaction chamber is positioned at the top in blanking chamber, described catcher is provided with material-dropping hole, be provided with distributor in the bottom of catcher, the surface of described distributor is evenly arranged with homocline hole.
Pass through such scheme, when material reacts after charging aperture enters the body of reactor in first falling into reaction chamber, owing to the low viscosity of temperature of charge at the beginning is big, poor fluidity cannot be flowed in blanking chamber from the material-dropping hole of catcher, only the product after reaction is completely could be from material-dropping hole blanking, product after blanking will drop in distributor, owing to being uniformly arranged homocline hole on distributor, so product out will present uniform strip from homocline hole, next process is entered into the most again from discharge hole for discharge, thus improve the uniformity coefficient of product.
It is optimized for further: the lower section in each homocline hole of described distributor all connects the tremie pipe leading to discharging opening, and the caliber of each tremie pipe is identical.
By such scheme, by the tremie pipe that caliber is identical, more further stabilize from distributor the shape uniformity coefficient of product out, further increase the discharging stability of product on the whole.
It is optimized for further: described body is additionally provided with agitating device, including being located at the motor of bodies top, in the rotating shaft of this motor penetrates the reaction chamber of body and connect and have scraper plate.
By such scheme, by agitating device, when the material in reaction chamber starts to react when, reacting substance can be stirred so that it is more abundant that reaction is carried out, and passes through scraper plate by scraper plate, material on the wall sticking to reaction chamber can also be hung, improve the utilization rate of material.
It is optimized for further: described scraper plate is the distribution of axial uniform intervals in rotating shaft, and to arrange number be 1-14.
By such scheme, scraper plate is arranged to the axial uniform intervals along rotating shaft and is distributed, it is also possible to arrange 1-14 according to the size of actual reacting substance and reactor, improve reaction efficiency.
It is optimized for further: the gap between described scraper plate and the cavity wall of reaction chamber is 0.1-6mm.
By such scheme, the gap between scraper plate and the cavity wall of reaction chamber is arranged to 0.1-6mm, the scraping between scraper plate and cavity wall i.e. can be avoided to wear and tear, effectively the material sticked in cavity wall can be hung again and fully react.
It is optimized for further: the outside of described body is additionally provided with chuck, is connected with conduction oil in described chuck.
By such scheme, by chuck and in chuck admittance deep fat, temperature stability when will can be effectively improved reactor reaction, and then improve the reaction stability of reactant.
It is optimized for further: the top of described body is additionally provided with standby material inlet.
By such scheme, when charging aperture is plugged when, or the when that only a charging aperture being insufficient for charging rate, standby material inlet can be opened, to meet emergent being used.
In sum, this utility model has the advantages that and reacting substance the most out is flowed out become uniform by being provided with distributor in reactor, and pass through tremie pipe, more improve from distributor the shape uniformity of material out, substantially increase the uniformity coefficient from the discharging opening of reactor material out and degree of stability.
Accompanying drawing explanation
Fig. 1 is the structure sectional view of embodiment.
In figure, 1, chuck；11, heat conductive oil inlet；12, conduction oil outlet；21, charging aperture；22, standby material inlet；3, motor；4, scraper plate；5, catcher；51, material-dropping hole；6, distributor；61, homocline hole；7, tremie pipe；8, discharging opening.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model is described in further detail.
This specific embodiment is only to explanation of the present utility model; it is not to restriction of the present utility model; the present embodiment can be made after reading this specification by those skilled in the art as required does not has the amendment of creative contribution, but as long as all being protected by Patent Law in right of the present utility model.
Embodiment, a kind of vertical reactor, see accompanying drawing 1, including reactor body, the bottom of body is provided with discharging opening 8, the charging aperture 21 on the sidewall at top, and is provided with standby material inlet 22 at the top of body；Being arranged on the chuck 1 of body exterior, the lower edge at chuck 1 is provided with heat conductive oil inlet 11, and the upper edge at chuck 1 is provided with conduction oil outlet 12；Body interior is provided with catcher 5, and the shape of catcher 5 is inverted cone, and body interior is divided into reaction chamber and blanking chamber, is provided with material-dropping hole 51 on catcher 5；The top of body is provided with agitating device, is provided with scraper plate 4 after penetrating reaction chamber including the rotating shaft of motor 3, motor 3, and scraper plate 4 is arranged to 1-14 along rotating shaft uniform intervals, and the gap that scraper plate 4 is between the cavity wall of reaction chamber is 0.1-6mm；It is provided with distributor 6 in the lower section of catcher 5, distributor 6 is provided with homocline hole 61, be provided with the identical tremie pipe of caliber 7 in the lower section in homocline hole 61.
The when of specific works, conduction oil is passed through from the heat conductive oil inlet 11 of chuck 1, and from conduction oil outlet 12 outflow, lasting carries out temperature control, promote temperature stability when reaction body；The material of reaction enters from charging aperture 21, when reactant demand is big, standby material inlet 22 can also be started simultaneously, material drops in reaction chamber after entering body and reacts, while while Fan Ying motor 3 drive scraper plate 4 to stir reactant simultaneously, make reaction become more abundant, and the material in the cavity wall sticking to reaction chamber can be hung in passing, improve the utilization rate of material；After reaction is complete, product will run down in blanking chamber from the material-dropping hole 51 of catcher 5, first product drops on distributor 6, owing to product blanking speed from reaction chamber is far longer than the speed fallen from the homocline hole 61 of distributor 6, product will be deposited on distributor 6, being flowed in tremie pipe 7 by homocline hole 61 the most slowly, is flowed out from discharging opening 8 the most again.Product after out, not only almost consistent in density, and owing to the caliber of tremie pipe 7 is identical, out product will present the shape of the most consistent a plurality of strip of diameter afterwards, thus shape is the most highly uniform, it is greatly improved product stability in following process.
Claims (7)
1. a vertical reactor, including reactor body, be located at body charging aperture (21) on the sidewall at top, be located at the discharging opening (8) of body bottom portion, it is characterized in that, described internal is provided with the catcher (5) that body interior is divided into reaction chamber and blanking chamber, described reaction chamber is positioned at the top in blanking chamber, described catcher (5) is provided with material-dropping hole (51), be provided with distributor (6) in the bottom of catcher (5), the surface of described distributor (6) is evenly arranged with homocline hole (61).
A kind of vertical reactor the most according to claim 1, it is characterized in that, the lower section of each homocline hole (61) of described distributor (6) all connects the tremie pipe (7) leading to discharging opening (8), and the caliber of each tremie pipe (7) is identical.
A kind of vertical reactor the most according to claim 2, it is characterized in that, described body is additionally provided with agitating device, including being located at the motor (3) of bodies top, in the rotating shaft of this motor (3) penetrates the reaction chamber of body and connect and have scraper plate (4).
A kind of vertical reactor the most according to claim 3, it is characterised in that described scraper plate (4) is the distribution of axial uniform intervals in rotating shaft, and to arrange number be that 1-14 is individual.
5. according to a kind of vertical reactor described in claim 3 or 4, it is characterised in that the gap between described scraper plate (4) and the cavity wall of reaction chamber is 0.1-6mm.
A kind of vertical reactor the most according to claim 5, it is characterised in that the outside of described body is additionally provided with chuck (1), and described chuck is connected with conduction oil in (1).
A kind of vertical reactor the most according to claim 6, it is characterised in that the top of described body is additionally provided with standby material inlet (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620338708.2U CN205517686U (en) | 2016-04-21 | 2016-04-21 | Vertical reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620338708.2U CN205517686U (en) | 2016-04-21 | 2016-04-21 | Vertical reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205517686U true CN205517686U (en) | 2016-08-31 |
Family
ID=56795807
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620338708.2U Active CN205517686U (en) | 2016-04-21 | 2016-04-21 | Vertical reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205517686U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669579A (en) * | 2017-02-24 | 2017-05-17 | 深圳市玖创科技有限公司 | Graphite-coated carbonization equipment for producing lithium battery electrode |
-
2016
- 2016-04-21 CN CN201620338708.2U patent/CN205517686U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106669579A (en) * | 2017-02-24 | 2017-05-17 | 深圳市玖创科技有限公司 | Graphite-coated carbonization equipment for producing lithium battery electrode |
| CN106669579B (en) * | 2017-02-24 | 2018-11-20 | 深圳新恒业电池科技有限公司 | A kind of graphite coat carbonizing apparatus of electrode of lithium cell production |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |