CN206325570U - A kind of reactor of homogeneous heating - Google Patents
A kind of reactor of homogeneous heating Download PDFInfo
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- CN206325570U CN206325570U CN201621454936.2U CN201621454936U CN206325570U CN 206325570 U CN206325570 U CN 206325570U CN 201621454936 U CN201621454936 U CN 201621454936U CN 206325570 U CN206325570 U CN 206325570U
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- power transmission
- reactor
- transmission shaft
- propeller
- homogeneous heating
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Abstract
The utility model discloses a kind of reactor of homogeneous heating, including shell, rabbling mechanism；Rabbling mechanism described in the utility model includes the first propeller and the second propeller, and the setting can be well mixed raw material, moreover it is possible to make contact of the raw material with nexine even closer, realize efficient heat transfer.So far, the utility model provide a kind of homogeneous heating, it is quick, while coolant evenly and rapidly reactor, the reactor has homogeneous heating, the fast advantage of firing rate.
Description
Technical field
The utility model is related to daily chemical product production equipment；Specifically related to a kind of reactor of homogeneous heating.
Background technology
Daily chemical product usage amount in the life of modern people is more and more；The species of daily chemical product also increasingly increases.
During preparing daily chemical product, it is often necessary to which heating realizes reaction or mix, for some viscosityes than larger and
The poor raw material of heat conductivility, can frequently result in heated uneven or heating and cooling duration length technological difficulties.So make
Spun out into the time used by the production time, virtually add the cost of production, can also influence the quality of product.
Utility model content
In order to overcome the deficiencies in the prior art, the purpose of this utility model is to provide for a kind of reaction of homogeneous heating
Kettle, the reactor is on the basis of common reactor, and increase is provided with the first power transmission shaft, second driving shaft, the first propeller
With the second propeller；It is so designed that, rapidly the raw material in reactor center can be flow near nexine, realize heating, this is anti-
Answering kettle has homogeneous heating, the fast advantage of firing rate.
The purpose of this utility model is realized using following technical scheme：
A kind of reactor of homogeneous heating, including shell, rabbling mechanism；The shell includes outer layer and nexine；It is described outer
Closed gap is provided between layer and nexine；The gap is used for the medium for being passed through heating or cooling；On the outer layer of the shell
It is provided with extraneous and gap the medium inlet of connection and media outlet；The bottom of shell is provided with material outlet；The mixer
Structure is installed in reactor；The rabbling mechanism includes motor, worm gear case, the first power transmission shaft, second driving shaft, the first spiral shell
Revolve oar, the second propeller；First power transmission shaft is connected with motor, and first power transmission shaft is pivotally connected with shell；Described
Two power transmission shafts are pivotally connected with shell；First power transmission shaft is connected with second driving shaft by worm gear case；Described first
Power transmission shaft and second driving shaft are mutually perpendicular to；The two ends of first power transmission shaft are provided with the first propeller；Second transmission
The two ends of axle are provided with the second propeller.
Preferably, the rabbling mechanism also includes the 3rd power transmission shaft and the 3rd propeller；3rd propeller is arranged on
The two ends of 3rd power transmission shaft；3rd power transmission shaft is connected with the first power transmission shaft by worm gear case, and the described 3rd passes
Moving axis is pivotally connected with shell；3rd power transmission shaft is vertical with the first power transmission shaft, and the 3rd power transmission shaft is vertical with second driving shaft.
Preferably, the nexine forms hollow radiating fin to reactor internal projection, and the radiating fin connects with gap
It is logical.
Preferably, the angle of the radiating fin and the first power transmission shaft is 30-60 degree.
Preferably, the angle of the radiating fin and the first power transmission shaft is 45 degree.
Preferably, installed in the first power transmission shaft close to the side of the axial thrust of first propeller of one end of reactor bottom
To towards worm gear case, the direction of the axial thrust of the first propeller of the other end dorsad worm gear case.
Preferably, the direction for the axial thrust that second propeller is produced is towards worm gear case；3rd spiral shell
The direction for the axial thrust that oar is produced is revolved towards worm gear case.
Preferably, the medium inlet is located at the bottom of reactor, and media outlet is located at the top of reactor.
Compared with prior art, the beneficial effects of the utility model are：
1st, the utility model, which is set, provides a kind of reactor of homogeneous heating, and the reactor is on the basis of common reactor
On, increase is provided with the first power transmission shaft, second driving shaft, the first propeller and the second propeller；It is so designed that, can be rapid
The raw material in reactor center is flow near nexine, heating is realized, the reactor has a homogeneous heating, fast excellent of firing rate
Point.
2nd, the nexine of reactor provided by the utility model is provided with radiating fin, in the setting can effectively increase
The contact area of layer and raw material, improves the efficiency of heat transfer；Inclined angle is also provided with simultaneously, liquid can be made to realize longitudinal direction
Flowing, increases the heat transference efficiency of different height aspect, promotes the mixing of raw material.
3rd, the utility model produces the first propeller of thrust, the second propeller, the by being provided with to worm gear case
Three propellers；The setting can make contact of the raw material with nexine closer, improve heat transference efficiency, while coordinating inclined design
Radiate fin, raw material liq is realized the convection current of levels, mixes raw material and mutually transmits heat.
Brief description of the drawings
Fig. 1 is the sectional view of embodiment 1 of the present utility model.
Wherein, 1, shell；11st, outer layer；12nd, nexine；13rd, gap；14th, material outlet；15th, media outlet；16th, medium enters
Mouthful；17th, radiate fin；2nd, rabbling mechanism；21st, worm gear case；22nd, the first power transmission shaft；221st, the first propeller；23rd, second
Power transmission shaft；231st, the second propeller；24th, motor；25th, the 3rd power transmission shaft；251st, the 3rd propeller.
Embodiment
Below, with reference to accompanying drawing and embodiment, the utility model is described further：
Embodiment 1：
As shown in figure 1, a kind of reactor of homogeneous heating, including shell 1, rabbling mechanism 2；The shell 1 includes outer layer
11 and nexine 12；Closed gap 13 is provided between the outer layer 11 and nexine 12；The gap 13 is used to be passed through heating or dropped
The medium of temperature；Extraneous and gap 13 the medium inlet 16 of connection and media outlet 15 are provided with the outer layer 11 of the shell 1；Outside
The bottom of shell 1 is provided with material outlet 14；The rabbling mechanism 2 is installed in reactor；The rabbling mechanism 2 includes motor
24th, worm gear case 21, the first power transmission shaft 22, second driving shaft 23, the first propeller 221, the second propeller 231；Described
One power transmission shaft 22 is connected with motor 24, and first power transmission shaft 22 is pivotally connected with shell 1；The second driving shaft 23 and shell
1 pivot joint；First power transmission shaft 22 is connected with second driving shaft 23 by worm gear case 21；First power transmission shaft 22
It is mutually perpendicular to second driving shaft 23；The two ends of first power transmission shaft 22 are provided with the first propeller 221；Second transmission
The two ends of axle 23 are provided with the second propeller 231.The rabbling mechanism 2 also includes the 3rd power transmission shaft 25 and the 3rd propeller 251；
3rd propeller 251 is arranged on the two ends of the 3rd power transmission shaft 25；3rd power transmission shaft 25 passes through with the first power transmission shaft 22
Worm gear case 21 is connected, and the 3rd power transmission shaft 25 is pivotally connected with shell 1.3rd power transmission shaft 25 and the first power transmission shaft
22 is vertical, and the 3rd power transmission shaft 25 is vertical with second driving shaft 23.The nexine 12 forms hollow radiating to reactor internal projection
Fin 17, the radiating fin 17 is connected with gap 13.The angle of the radiating power transmission shaft 22 of fin 17 and first is 30-60
Degree, it is preferable that the angle of the radiating power transmission shaft 22 of fin 17 and first is 45 degree.Installed in the first power transmission shaft 22 close to reaction
The direction of the axial thrust of first propeller 221 of the one end in bottom portion is towards worm gear case 21, the first spiral of the other end
The direction of the axial thrust of oar 221 dorsad worm gear case 21.The direction for the axial thrust that second propeller 231 is produced is equal
Towards worm gear case 21；The direction for the axial thrust that 3rd propeller 251 is produced is towards worm gear case 21.So
Setting can make propeller promote raw material to rush at nexine 12, make basic even closer, the effective raising heat of raw material and nexine 12
Transmission efficiency；The effect of mixing can also be realized simultaneously.The medium inlet 16 be located at reactor bottom, media outlet position 15 in
The top of reactor, is arranged such and is primarily due to the high thermal expansion of same substance temperature, and density is relatively low, easily floats.So
Longitudinal heat transfer can be realized and the utilization rate of heat energy is improved.
In use, required material is fitted into reactor, it is passed through by gap 13 of the medium inlet 16 into reactor
Heat medium, such as hot water or vapours；Flow through behind gap 13, medium flows out from media outlet 15；In this process, start
Motor 24, under the drive of motor 24, the first power transmission shaft 22, second driving shaft 23, the 3rd power transmission shaft 25 produce rotation, drive the
One propeller 221, the second propeller 231, the 3rd propeller rotation 251；Now, in the presence of propeller, by liquid charging stock
Push the direction of nexine 12 to, in the presence of impact, raw material is easily heated and mixed, improve heated or radiating effect.Instead
After the completion of answering, cold medium is passed through to media outlet 15, cooling is realized, finally discharges material from material outlet 14, mixing is completed
And its reaction.
It will be apparent to those skilled in the art that technical scheme that can be as described above and design, make other various
It is corresponding to change and deformation, and all these change and deformation should all belong to the protection of the utility model claim
Within the scope of.
Claims (9)
1. a kind of reactor of homogeneous heating, it is characterised in that：Including shell, rabbling mechanism；The shell includes outer layer and inner
Layer；Closed gap is provided between the outer layer and nexine；The gap is used for the medium for being passed through heating or cooling；The shell
Outer layer on be provided with extraneous and gap the medium inlet of connection and media outlet；The bottom of shell is provided with material outlet；Institute
Rabbling mechanism is stated to be installed in reactor；The rabbling mechanism includes motor, worm gear case, the first power transmission shaft, the second transmission
Axle, the first propeller, the second propeller；First power transmission shaft is connected with motor, first power transmission shaft and shell pivot
Connect；The second driving shaft is pivotally connected with shell；First power transmission shaft is connected with second driving shaft by worm gear case；
First power transmission shaft and second driving shaft are mutually perpendicular to；The two ends of first power transmission shaft are provided with the first propeller；It is described
The two ends of second driving shaft are provided with the second propeller.
2. the reactor of homogeneous heating according to claim 1, it is characterised in that：The rabbling mechanism also includes the 3rd and passed
Moving axis and the 3rd propeller；3rd propeller is arranged on the two ends of the 3rd power transmission shaft；3rd power transmission shaft and first is passed
Moving axis is connected by worm gear case, and the 3rd power transmission shaft is pivotally connected with shell；3rd power transmission shaft and the first transmission
Axle is vertical, and the 3rd power transmission shaft is vertical with second driving shaft.
3. the reactor of homogeneous heating according to claim 1, it is characterised in that：The nexine is to reactor internal projection shape
Into hollow radiating fin, the radiating fin is connected with gap.
4. the reactor of homogeneous heating according to claim 3, it is characterised in that：The radiating fin and the first power transmission shaft
Angle be 30-60 degree.
5. the reactor of homogeneous heating according to claim 4, it is characterised in that：The radiating fin and the first power transmission shaft
Angle be 45 degree.
6. the reactor of homogeneous heating according to claim 1, it is characterised in that：Installed in the first power transmission shaft close to reaction
The direction of the axial thrust of first propeller of the one end in bottom portion is towards worm gear case, the axle of the first propeller of the other end
To the direction of thrust dorsad worm gear case.
7. the reactor of homogeneous heating according to claim 6, it is characterised in that：The axial direction that second propeller is produced
The direction of thrust is towards worm gear case.
8. the reactor of homogeneous heating according to claim 2, it is characterised in that：The axial direction that 3rd propeller is produced
The direction of thrust is towards worm gear case.
9. the reactor of homogeneous heating according to claim 1, it is characterised in that：The medium inlet is located at reactor
Bottom, media outlet is located at the top of reactor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621454936.2U CN206325570U (en) | 2016-12-28 | 2016-12-28 | A kind of reactor of homogeneous heating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621454936.2U CN206325570U (en) | 2016-12-28 | 2016-12-28 | A kind of reactor of homogeneous heating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206325570U true CN206325570U (en) | 2017-07-14 |
Family
ID=59293320
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621454936.2U Active CN206325570U (en) | 2016-12-28 | 2016-12-28 | A kind of reactor of homogeneous heating |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206325570U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355512A (en) * | 2018-03-26 | 2018-08-03 | 湖北万禾源豆奶制品有限公司 | A kind of Fermented vegetable protein beverage processing blend tank |
| CN115646270A (en) * | 2022-11-21 | 2023-01-31 | 山东颐工材料科技股份有限公司 | PVC processing modifier production heat mixing equipment |
| CN116605909A (en) * | 2023-04-25 | 2023-08-18 | 湖南青冲新材料股份有限公司 | Electrolytic manganese dioxide purifying device and purifying method thereof |
-
2016
- 2016-12-28 CN CN201621454936.2U patent/CN206325570U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355512A (en) * | 2018-03-26 | 2018-08-03 | 湖北万禾源豆奶制品有限公司 | A kind of Fermented vegetable protein beverage processing blend tank |
| CN115646270A (en) * | 2022-11-21 | 2023-01-31 | 山东颐工材料科技股份有限公司 | PVC processing modifier production heat mixing equipment |
| CN116605909A (en) * | 2023-04-25 | 2023-08-18 | 湖南青冲新材料股份有限公司 | Electrolytic manganese dioxide purifying device and purifying method thereof |
| CN116605909B (en) * | 2023-04-25 | 2024-03-15 | 湖南青冲新材料股份有限公司 | Electrolytic manganese dioxide purifying device and purifying method thereof |
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Address after: 4 / F, building B2, No.13 Kexing West Road, Guangzhou private science and Technology Park, no.1633 Beitai Road, Baiyun District, Guangzhou, Guangdong 510000 Patentee after: Guangzhou aizhuo Biotechnology Co.,Ltd. Address before: 4 / F, building B2, No.13 Kexing West Road, Guangzhou private science and Technology Park, no.1633 Beitai Road, Baiyun District, Guangzhou, Guangdong 510000 Patentee before: GUANGZHOU AIZHUO BIOLOGICAL SCIENCE & TECHNOLOGY Co.,Ltd. |