CN208049927U - A kind of novel reaction kettle system - Google Patents
A kind of novel reaction kettle system Download PDFInfo
- Publication number
- CN208049927U CN208049927U CN201820305275.XU CN201820305275U CN208049927U CN 208049927 U CN208049927 U CN 208049927U CN 201820305275 U CN201820305275 U CN 201820305275U CN 208049927 U CN208049927 U CN 208049927U
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- CN
- China
- Prior art keywords
- reaction kettle
- kettle body
- circulation fluid
- stirring
- spirally
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model discloses a kind of novel reaction kettle systems comprising reaction kettle body, closed temperature circulatory system and blender offer circulation fluid import, circulation fluid outlet, reacting product outlet, air inlet and at least one material inlet on reaction kettle body;Temperature circulatory system includes spirally-wound tube, heat exchanger and circulating pump, and the both ends of spirally-wound tube export connection with circulation fluid import and circulation fluid respectively and spirally-wound tube is installed in reaction kettle body, and circulation fluid is provided in spirally-wound tube;Heat exchanger is connect with circulating pump, and heat exchanger and circulating pump are connect with the both ends of spirally-wound tube respectively;Blender is set in reaction kettle body and is connect with the retarder for being set to reaction kettle body bottom.The utility model is medium using circulation fluid, carries out heat exchange, and effective transformation efficiency for improving raw material keeps raw material remaining quantity less.
Description
Technical field
The utility model is related to reaction kettle apparatus fields, and in particular to a kind of novel reaction kettle system.
Background technology
Currently, reaction kettle is essential device in chemical engineering industry production, there are many gas in Chemical Manufacture
The chemical reaction for participating in occurring as raw material generally requires the reaction condition of feed change, typically to increase production efficiency
Change reaction temperature and is realized by the stirring of blender.But some chemical reactions are exothermic reactions, need to remove heat;One
A little chemical reactions are again the endothermic reactions, require supplementation with heat.Temperature control device is set in reaction kettle by some existing reaction kettles
Portion, complicated, maintenance difficult, manufacturing cost are high.
Utility model content
For the above-mentioned deficiency of the prior art, the utility model provides that a kind of feed stock conversion is high, external temperature control cycle
Novel reaction kettle system.
In order to reach foregoing invention purpose, the technical solution adopted in the utility model is:
There is provided a kind of novel reaction kettle system comprising reaction kettle body, closed temperature circulatory system and blender, reaction
Circulation fluid import, circulation fluid outlet, reacting product outlet, air inlet and at least one material inlet are offered on autoclave body;Temperature
The circulatory system includes spirally-wound tube, heat exchanger and circulating pump, and the both ends of spirally-wound tube go out with circulation fluid import and circulation fluid respectively
Mouth connects and spirally-wound tube is installed in reaction kettle body;Heat exchanger is connect with circulating pump, heat exchanger and circulating pump respectively with spiral
It is connected around the both ends of pipe;Blender includes motor, retarder, stirring rod and at least one stirring-head, and stirring rod runs through reaction kettle
Body is simultaneously connect with the retarder for being set to reaction kettle body bottom, and retarder is connect with motor;Stirring-head is set to reaction kettle body bottom
On the stirring rod in portion;Stirring rod and stirring-head are the hollow tube of mutual conduction, and one end of stirring rod is connect with air inlet, stirring
It is provided with venting ball on head, several gas vents are offered on venting ball.
Further, it is additionally provided with insulating layer on reaction kettle body, thermal insulation medium is provided in insulating layer, is opened up on insulating layer
There are thermal insulation medium import and thermal insulation medium outlet.
Further, returning charge mouth is offered at the top of reaction kettle.
The beneficial effects of the utility model are:The utility model is a kind of novel reaction kettle system, applies to have gas work
In the industrial chemistry reaction for participating in reaction for raw material, non-pneumatic raw material is injected from the material inlet on reaction kettle body, gas raw material
From the air inlet injection on reaction kettle body, gas raw material is imported reaction kettle body bottom, hair is contacted with raw material by hollow stirring rod
Raw reaction, product are discharged from product exit;Being set in the spirally-wound tube in reaction kettle body has circulation fluid, realization and reaction kettle body
Interior raw material carries out the function of heat exchange, and circulation fluid exchanges heat in external heat exchanger by being arranged with heat transferring medium, recycles
It pumps and provides basic circulation power to circulation fluid.
It is provided with stirring-head on stirring rod, is stirred in raw material reaction process, increases raw material reaction efficiency and conversion
Rate;Be discharged on the venting ball that gas raw material is arranged from stirring-head, while agitating, venting ball drive gas raw material fully with
Non-pneumatic raw material contacts, and further increases feed stock conversion and production efficiency;It is provided with insulating layer outside reaction kettle body, realizes heat preservation
Function;It is additionally provided with returning charge mouth on reaction kettle body, facilitates and the complete raw material of unreacted is added, carry out secondary response.
Description of the drawings
Fig. 1 is the schematic diagram of novel reaction kettle system.
Fig. 2 is the structural schematic diagram of venting ball.
Wherein, 1, reaction kettle body, 2,1 import of raw material, 3, air inlet, 4, returning charge mouth, 5, product exit, 6, thermal insulation medium goes out
Mouthful, 7, insulating layer, 8,2 import of raw material, 9, motor, 10, thermal insulation medium import, 11, holder, 12, stirring-head, 13, venting ball,
14, stirring rod, 15, spirally-wound tube, 16, circulation fluid outlet, 17, circulation fluid import, 18, heat transferring medium import, 19, heat transferring medium
Outlet, 20, heat exchanger, 21, circulating pump, 22, gas vent.
Specific implementation mode
Specific embodiment of the present utility model is described below, in order to facilitate understanding by those skilled in the art
The utility model, it should be apparent that the utility model is not limited to the range of specific implementation mode, to the common skill of the art
For art personnel, if various change the attached claims limit and determine the utility model spirit and scope in,
These variations are it will be apparent that all utilize the innovation and creation of the utility model design in the row of protection.
As shown in Figure 1, a kind of novel reaction kettle system includes reaction kettle body 1, spirally-wound tube 15, heat exchanger 20 and circulating pump
21, reaction kettle body 1 is installed on holder 11, and the top of reaction kettle body 1 offers 1 import 2 of raw material, air inlet 3 and returning charge mouth 4,
The bottom of reaction kettle body 1 offers 2 import 8 of raw material, and the side surface upper part of reaction kettle body 1 offers circulation fluid import 17 and bottom
Portion offers circulation fluid outlet 16.Spirally-wound tube 15 is installed in reaction kettle body 1, the both ends of spirally-wound tube 15 respectively with circulation fluid
16 connection of import 17 and circulation fluid outlet;Circulation fluid import 17 is connected with heat exchanger 20 by conduit, and one end of heat exchanger 20 connects
It is connected to circulating pump 21, circulating pump 21 is connect with circulation fluid outlet 16;Material is thus formed one using circulation fluid as the closing of medium
Temperature circulatory system.
Temperature circulatory system is real by flowing of the circulation fluid in spirally-wound tube 15 from bottom to up using circulation fluid as medium
Now with the heat exchange of raw material in reaction kettle, circulation fluid with heat transferring medium in heat exchanger 20 by realizing heat exchange;Heat exchange
Medium enters from the heat transferring medium import 18 of heat exchanger 20, from 19 discharge of heat transferring medium outlet;Circulating pump 21 is provided to circulation fluid
Circulation power forms forced circulation, keeps heat exchange more effective, further increase reaction efficiency and feed stock conversion.
When implementing, non-pneumatic raw material injects this programme from 1 import 2 of raw material and 2 import 8 of raw material, the center of reaction kettle body 1
Position is provided with hollow stirring rod 14, and the hollow stirring-head 12 be connected with stirring rod 14 is provided on 14 bottom of stirring rod,
It is preferred that stirring-head 12 is set as three, arranges in " trident " shape, and venting ball 13 is provided on stirring-head 12, on venting ball 13
Offer several gas vents 22;Gas raw material is injected from air inlet 3, and gas raw material is passed through reaction kettle by stirring rod 14
The bottom of body 1 contacts with each other with non-pneumatic raw material, forms chemical reaction, and the product that reaction product is opened up from reaction kettle body 1 goes out
Mouth 5 is discharged.
Stirring rod 14 run through 1 bottom of reaction kettle body, connect with the retarder for being set to 1 bottom of reaction kettle body, retarder and
Motor 9 connects;During reaction carries out, motor 9 drives stirring rod 14 to rotate, and stirring rod 14 drives stirring-head 12 to carry out reaction raw materials
Stirring accelerates the progress of reaction, increases the transformation efficiency of raw material;While stirring-head 12 rotates, drive gas in reaction kettle
Rotation, makes gas raw material be contacted with non-pneumatic raw material more abundant in body 1, so that feed stock conversion higher, raw material remaining
Amount is less.
This programme is preferred, and insulating layer 7 is arranged on reaction kettle body 1, is filled with thermal insulation medium in insulating layer 7, on insulating layer 7
Thermal insulation medium import 10 and thermal insulation medium outlet 6 are offered, it is convenient to replace thermal insulation medium in time, it is former to adapt to different reactions
Material, provides different reaction conditions.
Claims (3)
1. a kind of novel reaction kettle system, which is characterized in that including reaction kettle body (1), closed temperature circulatory system and stirring
Device offers circulation fluid import (17), circulation fluid outlet (16), reacting product outlet (5), air inlet on the reaction kettle body (1)
Mouth (3) and at least one material inlet;The temperature circulatory system includes spirally-wound tube (15), heat exchanger (20) and circulating pump
(21), the both ends of the spirally-wound tube (15) are connect and spiral winding with circulation fluid import (17) and circulation fluid outlet (16) respectively
Pipe (15) is installed in reaction kettle body (1);The heat exchanger (20) connect with circulating pump (21), the heat exchanger (20) and cycle
Pump (21) is connect with the both ends of spirally-wound tube (15) respectively;The blender include motor (9), retarder, stirring rod (14) and
At least one stirring-head (12), the stirring rod (14) through reaction kettle body (1) and be set to reaction kettle body (1) bottom
Retarder connects, and the retarder is connect with motor (9);The stirring-head (12) is set to the stirring of reaction kettle body (1) bottom
On bar (14);The stirring rod (14) and stirring-head (12) are the hollow tube of mutual conduction, one end of the stirring rod (14)
It is connect with air inlet (3), venting ball (13) is provided on the stirring-head (12), several rows are offered on the venting ball (13)
Stomata (22).
2. novel reaction kettle system according to claim 1, which is characterized in that be additionally provided on the reaction kettle body (1)
Insulating layer (7), the insulating layer (7) is interior to be provided with thermal insulation medium, and thermal insulation medium import (10) is offered on the insulating layer (7)
(6) are exported with thermal insulation medium.
3. novel reaction kettle system according to claim 1, which is characterized in that offer returning charge at the top of the reaction kettle
Mouth (4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820305275.XU CN208049927U (en) | 2018-03-06 | 2018-03-06 | A kind of novel reaction kettle system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820305275.XU CN208049927U (en) | 2018-03-06 | 2018-03-06 | A kind of novel reaction kettle system |
Publications (1)
Publication Number | Publication Date |
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CN208049927U true CN208049927U (en) | 2018-11-06 |
Family
ID=63991291
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201820305275.XU Expired - Fee Related CN208049927U (en) | 2018-03-06 | 2018-03-06 | A kind of novel reaction kettle system |
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CN (1) | CN208049927U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110253816A (en) * | 2019-08-02 | 2019-09-20 | 张良芹 | A kind of chemical materials polyurethane foaming machine |
CN114570083A (en) * | 2022-04-01 | 2022-06-03 | 栾川县山川生态农业开发有限公司 | Oil separator is used in walnut oil processing |
-
2018
- 2018-03-06 CN CN201820305275.XU patent/CN208049927U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110253816A (en) * | 2019-08-02 | 2019-09-20 | 张良芹 | A kind of chemical materials polyurethane foaming machine |
CN114570083A (en) * | 2022-04-01 | 2022-06-03 | 栾川县山川生态农业开发有限公司 | Oil separator is used in walnut oil processing |
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Legal Events
Date | Code | Title | Description |
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GR01 | Patent grant | ||
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: 20181106 Termination date: 20200306 |