CN206276381U - A kind of reactor of quick blend feedstock - Google Patents
A kind of reactor of quick blend feedstock Download PDFInfo
- Publication number
- CN206276381U CN206276381U CN201621290016.1U CN201621290016U CN206276381U CN 206276381 U CN206276381 U CN 206276381U CN 201621290016 U CN201621290016 U CN 201621290016U CN 206276381 U CN206276381 U CN 206276381U
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- kettle
- reactor
- circulation line
- external circulation
- spiral coil
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Abstract
The utility model discloses a kind of reactor of quick blend feedstock, including kettle, chuck, agitating paddle, stirring motor and agitating shaft, the kettle top is provided with charging aperture, and bottom is provided with discharging opening, it is characterised in that：Inner wall of kettle is provided with spiral coil, and the spiral coil is provided with some spouts, the spiral coil sealed bottom towards the tube wall inside kettle；External circulation line is additionally provided with outside the kettle, described external circulation line one end is connected with discharging opening, the other end is connected through kettle top with spiral coil, and the external circulation line is provided with centrifugal pump.The utility model can realize the Quick uniform mixing of raw material in kettle；The reaction rate of raw material in kettle can be accelerated, production efficiency is greatly improved.
Description
Technical field
The utility model is related to field of chemical equipment, and in particular to a kind of reactor of quick blend feedstock.
Background technology
The broad understanding of reactor has the container for physically or chemically reacting, and is matched somebody with somebody by the structure design to container and parameter
Put, realize the mixture function of heating, evaporation, cooling and the low high speed of technological requirement.Reactor be widely used in oil, chemical industry,
Rubber, agricultural chemicals, dyestuff, medicine, food, for completing to vulcanize, nitrifying, hydrogenate, hydrocarbonylation, polymerization, the pressure of the technical process such as condensation
Force container.
Existing reactor, be provided with mainly including kettle, chuck, agitating paddle, stirring motor and agitating shaft, in chuck for
Cooling or the outer coil pipe of heating, are provided with the inner coil pipe for cooling down or heating in kettle.This reactor is mainly by stirring
Motor drives the agitating paddle on agitating shaft to rotate, and realizes the stirring in kettle.This stirring can only realize raw material in level substantially
The rotation and mixing in direction, it is easy to cause the mixing of raw material in the vertical direction and the situation of inequality of being heated to occur.This is just big
It is big to reduce the reaction rate of overall raw material in kettle, and then reduce production efficiency.
Utility model content
Regarding to the issue above, the utility model discloses a kind of reactor of quick blend feedstock, and this reactor can realize kettle
The Quick uniform mixing of internal raw material；Liquid charging stock to be added can be also set quickly to realize uniform mixing simultaneously.Accelerate in kettle
The reaction rate of raw material, improve production efficiency.
To achieve the above object, the technical solution adopted in the utility model is：A kind of reactor of quick blend feedstock, bag
Kettle, chuck, agitating paddle, stirring motor and agitating shaft are included, the kettle top is provided with charging aperture, and bottom is provided with discharging opening, kettle
Internal wall is provided with spiral coil, and the spiral coil is provided with some spouts, the helical disk towards the tube wall inside kettle
Bottom of the tube is sealed；External circulation line is additionally provided with outside the kettle, described external circulation line one end is connected with discharging opening, and the other end is worn
Cross kettle top to be connected with spiral coil, the external circulation line is provided with centrifugal pump.
Further, the charging aperture and discharge outlet are equipped with valve.
Further, the external circulation line is connected with spiral coil flange；The spiral coil is welded in the kettle
On internal wall.
Further, the external circulation line is provided with condenser pipe.
Further, the condensation bottom of the tube is provided with cooling water inlet, and the condenser pipe top is provided with cooling water outlet.
Further, it is provided with liquid addition device on the external circulation line between the discharging opening and the centrifugal pump.
Further, the liquid addition device includes the drain of wet tank, connection liquid storage tank and external circulation line
Pipe.
Further, the wet tank top is provided with grinding port plug, is provided with for observing on the wet tank tank body
The observation window of wet tank internal liquid level, the observation window is provided with graduation mark；The catheter is provided with control valve.
Further, the outer coil pipe to kettle cooling is provided with the chuck, the chuck bottom is provided with outer coil pipe and enters
The mouth of a river, the chuck top is provided with outer coil pipe delivery port.
The beneficial effects of the utility model are：Spiral coil, spiral coil are provided with the utility model on inner wall of kettle
Some spouts, sealed bottom are provided with towards the tube wall inside kettle.And external circulation line, outer circulating tube are additionally provided with outside kettle
Road one end is connected with discharging opening, and the other end is connected through kettle top with spiral coil, and the external circulation line is provided with centrifugation
Pump.Raw material in kettle flows into external circulation line in the presence of centrifugal pump from the discharging opening of kettle, then by external circulation line stream
Enter in the spiral coil in kettle, finally the spout from helical disk tube side wall is sprayed into inside kettle.Thus make raw material
Can rapidly be well mixed in the horizontal and vertical directions.Condenser pipe is provided with external circulation line and in chuck in addition
The outer coil pipe to kettle cooling is provided with, can be made in kettle because the heat that reaction is produced is shed in time by heat exchange, make kettle
Interior reaction temperature is controlled in the range of technological requirement, prevents from increasing side reaction because reaction temperature is too high.In discharging opening
Be provided with liquid addition device with the external circulation line between the centrifugal pump, can other adding liquid raw material as needed, together
When liquid charging stock enter in spiral coil through external circulation line, then spout from helical disk tube side wall is sprayed into inside kettle, this
Liquid charging stock to be added is directly rapidly uniformly mixed and is reacted with the raw material in former kettle, improve
Production efficiency.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of the utility model spiral coil；
Fig. 3 is the A portions enlarged drawing of Fig. 1；
Wherein：1st, kettle, 1-1, charging aperture, 1-2, discharging opening；2nd, chuck；3rd, spiral coil, 3-1, spout；4th, stir
Oar；5th, stirring motor；6th, agitating shaft；7th, external circulation line；8th, centrifugal pump；9th, condenser pipe, 9-1, cooling water inlet, 9-2, cold water go out
Mouthful；10th, liquid addition device, 10-1, wet tank, 10-2, catheter, 10-3, observation window；10-4, graduation mark, 10-5, control
Valve；11st, outer coil pipe；11-1, outer coil inlets, 11-2, outer coil pipe delivery port.
Specific embodiment
Implementation method of the present utility model is described in further detail with reference to the accompanying drawings and examples.Following examples
For illustrating the utility model, but can not be used for limiting scope of the present utility model.
Fig. 1 to 3 is a specific embodiment of the present utility model：A kind of reactor of quick blend feedstock, including kettle
1st, chuck 2, agitating paddle 4, stirring motor 5 and agitating shaft 6, the top of the kettle 1 are provided with charging aperture 1-1, and bottom is provided with discharging opening
1-2.By the charging aperture 1-1 of kettle 1, to be mixed, reaction raw material is added in kettle 1, now controls the work of stirring motor 5
Make, stirring motor 5 drives agitating paddle 4 to rotate by agitating shaft 6, and the stirring of horizontal direction is carried out to raw material, is mixed raw material
Close, react.Spiral coil 3 is provided with the inwall of kettle 1, spiral coil 3 is provided with some spouts towards the tube wall inside kettle 1
3-1, the sealed bottom of the spiral coil 3；Be additionally provided with external circulation line 7 outside the kettle 1, the one end of the external circulation line 7 with
Discharging opening 1-2 is connected, and the other end is connected through the top of kettle 1 with spiral coil 3, and the external circulation line 7 is provided with centrifugal pump
8.When centrifugal pump 8 works, the raw material in kettle 1 can be entered in external circulation line 7 by discharging opening 1-2, in centrifugal pump 8
Under effect, flow through external circulation line 7 and enter in spiral coil 3.If in spiral coil 3 towards being provided with the tube wall inside kettle 1
Dry spout 3-1, and the sealed bottom of spiral coil 3, this raw material for allowing for entering in spiral coil 3 are all sprayed by spout 3-1
Enter inside kettle 1, raw material in the vertical direction is quickly well mixed, realize the overall Quick uniform mixing of raw material in kettle 1.
As one kind preferred embodiment, it is equipped with valve at the charging aperture 1-1 and discharging opening 1-2.Staff
According to the addition of actual conditions control raw material and raw material can be made to be mixed into external circulation line 7.
Used as another preferred embodiment, the external circulation line 7 is connected with the flange of spiral coil 3；The helical disk
Pipe 3 is welded on the inwall of the kettle 1.
It is preferable to carry out as another kind, the external circulation line 7 is provided with condenser pipe 9, the bottom of the condenser pipe 9 is provided with cold
Water inlet 9-1, the top of the condenser pipe 9 is provided with cooling water outlet 9-2.Condenser pipe 9, cooling water are set on external circulation line 7
Enter from cooling water inlet 9-1, and from cooling water outlet 9-2 outflows, cooling water can be made to be filled with the raw material in external circulation line 7
Divide heat exchange, the raw material in external circulation line 7 is lowered the temperature, and then reduce the temperature in kettle 1.
As other preferred embodiment, the external circulation line 7 between the discharging opening 1-2 and the centrifugal pump 8
It is provided with liquid addition device 10.The liquid addition device 10 includes wet tank 10-1, connection liquid storage tank 10-1 and follows outward
The catheter 10-2 on endless tube road 7.The wet tank 10-1 tops are provided with grinding port plug 10-6, on the wet tank 10-1 tank bodies
It is provided with and is provided with graduation mark 10-4 for observing the observation window 10-3, the observation window 10-3 of wet tank 10-1 internal liquid levels；
The catheter 10-2 is provided with control valve 10-5.When adding liquid raw material is needed, in order that raw material to be added can be with original
First raw material is rapidly performed by mixing, reacts, and liquid is provided with the external circulation line 7 between the discharging opening 1-2 and centrifugal pump 8
Body feeder 10.This liquid addition device 10 needs first to be got the raw materials ready before the use, when being got the raw materials ready, opens grinding port plug 10-
6, closing control valve 10-5, need the raw material of addition, by observation window 10-3 and graduation mark to being injected in wet tank 10-1
The amount that 10-4 controls are added, covers grinding port plug 10-6 afterwards, prevents volatility of raw material to be added.When needing adding liquid raw material
When, grinding port plug 10-6 is opened, while open that valve 10-5 is controlled, it is to be added in wet tank 10-1 in the presence of centrifugal pump 8
Liquid charging stock enters in external circulation line 7, then is sprayed into kettle 1 by the spout 3-1 on spiral coil 3, realizes quick mixed
Close.The amount of liquid to be added can also be determined by the graduation mark 10-4 on observation window 10-3, after the completion of addition, control is closed
Control valve 10-5, while covering grinding port plug 10-6.
It is preferable to carry out as another kind of the present utility model, the outer coil pipe 11 to the cooling of kettle 1 is provided with the chuck 2,
The bottom of the chuck 2 is provided with outer coil inlets 11-1, and the top of the chuck 2 is provided with outer coil pipe delivery port 11-2.In kettle 1
Substantial amounts of heat is often produced when raw material is reacted, the temperature of kettle 1 is constantly raised, if the temperature of kettle 1 is too high exceeding
After technological requirement temperature, side reaction can not only increased, while can also accelerate the inside agitating paddle 4 of kettle 1, agitating shaft 6, helical disk
The corrosion of pipe 3 and the inwall of kettle 1, reduces the service life of equipment.Cooling water is flowed into from outer coil inlets 11-1, from outer coil pipe
Delivery port 11-2 flows out, and sufficient heat exchange occurs with kettle 1, takes away substantial amounts of heat, realizes the cooling to kettle 1.
Finally it should be noted that：Above example is only used to illustrate the technical solution of the utility model, rather than its limitations；
Although being described in detail to the utility model with reference to the foregoing embodiments, it will be understood by those within the art that：
It can still be modified to the technical scheme described in previous embodiment, or which part technical characteristic is equal to
Replace；And these modifications or replacement, the essence of appropriate technical solution is departed from the utility model embodiment technical scheme
Spirit and scope.
Claims (9)
1. a kind of reactor of quick blend feedstock, including kettle (1), chuck (2), agitating paddle (4), stirring motor (5) and stir
Axle (6) is mixed, kettle (1) top is provided with charging aperture (1-1), and bottom is provided with discharging opening (1-2), it is characterised in that：Kettle (1)
Inwall is provided with spiral coil (3), and the spiral coil (3) is provided with some spout (3- towards the internal tube wall of kettle (1)
1), spiral coil (3) sealed bottom；External circulation line (7), the external circulation line (7) are additionally provided with outside the kettle (1)
One end is connected with discharging opening (1-2), and the other end is connected through kettle (1) top with spiral coil (3), the external circulation line
(7) it is provided with centrifugal pump (8).
2. the reactor of a kind of quick blend feedstock according to claim 1, it is characterised in that：The charging aperture (1-1)
Valve is equipped with discharging opening (1-2) place.
3. the reactor of a kind of quick blend feedstock according to claim 1, it is characterised in that：The external circulation line
(7) it is connected with spiral coil (3) flange；The spiral coil (3) is welded on the kettle (1) inwall.
4. the reactor of a kind of quick blend feedstock according to claim 1, it is characterised in that：The external circulation line
(7) it is provided with condenser pipe (9).
5. the reactor of a kind of quick blend feedstock according to claim 4, it is characterised in that：Condenser pipe (9) bottom
Portion is provided with cooling water inlet (9-1), and condenser pipe (9) top is provided with cooling water outlet (9-2).
6. the reactor of a kind of quick blend feedstock according to claim 1, it is characterised in that：In the discharging opening (1-
2) it is provided with liquid addition device (10) with the external circulation line (7) between the centrifugal pump (8).
7. the reactor of a kind of quick blend feedstock according to claim 6, it is characterised in that：The liquid addition device
(10) including the catheter (10-2) of wet tank (10-1), connection liquid storage tank (10-1) and external circulation line (7).
8. the reactor of a kind of quick blend feedstock according to claim 7, it is characterised in that：Wet tank (the 10-
1) top is provided with grinding port plug (10-6), is provided with wet tank (10-1) tank body internal for observing wet tank (10-1)
The observation window (10-3) of liquid level, the observation window (10-3) is provided with graduation mark (10-4)；The catheter (10-2) is provided with
Control valve (10-5).
9. the reactor of a kind of quick blend feedstock according to claim 1, it is characterised in that：Set in the chuck (2)
There is the outer coil pipe (11) to kettle (1) cooling, chuck (2) bottom is provided with outer coil inlets (11-1), the chuck (2)
Top is provided with outer coil pipe delivery port (11-2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621290016.1U CN206276381U (en) | 2016-11-29 | 2016-11-29 | A kind of reactor of quick blend feedstock |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621290016.1U CN206276381U (en) | 2016-11-29 | 2016-11-29 | A kind of reactor of quick blend feedstock |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206276381U true CN206276381U (en) | 2017-06-27 |
Family
ID=59076054
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621290016.1U Active CN206276381U (en) | 2016-11-29 | 2016-11-29 | A kind of reactor of quick blend feedstock |
Country Status (1)
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| CN (1) | CN206276381U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107913659A (en) * | 2017-12-28 | 2018-04-17 | 江苏东邦科技有限公司 | A kind of reaction kettle for TPU production of resins |
| CN109331701A (en) * | 2018-11-29 | 2019-02-15 | 童威洪 | A kind of allotment emulsion tank |
| CN109513946A (en) * | 2018-10-30 | 2019-03-26 | 金川集团股份有限公司 | A kind of apparatus and method preparing big partial size palladium powder |
| CN110127893A (en) * | 2019-05-05 | 2019-08-16 | 浙江大东吴集团建设有限公司 | A kind of assembled sewage-treatment plant |
| CN110227401A (en) * | 2019-06-04 | 2019-09-13 | 扬州天启新材料股份有限公司 | A kind of cyanate ester resin esterification technique |
| CN110302736A (en) * | 2019-08-07 | 2019-10-08 | 上海蓝科石化环保科技股份有限公司 | Exchange heat polymerization reaction system and method in a kind of kettle for strongly exothermic polymerization reaction |
| CN110590657A (en) * | 2019-09-16 | 2019-12-20 | 山东尚舜化工有限公司 | Equipment and process for full-automatic continuous production of antioxidant RD |
| CN112705144A (en) * | 2020-12-25 | 2021-04-27 | 黄伟辉 | Unitized compound synthesis reaction kettle |
-
2016
- 2016-11-29 CN CN201621290016.1U patent/CN206276381U/en active Active
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107913659A (en) * | 2017-12-28 | 2018-04-17 | 江苏东邦科技有限公司 | A kind of reaction kettle for TPU production of resins |
| CN109513946A (en) * | 2018-10-30 | 2019-03-26 | 金川集团股份有限公司 | A kind of apparatus and method preparing big partial size palladium powder |
| CN109513946B (en) * | 2018-10-30 | 2020-05-15 | 金川集团股份有限公司 | Device and method for preparing large-particle-size palladium powder |
| CN109331701A (en) * | 2018-11-29 | 2019-02-15 | 童威洪 | A kind of allotment emulsion tank |
| CN110127893A (en) * | 2019-05-05 | 2019-08-16 | 浙江大东吴集团建设有限公司 | A kind of assembled sewage-treatment plant |
| CN110127893B (en) * | 2019-05-05 | 2024-05-31 | 浙江大东吴集团建设有限公司 | Assembled sewage treatment plant |
| CN110227401A (en) * | 2019-06-04 | 2019-09-13 | 扬州天启新材料股份有限公司 | A kind of cyanate ester resin esterification technique |
| CN110227401B (en) * | 2019-06-04 | 2020-05-29 | 扬州天启新材料股份有限公司 | Cyanate ester resin esterification process |
| CN110302736A (en) * | 2019-08-07 | 2019-10-08 | 上海蓝科石化环保科技股份有限公司 | Exchange heat polymerization reaction system and method in a kind of kettle for strongly exothermic polymerization reaction |
| CN110590657A (en) * | 2019-09-16 | 2019-12-20 | 山东尚舜化工有限公司 | Equipment and process for full-automatic continuous production of antioxidant RD |
| CN110590657B (en) * | 2019-09-16 | 2020-11-17 | 山东尚舜化工有限公司 | Equipment and process for full-automatic continuous production of antioxidant RD |
| CN112705144A (en) * | 2020-12-25 | 2021-04-27 | 黄伟辉 | Unitized compound synthesis reaction kettle |
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