CN208810079U - A kind of multiphase flow heterogeneous catalytic reaction device - Google Patents
A kind of multiphase flow heterogeneous catalytic reaction device Download PDFInfo
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- CN208810079U CN208810079U CN201821124511.4U CN201821124511U CN208810079U CN 208810079 U CN208810079 U CN 208810079U CN 201821124511 U CN201821124511 U CN 201821124511U CN 208810079 U CN208810079 U CN 208810079U
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Abstract
The utility model discloses a kind of multiphase flow heterogeneous catalytic reaction devices, including upper cavity, middle cavity, lower chamber, No.1 water inlet pipe road, No. two water inlet pipe roads, solid reactor side wall, solid reactor top mesh and water conservancy diversion flange, the inner bottom of the solid reactor side wall and solid reactor top mesh formation of solid polycomplex reactor is filled with solid reactant catalyst, the inside of solid reactor is arranged in No.1 water inlet pipe road, and the middle cavity is internally provided with Cyclonic reactor and several strengthening reactors.A kind of multiphase flow heterogeneous catalytic reaction device described in the utility model, equipped with Cyclonic reactor, knock-on reaction device and submergence Circulative impinging stream generator, it solves multiphase flow heterogeneous mass transfer and reacts the extremely strong contradiction of timeliness with catalysis, energy is efficiently utilized simultaneously, avoid the energy loss in heterogeneous mass transfer is reacted with catalysis, the utilization rate of energy is further improved, better prospect of the application is brought.
Description
Technical field
The utility model relates to field of catalytic reactions, in particular to a kind of multiphase flow heterogeneous catalytic reaction device.
Background technique
Heterogeneous reaction refers to the component that reactant is two-phase or two-phase or more or one or more reactants at interface
The general name of the chemical reaction of upper progress；There are certain drawbacks when in use in existing multiphase flow heterogeneous catalytic reaction device,
A large amount of energy is consumed, the waste of the energy is caused, catalytic efficiency is low, and exhaust gas and sewage can be generated during reaction, pollutes
Environment, reactant is easily separated, and reaction rate is slow, and certain influence is brought to the use of catalyst reaction device, for this purpose, we mention
A kind of multiphase flow heterogeneous catalytic reaction device out.
Summary of the invention
The main purpose of the utility model is to provide a kind of multiphase flow heterogeneous catalytic reaction devices, can effectively solve
The problems in background technique.
To achieve the above object, a kind of technical solution that the utility model is taken are as follows: multiphase flow heterogeneous catalytic reaction dress
It sets, including upper cavity, middle cavity, lower chamber, No.1 water inlet pipe road, No. two water inlet pipe roads, solid reactor side wall, solid reaction
Device top mesh and water conservancy diversion flange, the solid reactor side wall are interior with solid reactor top mesh formation of solid polycomplex reactor
Portion bottom end is filled with solid reactant catalyst, and the inside of solid reactor, the lumen is arranged in No.1 water inlet pipe road
Body is internally provided with Cyclonic reactor and several strengthening reactors, and cyclone cavity is provided on Cyclonic reactor, institute
It states at the position that strengthening reactor is arranged between upper cavity and lower chamber, No. two can be set on the outside of the strengthening reactor
Electromagnetism cable and permanent magnetic iron, the lateral surface of the middle cavity is at least provided with a fluid inlet tube, and fluid inlet tube is eccentric
In tangential insertion cyclone cavity, the top of the Cyclonic reactor is fixedly connected with the upper plate of middle cavity, the cyclone chamber
The inner upper end of body is provided with top overflow pipe, and top overflow pipe is fixedly connected with the upper plate of middle cavity, the cyclone chamber
No.1 electromagnetism cable can be set on the outside of body, the bottom of the cyclone cavity is provided with No.1 flange, described to strengthen instead
The outlet at bottom of device is answered to be connected with No. two flanges, the lower chamber is internally provided with knock-on reaction device, the knock-on reaction device
Including ram cavity, several No. two flanges being installed on it, submergence Circulative impinging stream generator, knock-on reaction fluid flow guiding
Pipe, knock-on reaction fluid conduction pipeline, knock-on reaction fluid inlet flange and water outlet, the submergence Circulative impinging stream generator
It is symmetrically mounted at the inside of knock-on reaction device, the knock-on reaction fluid flow guiding pipe is connected to submergence Circulative impinging stream generator
At position between knock-on reaction device, the side wall that described knock-on reaction fluid flow guiding pipe one end passes through the guide shell enters leaching
Do not have inside Circulative impinging stream generator, the other end and the water conservancy diversion flanged joint being mounted on knock-on reaction device side wall, the water conservancy diversion
Part of the flange on the outside of knock-on reaction device, by the knock-on reaction fluid conduction piping connection to being mounted on lower chamber cavity
Knock-on reaction fluid inlet flange on outer wall.
The submergence Circulative impinging stream generator includes guide shell, screw propeller, drive shaft and driving motor, described
The side lower of guide shell is provided with several mesh, and one end of the guide shell is mounted on the cavity of knock-on reaction device,
And the other end of guide shell is directed toward the center of submergence Circulative impinging stream generator, the driving motor is mounted on knock-on reaction device
On the outside of cavity, connecting line is connected between the outlet of the strengthening reactor and No. two flanges.
Preferably, the solid reactor side wall is stainless steel cylinder structure, and the top of the cyclone cavity is circle
Tubular structure, and the lower part of cyclone cavity is conical structure.
Preferably, the fluid in the knock-on reaction fluid flow guiding pipe include liquid, gas, in solid any one or
The multiphase flow fluid being made of many kinds of substance.
Preferably, the cyclone cavity includes but is not limited to the cyclone that outside is provided with No.1 electromagnetism cable (207)
The cyclone cavity that cavity, outside are provided with the cyclone cavity of permanent magnetic iron (209), outside is arranged without other.
Preferably, the bottom of the solid reactor side wall and solid reactor top mesh formation of solid polycomplex reactor covers
There is solid, which includes but is not limited to solid reactant, solid catalyst.
Preferably, No. two flanges are mounted on the exit position of strengthening reactor by connecting line.
Preferably, one end of the drive shaft is connected in the rotation axis of driving motor, and the other end connection of drive shaft
In the inside of guide shell.
Compared with prior art, the utility model has the following beneficial effects: the multiphase flow heterogeneous catalytic reaction device,
By the Cyclonic reactor of setting, by different densities, different in flow rate, substance of different nature form with identical flow velocity, that
Non-steady state multiphase flow fluid that this dissolves each other, with quasi saturation dissolution characteristics, improves the reaction rate of raw material, passes through setting
Knock-on reaction device makes the condition for initially forming heterogeneous catalysis between the intracorporal different material of multiphase flow with reacting, and fills reaction
Point, by the submergence Circulative impinging stream generator of setting, raw material is saved, reduces pollution level, whole device is simple, operation side
Just, using effect is more preferable relative to traditional approach.
Detailed description of the invention
Fig. 1 is a kind of schematic view of the front view of multiphase flow heterogeneous catalytic reaction device of the utility model；
Fig. 2 is solid reactor overlooking structure diagram in Fig. 1；
Fig. 3 is the cyclone cavity schematic view of the front view of Fig. 1；
Fig. 4 is the cyclone cavity overlooking structure diagram of Fig. 3；
Fig. 5 is another situation schematic diagram in Fig. 4；
Fig. 6 is the submergence Circulative impinging stream generator overlooking structure diagram in Fig. 1；
Fig. 7 is the multiphase flow heterogeneous catalytic reaction apparatus structure schematic diagram for being mounted with heterogeneous reaction catalytic unit 210；
In figure: 1, upper cavity；2, middle cavity；3, lower chamber；101, No.1 water inlet pipe road；102, No. two water inlet pipe roads；
103, solid reactor side wall；104, solid reactor top mesh；105, solid reactant catalyst；112, pressure relief valve；
201, Cyclonic reactor；202, cyclone cavity；203, top overflow pipe；204, fluid inlet tube；205, No.1 flange；206,
Strengthening reactor；207, No.1 electromagnetism cable；208, No. two electromagnetism cables；209, permanent magnetic iron；210, heterogeneous reaction is catalyzed
Equipment；301, knock-on reaction device；302, No. two flanges；304, water outlet；305, guide shell；306, cylinder mesh；307, propeller
Propeller；308, connecting line；309, knock-on reaction fluid flow guiding pipe；310, water conservancy diversion flange；311, drive shaft；312, driving electricity
Machine；313, Circulative impinging stream generator is submerged；314, knock-on reaction fluid inlet flange；315 knock-on reaction fluid conduction pipelines.
Specific embodiment
To be easy to understand the technical means, creative features, achievement of purpose, and effectiveness of the utility model, below
In conjunction with specific embodiment, the utility model is further described.
As shown in figures 1 to 6, a kind of multiphase flow heterogeneous catalytic reaction device, including upper cavity 1, middle cavity 2, lower chamber 3,
The water inlet pipe road 102 of No.1 water inlet pipe road 101, two, solid reactor side wall 103, solid reactor top mesh 104 and water conservancy diversion
The inner bottom of flange 310, solid reactor side wall 103 and 104 formation of solid polycomplex reactor of solid reactor top mesh is filled
There is solid reactant catalyst 105, the inside of solid reactor, the inside setting of middle cavity 2 is arranged in No.1 water inlet pipe road 101
There are Cyclonic reactor 201 and several strengthening reactors 206, and be provided with cyclone cavity 202 on Cyclonic reactor 201, by force
Change reactor 206 to be arranged at the position between upper cavity 1 and lower chamber 3, the lateral surface of middle cavity 2 is at least provided with a fluid
Inlet tube 204, and in the eccentric tangential insertion cyclone cavity 202 of fluid inlet tube 204, the top of Cyclonic reactor 201 is in
The upper plate of cavity 2 is fixedly connected, and the inner upper end of cyclone cavity 202 is provided with top overflow pipe 203, and top overflow pipe
203 are fixedly connected with the upper plate of middle cavity 2, and the outside of Cyclonic reactor cavity 202 is equipped with electromagnetism cable 207；Cyclone chamber
The outside of body 202 is provided with No.1 electromagnetism cable 207, and the bottom of cyclone cavity 202 is provided with No.1 flange 205, strengthens anti-
The outlet at bottom of device 206 is answered to be connected with No. two flanges 302 by connecting line 308, lower chamber 3 is internally provided with knock-on reaction
Device 301, knock-on reaction device 301 include ram cavity, several No. two flanges 302 being installed on it, submergence Circulative impinging stream
Generator 313, knock-on reaction fluid flow guiding pipe 309, knock-on reaction fluid conduction pipeline 315, knock-on reaction fluid inlet flange
314 and water outlet 304, submergence Circulative impinging stream generator 313 is symmetrically mounted at the inside of knock-on reaction device 301, hits anti-
Fluid flow guiding pipe 309 is answered to be connected at the position between submergence Circulative impinging stream generator 313 and knock-on reaction device 301, it is described
The side wall that 309 one end of knock-on reaction fluid flow guiding pipe passes through the guide shell 305 enters in submergence Circulative impinging stream generator 313
Portion, the other end are connect with the water conservancy diversion flange 310 being mounted on 301 side wall of knock-on reaction device, and the water conservancy diversion flange 310 is being hit instead
The part for answering 301 outside of device, is connected to by the knock-on reaction fluid conduction pipeline 315 and is mounted on 3 chamber outer wall of lower chamber
On knock-on reaction fluid inlet flange 314.
Submerging Circulative impinging stream generator 313 includes guide shell 305, screw propeller 307, drive shaft 311 and driving
Motor 312, the side lower of guide shell 305 are provided with several mesh 306, and it is anti-that one end of guide shell 305 is mounted on shock
On the cavity for answering device 301, and the other end of guide shell 305 is directed toward the center of submergence Circulative impinging stream generator 313, driving motor
312 are mounted on the outside of the cavity of knock-on reaction device 301, are connected between the outlet of strengthening reactor 206 and No. two flanges 302
Take over road 308.
The flange in the bottom 205 of the Cyclonic reactor 201 including but not limited to side in its Cyclonic reactor cavity is equipped with
The flange in the bottom of heterogeneous reaction catalytic unit, the normally closed flange for not installing other equipment, the heterogeneous reaction catalytic unit
Including but not limited to ultrasonic vibrator, electromagnet, quartz burner, laser emitter；As shown in Figure 1, Cyclonic reactor 201
The flange of bottom is normally closed flange, without other settings on the outside of the cyclone cavity.
As shown in fig. 7, the flange of 201 bottom of Cyclonic reactor side in Cyclonic reactor cavity be equipped with it is heterogeneous anti-
Catalytic unit 210 is answered, the heterogeneous reaction catalytic unit 210 includes but is not limited to ultrasonic vibrator, electromagnet, ultraviolet light
Fluorescent tube, laser emitter.
As shown in fig. 7, the outside of strengthening reactor 206 is provided with No. two electromagnetism cables 208 and permanent magnetic iron 209, it is described
Wound form electromagnetic coil is provided on the outside of cyclone cavity.
As shown in figs. 1-7, solid reactor side wall 103 is stainless steel cylinder structure, and the top of cyclone cavity 202 is circle
Shape tubular structure, and the lower part of cyclone cavity 202 is conical structure；Fluid packet in knock-on reaction fluid flow guiding pipe 309
Include liquid, gas, any one or the multiphase flow fluid that is made of multiple fluid in solid；Solid reactor side wall 103 with
The bottom of 104 formation of solid polycomplex reactor of solid reactor top mesh is covered with solid, which includes but is not limited to that solid is anti-
Answer object, solid catalyst；No. two flanges 302 are mounted on the exit position of strengthening reactor 206 by connecting line 308；It drives
One end of moving axis 311 is connected in the rotation axis of driving motor 312, and the other end of drive shaft 311 is connected to guide shell 305
It is internal.
As shown in figs. 1-7, the flange of 201 bottom of Cyclonic reactor can by its Cyclonic reactor cavity side pacify
Heterogeneous reaction catalytic unit is filled, so that multiphase flow fluid is obtained better mass transfer and reaction condition, while can also be by unloading
Flange in the bottom is stated, the equipment installed thereon is safeguarded, and the intracorporal fluid of Cyclonic reactor chamber is discharged, removes dirt
Dirt or other sediments.
It should be noted that the utility model is a kind of multiphase flow heterogeneous catalytic reaction device, when in use, solid is anti-
Answer 104 formation of solid polycomplex reactor of device side wall 103 and solid reactor top mesh, Cyclonic reactor 201, strengthening reactor 206
The overall structure of catalyst reaction device, solid reaction are constituted with knock-on reaction device 301 and submergence Circulative impinging stream generator 313
The inner bottom of device side wall 103 and 104 formation of solid polycomplex reactor of solid reactor top mesh is catalyzed filled with solid reactant
Agent 105, under the effect of 312 pressure of driving motor, knock-on reaction fluid enters knock-on reaction device 301 sequentially through knock-on reaction fluid
Mouth flange 314, knock-on reaction fluid conduction pipeline 315, knock-on reaction fluid flow guiding pipe 309 are mounted on knock-on reaction device 301
One end of water conservancy diversion flange 310 enter in knock-on reaction device 301, and pass through knock-on reaction fluid flow guiding pipe 309, into being mounted on
In 313 guide shell 305 of submergence Circulative impinging stream generator on knock-on reaction device 301, driving motor 312 passes through drive shaft 311
Driving is mounted on 307 trandfer fluid of screw propeller of two 305 centers of guide shell along 305 flow at high speed of guide shell,
The huge liquid flowing for being directed toward 301 center of knock-on reaction device is formed inside guide shell 305, and at 305 bottom of guide shell
Portion forms huge suction, is equipped with the fluid in knock-on reaction device 301 constantly from 305 side lower of guide shell several
A mesh 306 is inhaled into guide shell 305, forms ellipsoid impingement region, the impingement region in 301 center of knock-on reaction device
Inside be enriched shock fluid, complete hit fluid quick catalysis, reaction while mobility big quantity of fluid from No. two methods
It is poured in orchid 302, forms mutual violent infiltration, mass transfer with impingement region fluid, be finally completed synchronous mass transfer, catalysis, reaction
Process, the multiphase flow fluid after completing heterogeneous catalytic reaction pass through the outlet for being mounted on 301 bottom of knock-on reaction device, pass through pipe
Road is output to outside multiphase flow heterogeneous catalytic reaction device knock-on reaction device 301；
Fluid tangentially enters installation by 204 high speed of fluid inlet tube being mounted on the lateral surface of middle cavity 2 when beginning
In the Cyclonic reactor 201 in middle cavity 2, fluid forms the downward centrifugal cyclone of high-speed screw in Cyclonic reactor 201
Movement, and it is centrally formed axial vacuum area in high speed centrifugation swirling motion, the materials of low density such as gas are under the influence of centrifugal force
It is precipitated, concentrates on axial vacuum area, the gas for being enriched in central axis zone constantly cuts around it and does high-speed rotating liquid, complete
Mass transport process is hit at fluid first time eddy flow, flow velocity increases during fluid decline, fluid when reaching No.1 flange 205
Flow velocity reaches maximum, and changes fluid direction of motion under pressure, and fluid does high speed impact along axial vacuum area upwards, stream
Body flow velocity moment from height to zero point, generates first time Hydrodynamic cavitation effect, and the Hydrodynamic cavitation intensity generated during this is not enough to
Its original property of molecular changes is caused, but is enough to break fluid molecule cluster, enhances multiphase flow heterogeneous mass transfer effect, simultaneously
Cavitation generates instantaneous high temperature, high pressure and ultrasonic energy, makes to initially form heterogeneous urge between the intracorporal different material of multiphase flow
The condition changed and reacted, fluid pass through the pipeline of top overflow pipe 203 and its connection, enter epicoele from No.1 water inlet pipe road 101
1 inner space of body, high-velocity fluid is after flowing through the No.1 water inlet pipe road 101 of upper cavity 1, in solid reactor center moment
It is released, flow velocity moment reduces, and generates second of Hydrodynamic cavitation effect, this time cavitation processes generate energy than first time cavitation
Intensity is bigger, it is sufficient to break active force between fluid molecule, but due to quickly entering larger low-voltage space, it is disorderly that fluid enters low speed
Stream mode, insoluble low density gas moment lose constraint, overflow from heterogeneous fluid, and the stabilization of fluid is saturated in heterogeneous fluid
Property is consolidated, and mass transfer effect is further enhanced, and fluid does irregular movement in upper cavity 1, ensure that spilling gas
Time of contact and contact area between heterogeneous fluid, fluid form delay in upper cavity 1, cause pressure in upper cavity 1
Increase, fluid enters reinforcing by the pipeline for being mounted on No. two water inlet pipe roads 102 of 1 bottom of upper cavity and its coupling under high pressure
Reactor 206, in the process, heterogeneous fluid discharge in solid reactor and eventually by being equipped at the top of solid reactor
During solid reactor top mesh 104 overflows, filled with the solid reactant catalyst 105 being covered in solid reactor
Tap touching, the liquid substance-gas reactant-solid reactant first time completed in multiphase flow under flow regime are heterogeneous
Synchronous catalysis, reaction process, are as a result the reduction of degree of saturation of the indissoluble substance in multiphase flow, make multiphase flow fluid difference phase
The mass-transfer efficiency of substance enhances, and provides advantage for later period catalysis reaction, overflows gas and heterogeneous fluid enters by force simultaneously
Change in reactor 206, since strengthening reactor 206 is using flow direction from top to down, fluid density is caused with characteristic difference
Heterogeneous fluid constantly impacts the lower spilling gas of flow velocity, ensure that overflow time of contact between gas and heterogeneous fluid and
Contact area, gas and liquid form vortex-like flowing and then are sufficiently mixed and contact in strengthening reactor 206, and mass transfer effect obtains
To further enhancing, fluid enters No. two flanges by 206 bottom water outlet 304 of strengthening reactor and by connecting line 308
302, fluid is entered in knock-on reaction device 301 by No. two flanges 302 of knock-on reaction device 301, and pressure abrupt release forms rapids
Stream, knock-on reaction fluid is mounted on by knock-on reaction fluid flow guiding pipe 309 and hits under the effect of external pumping pressure at the same time
310 one end of water conservancy diversion flange for hitting 301 outside of reactor enters in knock-on reaction device 301, and passes through knock-on reaction fluid flow guiding pipe
309, into the guide shell 305 being mounted on knock-on reaction device 301, driving motor 312 is mounted on by the driving of drive shaft 311
307 trandfer fluid of screw propeller of two 305 centers of guide shell is along 305 flow at high speed of guide shell, in guide shell 305
Inside forms the huge liquid flowing for being directed toward 301 center of knock-on reaction device, and is formed in 305 bottom of guide shell huge
Suction, several mesh 306 for being equipped with the fluid in knock-on reaction device 301 constantly from 305 side lower of guide shell are inhaled
Enter in guide shell 305, the liquid that high speed ejects in two guide shells 305 forms ellipse in 301 center of knock-on reaction device
Body shape high velocity turbulent flow impingement region is enriched in the impingement region and hits differential responses object or catalytic materials that fluid is loaded with, in impingement region
Mass transfer, catalysis, reaction is inside rapidly completed, region of the reaction product constantly to outside impingement region is permeated mass transfer, simultaneously flowed
A large amount of fluids of dynamic property are poured in from No. two flanges 302, to the continuous diffusion of impingement region, in impingement region and its fringe region in pole
It is completed in short time and hits mass transfer, catalysis reaction, heterogeneous reaction, liquid phase diffusion, the same stepping of the multiple processes of homogeneous reaction
Row solves multiphase flow reinforcing mass transfer catalysis and reacts the extremely strong contradiction of timeliness, while energy is efficiently utilized, and is greatly decreased
Idle energy consumption and loss in heterogeneous mass transfer, catalysis, reaction process, it is more practical.
The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (9)
1. a kind of multiphase flow heterogeneous catalytic reaction device, including upper cavity (1), middle cavity (2), lower chamber (3), No.1 enter water
Pipeline (101), No. two water inlet pipe roads (102), solid reactor side wall (103), solid reactor top mesh (104) and water conservancy diversion
Flange (310), it is characterised in that:
The inner bottom of the solid reactor side wall (103) and solid reactor top mesh (104) formation of solid polycomplex reactor
Filled with solid reactant catalyst (105), the inside of solid reactor is arranged in No.1 water inlet pipe road (101)；
The middle cavity (2) is internally provided with Cyclonic reactor (201) and several strengthening reactors (206), and eddy flow is anti-
It answers and is provided on device (201) cyclone cavity (202), the strengthening reactor (206) is arranged in upper cavity (1) and lower chamber
(3) at the position between, the lateral surface of the middle cavity (2) is at least provided with a fluid inlet tube (204), and fluid inlet tube
(204) in eccentric tangential insertion cyclone cavity (202), the top of the Cyclonic reactor (201) and the upper plate of middle cavity (2)
It is fixedly connected, the inner upper end of the cyclone cavity (202) is provided with top overflow pipe (203), and top overflow pipe (203)
It is fixedly connected with the upper plate of middle cavity (2), the bottom of the cyclone cavity (202) is provided with No.1 flange (205), described strong
The outlet at bottom for changing reactor (206) is connected with No. two flanges (302) by connecting line (308)；
The lower chamber (3) is internally provided with knock-on reaction device (301), and the knock-on reaction device (301) includes ram chamber
Body, several No. two flanges (302) being installed on it, submergence Circulative impinging stream generator (313), knock-on reaction fluid flow guiding pipe
(309), knock-on reaction fluid conduction pipeline (315), knock-on reaction fluid inlet flange (314) and water outlet (304), the leaching
Do not have Circulative impinging stream generator (313) to be symmetrically mounted at the inside of knock-on reaction device (301), the knock-on reaction fluid flow guiding
Pipe (309) is connected at the position between submergence Circulative impinging stream generator (313) and knock-on reaction device (301), the submergence
Circulative impinging stream generator (313) includes guide shell (305), screw propeller (307), drive shaft (311) and driving motor
(312), the side of the guide shell (305) is provided with several mesh (306), the guide shell close to driving motor side
(305) one end is mounted on the cavity of knock-on reaction device (301), and the other end of guide shell (305) is directed toward submergence circulation and hits
The center of flow-generator (313) is hit, the driving motor (312) is mounted on the outside of the cavity of knock-on reaction device (301).
2. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the solid reaction
Device side wall (103) is stainless steel cylinder structure, and the top of the cyclone cavity (202) is rounded cylindrical structure, and cyclone
The lower part of cavity (202) is conical structure.
3. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the knock-on reaction
The side wall that fluid flow guiding pipe (309) one end passes through the guide shell (305) enters in submergence Circulative impinging stream generator (313)
Portion, the other end are connect with the water conservancy diversion flange (310) being mounted on knock-on reaction device (301) side wall, and the water conservancy diversion flange (310) exists
Part on the outside of knock-on reaction device (301) is connected to by the knock-on reaction fluid conduction pipeline (315) and is mounted on lower chamber
(3) the knock-on reaction fluid inlet flange (314) on chamber outer wall.
4. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the knock-on reaction
Fluid in fluid flow guiding pipe (309) includes liquid, gas, any one or the multiphase flow that is made of many kinds of substance in solid
Fluid.
5. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the cyclone chamber
Body includes but is not limited to that outside is provided with the cyclone cavity of No.1 electromagnetism cable (207), outside is provided with permanent magnetic iron (209)
Cyclone cavity, the cyclone cavity that is arranged without other of outside.
6. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the solid reaction
The bottom of device side wall (103) and solid reactor top mesh (104) formation of solid polycomplex reactor is covered with solid, which includes
But it is not limited to solid reactant, solid catalyst.
7. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the reinforcing reaction
Device (206) includes but is not limited to that outside is provided with the strengthening reactor of No. two electromagnetism cables (208), outside is provided with permanent magnetic iron
(209) strengthening reactor that strengthening reactor, outside are arranged without other.
8. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: No. two flanges
(302) exit position of strengthening reactor (206) is connected to by connecting line (308).
9. a kind of multiphase flow heterogeneous catalytic reaction device according to claim 1, it is characterised in that: the drive shaft
(311) one end is connected in the rotation axis of driving motor (312), and the other end of drive shaft (311) is connected to guide shell
(305) inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821124511.4U CN208810079U (en) | 2018-07-16 | 2018-07-16 | A kind of multiphase flow heterogeneous catalytic reaction device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821124511.4U CN208810079U (en) | 2018-07-16 | 2018-07-16 | A kind of multiphase flow heterogeneous catalytic reaction device |
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| CN208810079U true CN208810079U (en) | 2019-05-03 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108671876A (en) * | 2018-07-16 | 2018-10-19 | 山东绿色自由基科技研究中心 | A kind of multiphase flow heterogeneous catalytic reaction device |
| CN110314619A (en) * | 2019-07-29 | 2019-10-11 | 浙江工业大学 | A kind of hypergravity outer circulation reactor for heterogeneous catalytic reaction |
-
2018
- 2018-07-16 CN CN201821124511.4U patent/CN208810079U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108671876A (en) * | 2018-07-16 | 2018-10-19 | 山东绿色自由基科技研究中心 | A kind of multiphase flow heterogeneous catalytic reaction device |
| CN108671876B (en) * | 2018-07-16 | 2024-02-20 | 山东绿色自由基科技研究中心 | Heterogeneous catalytic reaction device of multiphase flow |
| CN110314619A (en) * | 2019-07-29 | 2019-10-11 | 浙江工业大学 | A kind of hypergravity outer circulation reactor for heterogeneous catalytic reaction |
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