CN108671875A - A kind of multiphase flow reinforcing mass transfer reaction device - Google Patents
A kind of multiphase flow reinforcing mass transfer reaction device Download PDFInfo
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- CN108671875A CN108671875A CN201810780328.8A CN201810780328A CN108671875A CN 108671875 A CN108671875 A CN 108671875A CN 201810780328 A CN201810780328 A CN 201810780328A CN 108671875 A CN108671875 A CN 108671875A
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- 230000003014 reinforcing effect Effects 0.000 title claims abstract description 28
- 238000006276 transfer reaction Methods 0.000 title claims abstract description 19
- 239000012530 fluid Substances 0.000 claims abstract description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 79
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 238000009434 installation Methods 0.000 claims description 8
- 229910052742 iron Inorganic materials 0.000 claims description 8
- 239000010453 quartz Substances 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 230000003068 static effect Effects 0.000 claims description 3
- 230000004044 response Effects 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims 1
- 229920006395 saturated elastomer Polymers 0.000 abstract description 3
- 238000003780 insertion Methods 0.000 abstract description 2
- 230000037431 insertion Effects 0.000 abstract description 2
- 230000009466 transformation Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 11
- 238000000034 method Methods 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 238000005728 strengthening Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 241000233855 Orchidaceae Species 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/245—Stationary reactors without moving elements inside placed in series
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/087—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electric or magnetic energy
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/10—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing sonic or ultrasonic vibrations
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/121—Coherent waves, e.g. laser beams
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/08—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
- B01J19/12—Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
- B01J19/122—Incoherent waves
- B01J19/123—Ultraviolet light
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
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Abstract
The invention discloses a kind of multiphase flows to strengthen mass transfer reaction device, including upper cavity, middle cavity and lower chamber, the upper cavity bottom is equipped with upper cavity oral siphon road and strengthens mass transfer device oral siphon road, reinforcing mass transfer device equipped with eddy flow ram and several connection upper cavities and lower chamber in the lumen body, the lateral surface of the middle cavity is set there are one fluid inlet tube, in the eccentric tangential insertion eddy flow ram cavity of the fluid inlet tube, it is fixedly connected with middle cavity upper plate at the top of the eddy flow ram cavity, top overflow pipe is equipped at the top of the eddy flow ram cavity, the top overflow pipe is fixedly connected with middle cavity upper plate.A kind of multiphase flow of the present invention strengthens mass transfer reaction device, equipped with mass transfer device and upper cavity is strengthened, orderly alternate energy gradient transformation is realized, multiphase flow is solved and strengthens mass transfer and the contradiction for being saturated stability, energy is efficiently utilized simultaneously, brings better prospect of the application.
Description
Technical field
The present invention relates to the mixing of the various fluids such as gas, liquid, solid, dissolving, mass transfer technical applications, especially
It is related to a kind of multiphase flow reinforcing mass transfer reaction device.
Background technology
In the fields such as chemical industry, pharmacy, environmental protection, two or more the material mixing for being not belonging to same phase can be used
Obtain the gas of non-homogeneous mixture progress industrial and agricultural production, especially some slightly solubilities, solid needs largely enter in liquid
Mixed solution is formed, this process is referred to as heterogeneous reinforcing mass transfer, needs to use device and method appropriate, and consume certain
Material and energy consumption；There are certain drawbacks in existing consersion unit, traditional consersion unit energy consumption is too big, actually has when in use
Effect work doing efficiency is inclined, and the raw material that traditional consersion unit is consumed is larger, generates certain waste, is brought to user certain
It influences, for this purpose, it is proposed that a kind of multiphase flow strengthens mass transfer reaction device.
Invention content
The main purpose of the present invention is to provide a kind of multiphase flows to strengthen mass transfer reaction device, can effectively solve background technology
The problems in.
To achieve the above object, the technical solution that the present invention takes is：
A kind of multiphase flow reinforcing mass transfer reaction device, including upper cavity, middle cavity and lower chamber, the upper cavity bottom are equipped with
Upper cavity oral siphon road and reinforcing mass transfer device oral siphon road, the lumen body is interior to be equipped with eddy flow ram and several connection epicoeles
The lateral surface of the reinforcing mass transfer device of body and lower chamber, the middle cavity is set there are one fluid inlet tube, and the fluid inlet tube is inclined
It is anxious to being inserted into eddy flow ram cavity, be fixedly connected with middle cavity upper plate at the top of the eddy flow ram cavity, the rotation
It flows and is equipped with top overflow pipe at the top of ram cavity, the top overflow pipe is fixedly connected with middle cavity upper plate, and passes through pipeline
It is connect with upper cavity oral siphon road, the eddy flow ram cavity top is rounded cylindrical structure, and the fluid inlet tube is eccentric
It is tangentially inserted into the eddy flow ram cavity top, the eddy flow ram cavity lower part is conical structure, and the reinforcing passes
It is fixedly connected with middle cavity upper plate at the top of matter device, the reinforcing mass transfer device bottom is fixedly connected with middle cavity lower plate, the reinforcing
Mass transfer device bottom water outlet is by being equipped with secondary impact reactor water inlet end flanges, the secondary impact in piping connection lower chamber
It is fixedly connected with lower chamber upper plate at the top of reactor water inlet end flanges, secondary impact reactor cavity is equipped in secondary impact reactor
Body, the water inlet end flanges are divided into secondary impact reactor outer flange and secondary impact reactor inner flange two parts,
Middle secondary impact reactor outer flange is connected by pipeline and the reinforcing mass transfer device water outlet in middle cavity lower plate
It connects, secondary impact reactor inner flange is fixedly connected with secondary impact reactor water inlet drainage impact tube water inlet end, outside method
Orchid is connect by pipeline with inner flange, and water inlet drainage impact tube water outlet is directed toward in secondary impact reactor cavity inside
Heart point, each water inlet drainage impact tube water outlet end position correspond to, and the fluid that multiple water inlet drainage impact tubes water outlet is projected is made to realize
High-speed impact, the secondary impact reactor bottom are equipped with water outlet port, and the water outlet port is exported fluid by pipeline anti-
It answers outside device.
Preferably, the eddy flow ram cavity lower part is conical structure, the eddy flow ram cavity upper circular
Tubular structure diameter is 1 with the eddy flow ram cavity lower cone body structure height ratio:5-1:15.
Preferably, permanent magnetic iron and No.1 electromagnetism cable are installed on the outside of the reinforcing mass transfer device cavity.
Preferably, No. two electromagnetism cables are installed on the outside of the eddy flow ram cavity, are installed on the eddy flow ram
There is flange in the bottom.
Preferably, the reinforcing mass transfer device includes but not limited to metallic water pipe, nonmetallic water pipe, internal helicoid water pipe, water
The water pipe of installation electromagnetic coil on the outside of pipe, the water pipe of installation electromagnet on the outside of water pipe, the water pipe of installation permanent magnetic iron on the outside of water pipe,
Static mixer.
Preferably, the reinforcing mass transfer device being equipped with by upper cavity bottom described in piping connection at the top of mass transfer device of strengthening enters
Water lines, the eddy flow ram top pass through the lower chamber oral siphon road at the top of piping connection lower chamber.
Compared with prior art, the present invention has the advantages that：Multiphase flow strengthens mass transfer reaction device, is provided with epicoele
Body enters upper cavity inner space from upper cavity oral siphon road, and high-velocity fluid moment is released, and flow velocity moment reduces, and generates
Second of Hydrodynamic cavitation effect, this time cavitation processes are than first time cavitation generation energy intensity bigger, it is sufficient to will be between fluid molecule
Active force is broken, but due to quickly entering larger low-voltage space, and fluid enters low speed turbulent flow state, insoluble low density gas wink
Between lose constraint, overflowed from heterogeneous fluid, in heterogeneous fluid be saturated fluid stability consolidated, mass transfer effect obtain into
One step enhances, and sufficient utilization is played to raw material, overflows gas and enters simultaneously in reinforcing mass transfer device with heterogeneous fluid, due to strong
Change mass transfer device using flow direction from top to down, fluid density and characteristic difference cause heterogeneous fluid constantly impact flow velocity compared with
Low spilling gas ensure that time of contact and the contact area overflowed between gas and heterogeneous fluid, strengthen in mass transfer device
Gas and liquid form vortex-like flowing and then are sufficiently mixed and contact, and mass transfer effect is further enhanced, and is not easy to fall, entirely
Device is simple, easy to operate, and the effect of mass transfer is more preferable relative to traditional approach.
Description of the drawings
Fig. 1 is the overall structure diagram that multiphase flow of the present invention strengthens mass transfer reaction device；
Fig. 2 is the vertical view of eddy flow ram structure in Fig. 1；
Fig. 3 is another case structure signal of Fig. 1；
Fig. 4 is eddy flow ram main structure diagram in Fig. 3；
Fig. 5 is the overlooking structure diagram of Section A-A in Fig. 4；
Fig. 6 is another situation schematic diagram in Fig. 5；
In figure：1, upper cavity；2, middle cavity；3, lower chamber；101, upper cavity oral siphon road；102, strengthen mass transfer device and enter water
Pipeline；201, eddy flow ram；202, eddy flow ram cavity；203, top overflow pipe；204, fluid inlet tube；205, bottom
Flange；206, strengthen mass transfer device；207, No. two electromagnetism cables；208, No.1 electromagnetism cable；209, permanent magnetic iron；210, heterogeneous
Catalytic reaction equipment；301, secondary impact reactor cavity；302, secondary impact reactor water inlet end flanges；303, secondary impact
Reactor water inlet drainage impact tube；304, water outlet is hit；305, water outlet port.
Specific implementation mode
To make the technical means, the creative features, the aims and the efficiencies achieved by the present invention be easy to understand, with reference to
Specific implementation mode, the present invention is further explained.
As shown in figures 1 to 6, a kind of multiphase flow strengthens mass transfer reaction device, including upper cavity 1, middle cavity 2 and lower chamber 3, on
1 bottom of cavity is equipped with upper cavity oral siphon road 101 and strengthens mass transfer device oral siphon road 102, and eddy flow ram is equipped in middle cavity 2
201 and several connection upper cavities 1 and lower chamber 3 reinforcing mass transfer device 206, the lateral surface of middle cavity 2 set there are one fluid enters
Mouthful pipe 204, fluid inlet tube 204 it is eccentric it is tangential be inserted into 202 in eddy flow ram cavity, 202 top of eddy flow ram cavity with
Middle cavity upper plate is fixedly connected, and 202 top of eddy flow ram cavity is equipped with top overflow pipe 203, top overflow pipe 203 and lumen
Body upper plate is fixedly connected, and is connect with upper cavity oral siphon road 101 by pipeline, and 202 top of eddy flow ram cavity is circle
Tubular structure, eccentric tangential 202 top of insertion eddy flow ram cavity of fluid inlet tube 204,202 lower part of eddy flow ram cavity
For conical structure, strengthens 206 top of mass transfer device and be fixedly connected with middle cavity upper plate, strengthen 206 bottom of mass transfer device and middle cavity
Lower plate is fixedly connected, strengthen 206 bottom water outlet of mass transfer device by be equipped in piping connection lower chamber 3 secondary impact reactor into
Water end (W.E.) flange 302,302 top of secondary impact reactor water inlet end flanges are fixedly connected with lower chamber upper plate, secondary impact reaction
Secondary impact reactor cavity 301 is equipped in device, water inlet end flanges are divided into secondary impact reactor outer flange and secondary impact
Reactor inner flange two parts, wherein secondary impact reactor outer flange are by pipeline and in middle cavity lower plate
Strengthen the 206 water outlet connection of mass transfer device, secondary impact reactor inner flange and secondary impact reactor water inlet drainage impact tube
303 water inlet ends are fixedly connected, and outer flange is connect by pipeline with inner flange, 303 water outlet of the water inlet drainage impact tube
It is directed toward secondary impact reactor cavity inside center point, each water inlet drainage impact tube 303 is discharged end position and corresponds to, and makes multiple water inlets
It drains the fluid that 303 water outlet of impact tube is projected and realizes that high-speed impact, secondary impact reactor bottom are equipped with water outlet port 305,
Water outlet port 305 will be outside fluid output-response device by pipeline；
202 lower part of eddy flow ram cavity is conical structure, and 202 upper circular tubular structure of eddy flow ram cavity is straight
Diameter is 1 with 202 lower cone body structure height ratio of eddy flow ram cavity：5-1：15；Strengthen peace on the outside of 206 cavity of mass transfer device
Equipped with permanent magnetic iron 209 and No.1 electromagnetism cable 208；202 outside of eddy flow ram cavity is equipped with No. two electromagnetism cables 207,
Flange in the bottom 205 is installed on eddy flow ram 201；It includes but not limited to metallic water pipe, nonmetallic water to strengthen mass transfer device 206
The water pipe of installation electromagnetic coil, the water pipe of water pipe outside installation electromagnet, water pipe outside on the outside of pipe, internal helicoid water pipe, water pipe
Water pipe, the static mixer of permanent magnetic iron 209 are installed；Strengthen 206 top of mass transfer device to be equipped with by 1 bottom of piping connection upper cavity
Reinforcing mass transfer device oral siphon road 102, the top of eddy flow ram 201 enters water by the lower chamber 3 at 3 top of piping connection lower chamber
Pipeline.
As shown in figure 3, the outside of Cyclonic reactor cavity 202 is equipped with electromagnetism cable 207；The bottom of Cyclonic reactor 201
Portion's flange 205 includes but not limited to the bottom that side is equipped with heterogeneous reaction catalytic unit 210 in its Cyclonic reactor cavity
Portion's flange, the normally closed flange for not installing other equipment, the heterogeneous reaction catalytic unit 210 include but not limited to that ultrasonic wave shakes
Dynamic device, electromagnet, quartz burner, laser emitter；As shown in Figure 1, the flange of 201 bottom of Cyclonic reactor is normally closed method
Orchid, as shown in figure 3, the flange of 201 bottom of Cyclonic reactor side in Cyclonic reactor cavity is equipped with heterogeneous reaction and urges
Change equipment 210, the heterogeneous reaction catalytic unit includes but not limited to ultrasonic vibrator, electromagnet, quartz burner, swashs
Optical transmitting set.
As shown in figure 3, the flange of 201 bottom of Cyclonic reactor can by its Cyclonic reactor cavity side install
Heterogeneous reaction catalytic unit makes multiphase flow fluid obtain better mass transfer and reaction condition, while also can be described by unloading
Flange in the bottom safeguards the equipment installed thereon, and the fluid in Cyclonic reactor cavity is discharged, is taken out stains
Or other sediments.
It should be noted that the present invention, which is a kind of multiphase flow, strengthens mass transfer reaction device, flow velocity increases during fluid declines
Add, fluid flow rate reaches maximum when reaching eddy flow ram 202 flange in the bottom 205 of cavity, and changes fluid under pressure
The direction of motion, high speed impact is done in vacuum area to fluid upwards in an axial direction, and fluid flow rate moment from height to zero, generates first time waterpower
Cavitation effect, the Hydrodynamic cavitation intensity generated during this is not enough to cause its original property of molecular changes, but is enough to break stream
Body molecular cluster enhances multiphase flow heterogeneous mass transfer degree, and fluid passes through top overflow pipe 203 and its pipeline of connection, from
Upper cavity oral siphon road 101 enters upper cavity 1 inner space, and high-velocity fluid moment is released, and flow velocity moment reduces, and generates the
Secondary waterpower cavitation effect, this time cavitation processes are than first time cavitation generation energy intensity bigger, it is sufficient to will make between fluid molecule
Firmly break, but due to quickly entering larger low-voltage space, fluid enters low speed turbulent flow state, insoluble low density gas moment
Constraint is lost, is overflowed from heterogeneous fluid, the stability that fluid is saturated in heterogeneous fluid is consolidated, and mass transfer effect is obtained into one
Step enhancing, fluid do irregular movement in upper cavity 1, ensure that the time of contact overflowed between gas and heterogeneous fluid and connect
Contacting surface is accumulated, and fluid is formed in upper cavity 1 to be detained, and causes pressure in upper cavity 1 to increase, fluid is upper by being mounted under high pressure
The pipeline of the reinforcing mass transfer device oral siphon road 102 of 1 bottom of cavity and its connection, which enters, strengthens mass transfer device 206, overflow gas with it is more
Phase fluid enters simultaneously to be strengthened in mass transfer device 206, and due to strengthening mass transfer device 206 using flow direction from top to down, fluid is close
The degree heterogeneous fluid that causes different with characteristic constantly impacts the lower spilling gas of flow velocity, ensure that and overflows gas and heterogeneous fluid
Between time of contact and contact area, form vortex-like flowing strengthening gas and liquid in mass transfer device 206 and then be sufficiently mixed
And contact, mass transfer effect are further enhanced, fluid is by strengthening mass transfer device 206 and entering secondary impact reaction by pipeline
Device water inlet pipe, fluid intake into secondary impact reactor by secondary impact reactor water inlet end flanges 302 and drain impact tube
303, gradually increase with the caliber flow velocity that becomes smaller, and finally form high pressure in secondary impact reactor drainage impact tube 303 of intaking
High speed impact stream, and be released, third time Hydrodynamic cavitation effect is formed, is at the same time intake from each secondary impact reactor
The spouting impingement flow of impact tube 303 is drained, moment strengthens the heterogeneous mass transfer effect of multiphase flow.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (7)
1. a kind of multiphase flow strengthens mass transfer reaction device, including upper cavity (1), middle cavity (2) and lower chamber (3), it is characterised in that：
Upper cavity (1) bottom is equipped with upper cavity oral siphon road (101) and strengthens mass transfer device oral siphon road (102), the middle cavity
(2) the reinforcing mass transfer device (206) equipped with eddy flow ram (201) and several connection upper cavity (1) and lower chamber (3), institute in
The lateral surface for stating middle cavity (2) is set there are one fluid inlet tube (204), and eccentric tangential be inserted into of the fluid inlet tube (204) is revolved
It flows in ram cavity (202), is fixedly connected with middle cavity upper plate at the top of the eddy flow ram cavity (202), the eddy flow
Top overflow pipe (203) is equipped at the top of ram cavity (202), the top overflow pipe (203) is fixed with middle cavity upper plate to be connected
It connects, and is connect with upper cavity oral siphon road (101) by pipeline, eddy flow ram cavity (202) top is rounded cylindrical
Structure, the fluid inlet tube (204) is eccentric to be tangentially inserted into eddy flow ram cavity (202) top, and the eddy flow is hit
Device cavity (202) lower part is conical structure, is fixedly connected with middle cavity upper plate at the top of the reinforcing mass transfer device (206), described
Strengthen mass transfer device (206) bottom to be fixedly connected with middle cavity lower plate, reinforcing mass transfer device (206) bottom water outlet passes through pipeline
It connects and is equipped with secondary impact reactor water inlet end flanges (302) in lower chamber (3), the secondary impact reactor water inlet end flanges
(302) top is fixedly connected with lower chamber upper plate, and secondary impact reactor cavity (301), institute are equipped in secondary impact reactor
It states into water end flanges and is divided into secondary impact reactor outer flange and secondary impact reactor inner flange two parts, wherein secondary
Knock-on reaction device outer flange is connected by pipeline and reinforcing mass transfer device (206) water outlet in middle cavity lower plate
It connects, secondary impact reactor inner flange is fixedly connected with secondary impact reactor water inlet drainage impact tube (303) water inlet end, outside
Side flange is connect by pipeline with inner flange, and secondary impact reactor is directed toward in water inlet drainage impact tube (303) water outlet
Inside cavity central point, each water inlet drainage impact tube (303) are discharged end position and correspond to, and make multiple water inlet drainage impact tubes (303)
The fluid that water outlet is projected realizes that high-speed impact, the secondary impact reactor bottom are equipped with water outlet port (305), the water outlet
It port (305) will be outside fluid output-response device by pipeline.
2. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：The eddy flow ram chamber
Body (202) lower part is conical structure, eddy flow ram cavity (202) the upper circular tubular structure diameter and the eddy flow
Ram cavity (202) lower cone body structure height ratio is 1:5-1:15.
3. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：The Cyclonic reactor chamber
Body (202) includes but not limited to that outside is equipped with the Cyclonic reactor cavity of No.1 electromagnetism cable (207), outside is equipped with electricity
The Cyclonic reactor cavity of magnet, outside are equipped with the Cyclonic reactor cavity of permanent magnetic iron, any equipment is not installed in outside
Cyclonic reactor cavity.
4. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：In the middle cavity (2)
The enhanced reactor (206) of portion's setting includes but not limited to that the reinforcing reaction of No. two electromagnetism cables (208) is equipped on the outside of cavity
Device, the enhanced reactor that permanent magnetic iron (209) are equipped on the outside of cavity, the reinforcing reaction for not installing any equipment on the outside of cavity
Device.
5. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：The eddy flow ram chamber
Body (202) bottom is equipped with flange in the bottom (205), and the Cyclonic reactor flange in the bottom (205) includes but not limited to be equipped with
The flange of ultrasonic vibrator, the flange for being equipped with quartz burner, is equipped with laser emitter at the flange for being equipped with electromagnet
Flange, the normally closed flange of any other equipment is not installed.
6. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：The reinforcing mass transfer device
(206) include but not limited to metallic water pipe, nonmetallic water pipe, internal helicoid water pipe, the water pipe of installation electromagnetic coil on the outside of water pipe,
Water pipe, the static mixer of the water pipe of installation electromagnet, water pipe outside installation permanent magnetic iron (209) on the outside of water pipe.
7. a kind of multiphase flow according to claim 1 strengthens mass transfer reaction device, it is characterised in that：The reinforcing mass transfer device
(206) the reinforcing mass transfer device oral siphon road (102) that top is equipped with by upper cavity described in piping connection (1) bottom, the eddy flow
Pass through lower chamber (3) oral siphon road at the top of piping connection lower chamber (3) at the top of ram (201).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810780328.8A CN108671875B (en) | 2018-07-16 | 2018-07-16 | Multiphase flow intensified mass transfer reactor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810780328.8A CN108671875B (en) | 2018-07-16 | 2018-07-16 | Multiphase flow intensified mass transfer reactor |
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| CN108671875A true CN108671875A (en) | 2018-10-19 |
| CN108671875B CN108671875B (en) | 2024-03-26 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110833805A (en) * | 2019-11-20 | 2020-02-25 | 宁波诺丁汉大学 | Ultrasonic-assisted reinforced turbulent cyclone reactor for preparing fine particles |
| CN110921770A (en) * | 2019-12-23 | 2020-03-27 | 北京工业大学 | Self-oscillation cavitation impinging stream reactor |
| CN111977869A (en) * | 2020-08-19 | 2020-11-24 | 王天琛 | System for treating sewage by utilizing ultrasonic multiphase flow rotational flow cavitation impinging stream technology |
| CN112237896A (en) * | 2020-09-21 | 2021-01-19 | 中国石油大学(华东) | Novel mixing-enhanced reactor for alkylation of ionic liquid |
| CN113413846A (en) * | 2021-06-29 | 2021-09-21 | 宁波诺丁汉大学 | Ultrasonic-enhanced reverse vortex flow impinging stream reactor |
| CN114394656A (en) * | 2022-01-18 | 2022-04-26 | 中国矿业大学 | Shale atmospheric pressure splits and returns flowing back flocculation treatment reactor |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110833805A (en) * | 2019-11-20 | 2020-02-25 | 宁波诺丁汉大学 | Ultrasonic-assisted reinforced turbulent cyclone reactor for preparing fine particles |
| CN110921770A (en) * | 2019-12-23 | 2020-03-27 | 北京工业大学 | Self-oscillation cavitation impinging stream reactor |
| CN111977869A (en) * | 2020-08-19 | 2020-11-24 | 王天琛 | System for treating sewage by utilizing ultrasonic multiphase flow rotational flow cavitation impinging stream technology |
| CN111977869B (en) * | 2020-08-19 | 2022-11-22 | 王天琛 | System for treating sewage by utilizing ultrasonic multiphase flow rotational flow cavitation impinging stream technology |
| CN112237896A (en) * | 2020-09-21 | 2021-01-19 | 中国石油大学(华东) | Novel mixing-enhanced reactor for alkylation of ionic liquid |
| CN112237896B (en) * | 2020-09-21 | 2022-04-12 | 中国石油大学(华东) | Novel mixing-enhanced reactor for alkylation of ionic liquid |
| CN113413846A (en) * | 2021-06-29 | 2021-09-21 | 宁波诺丁汉大学 | Ultrasonic-enhanced reverse vortex flow impinging stream reactor |
| CN114394656A (en) * | 2022-01-18 | 2022-04-26 | 中国矿业大学 | Shale atmospheric pressure splits and returns flowing back flocculation treatment reactor |
| CN114394656B (en) * | 2022-01-18 | 2023-11-17 | 中国矿业大学 | Shale gas fracturing flow-back fluid flocculation treatment reactor |
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