CN109529755B - Multi-suction reinforced mixing Venturi reactor - Google Patents
Multi-suction reinforced mixing Venturi reactor Download PDFInfo
- Publication number
- CN109529755B CN109529755B CN201910104500.2A CN201910104500A CN109529755B CN 109529755 B CN109529755 B CN 109529755B CN 201910104500 A CN201910104500 A CN 201910104500A CN 109529755 B CN109529755 B CN 109529755B
- Authority
- CN
- China
- Prior art keywords
- venturi
- suction
- reactor
- axis
- throat
- 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.)
- Active
Links
- 238000006243 chemical reaction Methods 0.000 claims abstract description 21
- 239000012530 fluid Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 description 10
- 239000003814 drug Substances 0.000 description 4
- 229940079593 drug Drugs 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 238000005728 strengthening Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- -1 hydroxyl free radical Chemical class 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
- B01J19/2415—Tubular reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
- B01F25/31242—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a multi-suction reinforced mixing Venturi reactor, which is characterized in that: comprises a venturi converging section, a venturi throat and a venturi diffusing section which are connected in sequence; and two or more suction pipelines are uniformly arranged on the negative pressure section of the venturi throat along the axis of the multi-suction enhanced mixing venturi reactor. The invention strengthens the mixing mode of the reaction fluid, strengthens the mixing and mass transfer disturbance of the fluid in the venturi tube, reduces the dosage and improves the chemical reaction rate by arranging two or more suction pipelines at the negative pressure section of the throat part of the venturi tube.
Description
Technical Field
The invention relates to a multi-suction reinforced mixing Venturi reactor which strengthens the chemical reaction speed and improves the utilization rate of chemical medicines.
Background
The rate at which chemical reactions occur with a variety of fluids is affected by a variety of factors such as the intensity of mass transfer, the contact area, the form of the reaction, etc. When the gas-liquid reaction is involved, a bubbling reactor, a washing tower or a spraying tower type reactor is often used, and the reactor has the problems of poor gas-liquid reaction effect and low chemical agent utilization rate. The invention is designed and modified into a multi-suction channel based on the traditional Venturi ejector, so that various reaction fluids are mixed in high-speed, negative-pressure and strong-disturbance environments, thereby strengthening mass transfer, increasing contact area and improving reaction rate. Meanwhile, the ejector can trigger cavitation effect under certain working condition to generate hydroxyl free radical, micro-jet and other phenomena, thereby further promoting the occurrence of chemical reaction.
The current gas-liquid two-phase reaction is mainly limited by the contact area, and the size of the reactor needs to be designed to be large in order to improve the contact area. The hydrodynamic cavitation reactor formed by the venturi tube with multiple suction inlets can realize a large liquid-gas ratio on a small-sized reactor, greatly promote gas-liquid mixing, improve the utilization rate of reaction medicines and improve the chemical reaction rate.
Disclosure of Invention
According to the technical problem, a multi-suction enhanced mixing venturi reactor is provided. The invention adopts the following technical means:
a multi-suction enhanced mixing Venturi reactor comprises a Venturi tube convergent section, a Venturi tube throat section and a Venturi tube diffusion section which are connected in sequence;
Two or more suction pipelines are uniformly arranged on the negative pressure section of the throat part of the venturi tube along the axis of the multi-suction enhanced mixing venturi reactor, namely, the two or more suction pipelines are respectively positioned at different positions of the negative pressure section of the throat part of the venturi tube.
Liquid enters through the free end of the converging section of the venturi tube, and a negative pressure section is formed at the throat part of the venturi tube, so that the fluid is sucked in a sectional mode.
The multi-suction enhanced mixing venturi reactor is a mixing suction venturi jet device designed by utilizing a jet negative pressure cavitation principle, can increase the types and modes of sucked fluids, drives the fluids to suck two or more fluids simultaneously and uniformly mix the two or more fluids, and allows different fluids to enter from different suction pipelines, so that the contact area is increased, the mass transfer is enhanced, and the reaction speed and the medicine utilization rate are increased.
The axis of the suction pipeline is perpendicular to the axis of the multi-suction enhanced mixing Venturi reactor;
the orthographic projection of the suction pipeline in a plane perpendicular to the axis of the multi-suction enhanced mixing Venturi reactor is uniformly distributed by taking the axis of the multi-suction enhanced mixing Venturi reactor as an axis.
The suction pipeline is communicated with the venturi throat through an annular cavity protruding outwards from the outer wall of the venturi throat, and an inner ring of the annular cavity is communicated with the venturi throat.
The fluid enters the annular cavity to form annular mixed liquid, so that the utilization rate of medicines is improved, and the dosage is reduced.
One part of the suction pipeline is used for absorbing the reaction fluid, and the other part of the suction pipeline is used for absorbing the fluid to be treated.
Compared with the prior art, the invention has the following beneficial effects:
The invention strengthens the mixing mode of the reaction fluid, strengthens the mixing and mass transfer disturbance of the fluid in the venturi tube, reduces the dosage and improves the chemical reaction rate by arranging two or more suction pipelines at the negative pressure section of the throat part of the venturi tube.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, and it is obvious that the drawings in the following description are some embodiments of the present invention, and other drawings may be obtained according to the drawings without inventive effort to a person skilled in the art.
FIG. 1 is a schematic diagram of a multi-suction enhanced mixing venturi reactor in accordance with an embodiment of the present invention.
Fig. 2 is a cross-sectional view taken along A-A in fig. 1.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present invention more apparent, the technical solutions of the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is apparent that the described embodiments are some embodiments of the present invention, but not all embodiments of the present invention. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
As shown in fig. 1 and 2, a multi-suction enhanced mixing venturi reactor comprises a venturi convergent section 1, a venturi throat 2 and a venturi diffusion section 3 which are connected in sequence;
two suction pipelines 4 are uniformly arranged on the negative pressure section of the venturi throat 2 along the axis of the multi-suction enhanced mixing venturi reactor.
The axis of the suction pipeline 4 is perpendicular to the axis of the multi-suction enhanced mixing Venturi reactor;
The orthographic projection of the suction pipeline 4 in a plane perpendicular to the axis of the multi-suction enhanced mixing venturi reactor is uniformly distributed by taking the axis of the multi-suction enhanced mixing venturi reactor as an axis.
The suction pipeline 4 is communicated with the venturi throat 2 through an annular cavity 5 protruding outwards from the outer wall of the venturi throat 2, and the inner ring of the annular cavity 5 is communicated with the venturi throat 2.
One of the suction lines 4 is for absorbing the reaction fluid and the other suction line 4 is for absorbing the fluid to be treated.
In this embodiment, the suction pipe 4 is symmetrical up and down, when the liquid is ejected from the venturi converging section 1 at a high speed, and the liquid flowing at a high speed passes through the venturi throat 2, vacuum is formed in the venturi throat 2, a large amount of gas or solution is sucked by the suction pipe 4, and the sucked material is vigorously mixed with the liquid at the venturi throat 2 after entering the venturi throat 2, so as to form a gas-liquid mixture, and is discharged from the venturi diffuser 3.
The invention is designed and modified into a multi-suction channel based on the traditional Venturi ejector, so that various reaction fluids are mixed in high-speed, negative-pressure and strong-disturbance environments, thereby strengthening mass transfer, increasing contact area and improving reaction rate. Meanwhile, the multi-absorption reinforced mixing Venturi reactor can cause cavitation effect under a certain working condition to generate hydroxyl free radicals, microjet and other phenomena, so that the occurrence of chemical reaction is further promoted.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present invention, and not for limiting the same; although the invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some or all of the technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit of the invention.
Claims (2)
1. A multi-suction enhanced mixing venturi reactor, characterized in that: comprises a venturi converging section, a venturi throat and a venturi diffusing section which are connected in sequence;
Two or more suction pipelines are uniformly arranged on the negative pressure section of the venturi throat along the axis of the multi-suction enhanced mixing venturi reactor;
the axis of the suction pipeline is perpendicular to the axis of the multi-suction enhanced mixing Venturi reactor;
The suction pipeline is communicated with the venturi throat through an annular cavity protruding outwards from the outer wall of the venturi throat, and the inner ring of the annular cavity is communicated with the venturi throat;
One part of the suction pipeline is used for absorbing the reaction fluid, and the other part of the suction pipeline is used for absorbing the fluid to be treated.
2. The multiple suction enhanced mixing venturi reactor according to claim 1, wherein:
the orthographic projection of the suction pipeline in a plane perpendicular to the axis of the multi-suction enhanced mixing Venturi reactor is uniformly distributed by taking the axis of the multi-suction enhanced mixing Venturi reactor as an axis.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910104500.2A CN109529755B (en) | 2019-02-01 | 2019-02-01 | Multi-suction reinforced mixing Venturi reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910104500.2A CN109529755B (en) | 2019-02-01 | 2019-02-01 | Multi-suction reinforced mixing Venturi reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109529755A CN109529755A (en) | 2019-03-29 |
| CN109529755B true CN109529755B (en) | 2024-07-02 |
Family
ID=65838892
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910104500.2A Active CN109529755B (en) | 2019-02-01 | 2019-02-01 | Multi-suction reinforced mixing Venturi reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109529755B (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109225117B (en) * | 2018-09-17 | 2024-04-16 | 沈阳化工大学 | Impinging stream reaction kettle for preparing ultrafine powder |
| CN112158899A (en) * | 2020-10-15 | 2021-01-01 | 扬州坤健环保科技有限公司 | Liquid-phase CFB reactor device |
| CN112999993B (en) * | 2021-02-08 | 2023-04-07 | 乌兰浩特市圣益商砼有限公司 | Vortex-spraying two-stage strengthening reactor for preparing polycarboxylate superplasticizer and preparation method |
| CN112933866B (en) * | 2021-03-22 | 2022-07-22 | 哈尔滨工程大学 | Gas-liquid two-phase ejector capable of being used for purifying harmful gas |
| CN114192044A (en) * | 2021-12-14 | 2022-03-18 | 高点(深圳)科技有限公司 | Production equipment, mixed precipitate prepared by using production equipment, and method and application of mixed precipitate |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103111212A (en) * | 2013-02-04 | 2013-05-22 | 西安交通大学 | Multi-point introduction structure and flow control mode of venturi mixer |
| CN106975379A (en) * | 2017-04-08 | 2017-07-25 | 深圳欧威奇科技有限公司 | A kind of jet mixer of air inlet biasing |
| CN210022151U (en) * | 2019-02-01 | 2020-02-07 | 大连海事大学 | Multi-suction intensified mixing Venturi reactor |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2001549B (en) * | 1977-07-27 | 1982-01-20 | Zink Co John | Venturi scrubber |
| GB2233915A (en) * | 1989-07-12 | 1991-01-23 | Exxon Research Engineering Co | Contacting solid particles and fluid |
| CN2898007Y (en) * | 2006-03-17 | 2007-05-09 | 成都绿水科技有限公司 | Efficient fluid jetter |
| EP2185274A4 (en) * | 2007-09-07 | 2012-12-05 | Turbulent Energy Inc | Dynamic mixing of fluids |
| CN203061076U (en) * | 2013-02-04 | 2013-07-17 | 西安交通大学 | Multipoint introduction structure of Venturi mixer |
| CN103111213B (en) * | 2013-02-04 | 2015-10-21 | 西安交通大学 | A kind of venturi mixer containing special Inserting Tube |
| CN104275102A (en) * | 2013-07-02 | 2015-01-14 | 德昌电机(深圳)有限公司 | Venturi mixer |
| CN104028132B (en) * | 2014-05-22 | 2016-08-24 | 西安交通大学 | The venturi mixer of symmetrical introducing pipe is contained in a kind of throat |
| CN105498567B (en) * | 2015-12-18 | 2018-02-16 | 中国水利水电科学研究院 | Blowdown diffuser pre-blended method and a kind of strong pre-blended blowdown diffuser |
| CN205903805U (en) * | 2016-06-10 | 2017-01-25 | 西安交通大学 | Rectangle built -in structure's venturi mixer contains in throat |
| CN106540647B (en) * | 2016-11-25 | 2018-10-02 | 中国科学院广州能源研究所 | A kind of hydrate suitable under pipeline flox condition generates intensifying device |
| CN108714376B (en) * | 2018-05-21 | 2020-08-18 | 山东新和成氨基酸有限公司 | Venturi mixer containing porous annular cavity and application of venturi mixer in synthesizing cyanohydrin |
| CN108844673A (en) * | 2018-06-27 | 2018-11-20 | 天津浩天自动化仪表制造有限公司 | A kind of rectification type Venturi tube pressure difference measuring device |
-
2019
- 2019-02-01 CN CN201910104500.2A patent/CN109529755B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103111212A (en) * | 2013-02-04 | 2013-05-22 | 西安交通大学 | Multi-point introduction structure and flow control mode of venturi mixer |
| CN106975379A (en) * | 2017-04-08 | 2017-07-25 | 深圳欧威奇科技有限公司 | A kind of jet mixer of air inlet biasing |
| CN210022151U (en) * | 2019-02-01 | 2020-02-07 | 大连海事大学 | Multi-suction intensified mixing Venturi reactor |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109529755A (en) | 2019-03-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109529755B (en) | Multi-suction reinforced mixing Venturi reactor | |
| US8622715B1 (en) | Twin turbine asymmetrical nozzle and jet pump incorporating such nozzle | |
| CN105909567A (en) | Jet device capable of improving cavitation performance of jet type centrifugal pump | |
| CN210022151U (en) | Multi-suction intensified mixing Venturi reactor | |
| CN108204382A (en) | A kind of compound jet pump being combined based on central jet and annular jet | |
| CN109911967A (en) | A kind of jet flow negative pressure formula ammonia nitrogen blowing-off device | |
| CN109731494A (en) | A kind of generating device and method of micro-nano bubble | |
| TWI841363B (en) | Suction protection structure for micro-bubble device | |
| CN111018100B (en) | Jet aerator and sewage treatment system | |
| JP2013220383A (en) | Gas/liquid mixer | |
| CN216038881U (en) | Negative pressure type efficient air dissolving device | |
| CN201500605U (en) | venturi ejector | |
| CN116474582A (en) | Jet device | |
| CN209668866U (en) | A kind of tube aerator through-hole type attachment device | |
| CN113354071A (en) | Micro-nano jet aerator | |
| CN211706460U (en) | Pipeline mixer | |
| JP3220785U (en) | Fine bubble generator | |
| JP2003056500A (en) | Ejector | |
| CN108050111B (en) | Multi-stage multi-tube high-efficiency jet pump | |
| CN219308568U (en) | Air suction protection structure of micro-bubble device | |
| CN207158927U (en) | A kind of hoisting type aerator | |
| CN219994014U (en) | Jet pump is with jet pipe | |
| CN216500116U (en) | Venturi ejector with special-shaped nozzle and gas turbulence | |
| CN106731938A (en) | A kind of microbubble generating mechanism | |
| CN210410256U (en) | Glass fiber reinforced plastic fluid mixing tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant |