CN114522648A - Mixing reactor for automatically and rapidly mixing solution and construction method - Google Patents
Mixing reactor for automatically and rapidly mixing solution and construction method Download PDFInfo
- Publication number
- CN114522648A CN114522648A CN202210368841.2A CN202210368841A CN114522648A CN 114522648 A CN114522648 A CN 114522648A CN 202210368841 A CN202210368841 A CN 202210368841A CN 114522648 A CN114522648 A CN 114522648A
- Authority
- CN
- China
- Prior art keywords
- liquid
- mixing
- reaction
- weir
- box body
- 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.)
- Pending
Links
- 238000002156 mixing Methods 0.000 title claims abstract description 85
- 238000010276 construction Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 124
- 238000006243 chemical reaction Methods 0.000 claims abstract description 62
- 239000000243 solution Substances 0.000 claims abstract description 26
- 238000000034 method Methods 0.000 claims abstract description 16
- 239000011259 mixed solution Substances 0.000 claims abstract description 3
- 238000000576 coating method Methods 0.000 claims description 11
- 239000011248 coating agent Substances 0.000 claims description 10
- 239000012495 reaction gas Substances 0.000 claims description 10
- 239000011152 fibreglass Substances 0.000 claims description 9
- 230000035484 reaction time Effects 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims description 4
- 238000012360 testing method Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 abstract description 12
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000012824 chemical production Methods 0.000 abstract description 2
- 238000013461 design Methods 0.000 abstract description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- 230000007306 turnover Effects 0.000 description 9
- 238000005660 chlorination reaction Methods 0.000 description 7
- 239000002699 waste material Substances 0.000 description 7
- 239000011780 sodium chloride Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 229910003074 TiCl4 Inorganic materials 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
Images
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
- B01J14/00—Chemical processes in general for reacting liquids with liquids; Apparatus specially adapted therefor
-
- 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
- B01J19/006—Baffles
-
- 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
-
- 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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
-
- 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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/008—Feed or outlet control devices
-
- 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
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/02—Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents
-
- 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
- B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
- B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
The invention discloses a mixing reactor for automatically and rapidly mixing a solution and a construction method, and belongs to the technical field of design and manufacture of salt chemical production process equipment. Provides a mixing reactor capable of rapidly and automatically mixing various solutions uniformly and a construction method thereof. The mixing reactor comprises a reaction tank, a weir-turning type mixing mechanism and a liquid conveying piping system, wherein the weir-turning type mixing mechanism is arranged in the reaction tank, a solution to be mixed is input into the weir-turning type mixing mechanism through the liquid conveying piping system to be mixed and turned out to the reaction tank for reaction, and a mixed solution after the reaction is finished is output out of the reaction tank through the liquid conveying piping system. The construction method comprises the steps of inputting different types of liquid into the open sleeve through the liquid input pipe, mixing the liquid in the open sleeve in a weir turning mode, entering the box body to react in the weir turning process, and finally outputting the liquid to the reaction tank through the liquid output pipe to complete the mixing and reaction of various liquids in the mixing reactor.
Description
Technical Field
The invention relates to a mixing reactor, in particular to a mixing reactor for automatically and quickly mixing a solution, and belongs to the technical field of design and manufacture of salt chemical production process equipment. The invention also relates to a construction method for mixed liquid reaction by adopting the mixed reactor.
Background
The main raw material for producing the titanium sponge and the titanium dioxide in China is TiCl4, and the TiCl4 mainly adopts a molten salt chlorination process and a boiling chlorination process. Aiming at the condition that W (Ca + Mg) in the titanium slag raw material is more than 5 percent, the most suitable process at present is a molten salt chlorination process. The generation of a large amount of Cl-containing waste residues (waste salts for short) by the chlorination of the molten salt is commonly adopted at present. Through research and development, the developed new waste salt treatment process needs to effectively mix various waste liquids generated in production, so that the multiple waste liquids are quickly and uniformly mixed in a reactor, elements such as Fe, Mn, Ca, Mg and the like are gradually separated, and finally NaCl is recycled and returned to a molten salt chlorination furnace for use.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: provides a mixing reactor capable of rapidly and automatically mixing various solutions uniformly and a construction method for adopting the mixing reactor to mix liquid for reaction.
The technical scheme adopted for solving the technical problems is as follows: the utility model provides a mixed reactor for automatic quick mixing of solution, mixed reactor include the reaction tank, turn over weir formula mixing mechanism and liquid delivery piping, turn over weir formula mixing mechanism and arrange the reaction tank in, the solution that needs to mix passes through liquid delivery piping input turn over weir formula mixing mechanism in mix and turn out to the reaction tank in react, the mixed liquid after the reaction is accomplished passes through liquid delivery piping output the reaction tank.
Furthermore, the reaction tank is composed of a closable box body, the weir-turning type mixing mechanism is arranged in the box body, a liquid input pipe of the liquid conveying pipe system extends into the box body from the middle upper part of the box body, and a liquid output pipe of the liquid conveying pipe system is communicated with the box body from the lower part of the box body.
The preferable mode of the scheme is that the inner surface of the box body is provided with a lining glass fiber reinforced plastic anticorrosive layer, the top of the box body is provided with a reaction gas outlet and a liquid input pipe arrangement hole, and the reaction gas outlet and the liquid input pipe arrangement hole are uniformly provided with a detachable sealing cover.
Further, the lining glass fiber reinforced plastic anticorrosive coating is a 9-cloth 10-coating structural glass fiber reinforced plastic anticorrosive coating arranged on the inner surface of the box body.
The preferred mode of the above scheme is that the weir-turning mixing mechanism is an open casing arranged in the box body, the distance from the tail end of each liquid input pipe for conveying different liquids to the bottom of the open casing is less than the pipe diameter of the liquid input pipe, and the distance from the open upper opening of the open casing to the bottom of the box body is not less than two thirds of the height of the box body.
Furthermore, control valves are arranged on a liquid input pipe and a liquid output pipe of the liquid conveying pipe system, the top of the box body is detachably sealed through a cover plate, and a reaction gas outlet and liquid input pipe arrangement holes are uniformly arranged on the cover plate.
The construction method comprises the steps of inputting different types of liquid into the open sleeve through the liquid input pipe, mixing the liquid in the open sleeve in a weir turning mode, entering the box body to react in the weir turning process, and finally outputting the liquid to the reaction tank through the liquid output pipe to complete the mixing and reaction of the various types of liquid in the mixing reactor.
Further, the stay time of the mixed liquid in the box body is longer than or equal to the reaction time of various liquids.
In a preferred embodiment of the above-described embodiment, the reaction time is obtained by an external reaction test.
Furthermore, the staying time of various liquids in the box body is controlled by the control valves arranged on the liquid output pipe and the liquid input pipe so as to control the amount of the input and/or output liquid.
The invention has the beneficial effects that: the technical scheme that this application provided is through setting up one set including the reaction tank, turning over the mixed reactor of weir formula mixing mechanism and liquid delivery piping, and will turn over weir formula mixing mechanism and arrange the reaction tank in, then pass through the solution that needs to mix liquid delivery piping input turn over weir formula mixing mechanism in mix and turn over to the reaction tank in react, the mixed liquid after the reaction is accomplished passes through liquid delivery piping output the reaction tank. Because the technical scheme that this application provided adopts each liquid that liquid conveying piping system will need to mix to import simultaneously turns over weir formula mixing mechanism to realize the mixing of stirring completion various liquid between the different liquid at this turns over weir formula mixing mechanism through the form that turns over the weir formula, changed prior art and need can't effectively mix or need set up the current situation that large-scale mixing tank adds agitating unit and just can mix a large amount of different liquid, reached quick automatic liquid to multiple needs reaction and mixed the purpose. The method creates conditions for separating elements such as Fe, Mn, Ca, Mg and the like from the waste salt through reaction treatment and finally realizing the recovery of NaCl and returning the NaCl to the fused salt chlorination furnace for use.
Drawings
FIG. 1 is a simplified structural diagram of a mixing reactor for automatic and rapid mixing of a solution according to the present invention.
Labeled as: the device comprises a reaction tank 1, a weir-turning type mixing mechanism 2, a liquid conveying pipe system 3, a liquid input pipe 4, a liquid output pipe 5, a reaction gas outlet 6, a liquid input pipe arrangement hole 7, a control valve 8 and a cover plate 9.
Detailed Description
Fig. 1 shows a mixing reactor capable of rapidly and automatically mixing a plurality of solutions according to the present invention. The mixing reactor comprises a reaction tank 1, a weir-turning type mixing mechanism 2 and a liquid conveying piping system 3, wherein the weir-turning type mixing mechanism 2 is arranged in the reaction tank 1, a solution to be mixed is input into the weir-turning type mixing mechanism 2 through the liquid conveying piping system 3 to be mixed and turned out to the reaction tank 1 for reaction, and a mixed solution after the reaction is finished is output out of the reaction tank 1 through the liquid conveying piping system 3. The construction method comprises the steps of inputting different types of liquid into the open sleeve through the liquid input pipe 4, mixing the liquid in the open sleeve in a weir turning mode, entering the box body in the weir turning process to react, and finally outputting the liquid out of the reaction tank through the liquid output pipe 5 to complete mixing and reaction of various liquids in the mixing reactor. The technical scheme that this application provided is through setting up one set including the reaction tank, turning over the mixed reactor of weir formula mixing mechanism and liquid delivery piping, and will turn over weir formula mixing mechanism and arrange the reaction tank in, then pass through the solution that needs to mix liquid delivery piping input turn over weir formula mixing mechanism in mix and turn over to the reaction tank in react, the mixed liquid after the reaction is accomplished passes through liquid delivery piping output the reaction tank. Because the technical scheme that this application provided adopts each liquid that liquid conveying piping system will need to mix to import simultaneously turns over weir formula mixing mechanism to realize the mixing of stirring completion various liquid between the different liquid at this turns over weir formula mixing mechanism through the form that turns over the weir formula, changed prior art and need can't effectively mix or need set up the current situation that large-scale mixing tank adds agitating unit and just can mix a large amount of different liquid, reached quick automatic liquid to multiple needs reaction and mixed the purpose. The method creates conditions for separating elements such as Fe, Mn, Ca, Mg and the like from the waste salt through reaction treatment and finally realizing the recovery of NaCl and returning the NaCl to the fused salt chlorination furnace for use.
In the above embodiment, in order to simplify the structure of each part of the present application, facilitate the manufacture, assembly and use, and improve the mixing effect, the reaction tank 1 of the present application is composed of a closable tank body, the weir-turning mixing mechanism 2 is disposed in the tank body, the liquid input pipe 4 of the liquid conveying piping system 3 extends into the tank body from the middle upper part of the tank body, and the liquid output pipe 5 of the liquid conveying piping system is communicated with the tank body from the lower part of the tank body. The weir-turning type mixing mechanism 2 is an open casing arranged in the box body, the distance from the tail end of each liquid input pipe 4 for conveying different liquids to the bottom of the open casing is smaller than the pipe diameter of the liquid input pipe 4, and the distance between the open upper opening of the open casing and the bottom of the box body is not smaller than two thirds of the height of the box body. And the liquid input pipe 4 and the liquid output pipe 5 of the liquid conveying pipe system 3 are both provided with a control valve 8, the top of the box body is detachably sealed by a cover plate 9, and the reaction gas outlet 6 and the liquid input pipe arrangement hole 7 are both arranged on the cover plate 9. Correspondingly, all have the characteristics of corrosivity in order to adapt to this application various liquid that need mix, in order to prolong the life of this application mixing reactor, be provided with inside lining glass steel anticorrosive coating on the internal surface of box, be provided with reaction gas discharge port 6 and liquid input pipe arrangement hole 7 at the top of box reaction gas discharge port 6 with liquid input pipe arrangement hole 7 on the equipartition have placed detachable sealed lid. At the moment, the lining glass fiber reinforced plastic anticorrosive coating is a 9-cloth 10-coating structural glass fiber reinforced plastic anticorrosive coating arranged on the inner surface of the box body.
Further, in order to improve the reaction effect, the stay time of the mixed liquid in the box body is longer than or equal to the reaction time of various liquids. In this case, the reaction time is determined by an external reaction test. The staying time of various liquids in the box body is adopted to control the amount of the liquid input and/or output by control valves arranged on the liquid output pipe 5 and the liquid input pipe 4.
DETAILED DESCRIPTION OF EMBODIMENT (S) OF INVENTION
The main content of the invention is as follows:
1. the invention is suitable for acidic solution, and is anticorrosive by lining glass fiber reinforced plastic in a reactor, and adopting 9 cloth and 10 coatings;
2. the invention arranges a sleeve in a reaction tank, and inserts a plurality of solution feed pipes into the bottom of the sleeve to ensure that the solution turns upwards and overflows the sleeve, and forms a 'turning weir' to ensure that the solution is fully mixed, then flows downwards in the reaction tank and is discharged out of a reactor at the bottom of a container;
3. the external reaction tank calculates the retention time of the solution in the reactor according to the reaction time, thereby effectively solving the chemical reaction effect;
4. setting other reaction discharge holes at the top of the molten pool, and effectively treating the gas;
5. a flow control system is arranged on the feeding system, and the proportioning problem is solved through a regulating valve.
Example one
According to the invention, through researching material properties and process conditions, a reactor for quickly and automatically mixing various solutions is developed, and the purposes of quickly mixing and effectively controlling reaction rate are achieved.
The first step is as follows: selecting materials according to working conditions;
the second step is that: according to the process requirements, calculating the mixing time of the solution in the reactor, designing the length of a sleeve and the like;
the third step: the reactor specifications are designed according to the process requirements, the length of the sleeve and the reaction time in the reactor.
Claims (10)
1. A mixing reactor that is used for automatic quick mixing of solution which characterized in that: the mixing reactor comprises a reaction tank (1), a weir-turning type mixing mechanism (2) and a liquid conveying piping system (3), wherein the weir-turning type mixing mechanism (2) is arranged in the reaction tank (1), a solution needing to be mixed is input into the weir-turning type mixing mechanism (2) through the liquid conveying piping system (3) to be mixed and turned out to the reaction tank (1) for reaction, and a mixed solution after the reaction is finished is output from the reaction tank (1) through the liquid conveying piping system (3).
2. The mixing reactor for automatic and rapid blending of solutions according to claim 1, characterized in that: the reaction tank (1) is composed of a closable tank body, the weir-turning type mixing mechanism (2) is arranged in the tank body, a liquid input pipe (4) of the liquid conveying pipe system (3) extends into the tank body from the middle upper part of the tank body, and a liquid output pipe (5) of the liquid conveying pipe system is communicated with the tank body from the lower part of the tank body.
3. The mixing reactor for automatic and rapid blending of solutions according to claim 2, characterized in that: the inner surface of the box body is provided with a lining glass fiber reinforced plastic anticorrosive layer, the top of the box body is provided with a reaction gas outlet (6) and a liquid input pipe arrangement hole (7), and detachable sealing covers are uniformly distributed on the reaction gas outlet (6) and the liquid input pipe arrangement hole (7).
4. The mixing reactor for automatic and rapid blending of solutions according to claim 3, characterized in that: the lining glass fiber reinforced plastic anticorrosive coating is a 9-cloth 10-coating structural glass fiber reinforced plastic anticorrosive coating arranged on the inner surface of the box body.
5. The mixing reactor for automatic rapid blending of solutions according to claim 1, 2, 3 or 4, characterized in that: the weir-turning type mixing mechanism (2) is an open sleeve arranged in the box body, the distance from the tail end of each liquid input pipe (4) for conveying different liquids to the bottom of the open sleeve is smaller than the pipe diameter of the liquid input pipe (4), and the distance between the open upper opening of the open sleeve and the bottom of the box body is not smaller than two thirds of the height of the box body.
6. The mixing reactor for automatic and rapid blending of solutions according to claim 5, characterized in that: control valves (8) are arranged on a liquid input pipe (4) and a liquid output pipe (5) of the liquid conveying pipe system (3), the top of the box body is detachably sealed through a cover plate (9), and reaction gas discharge ports (6) and liquid input pipe arrangement holes (7) are uniformly arranged on the cover plate (9).
7. The construction method for reacting the mixed liquid in the mixing reactor of claim 6, wherein: the construction method comprises the steps of inputting different types of liquid into the open sleeve through the liquid input pipe (4), mixing the liquid in the open sleeve in a weir turning mode, entering the box body to react in the weir turning process, and finally outputting the liquid to the reaction tank through the liquid output pipe (5) to complete the mixing and reaction of various liquids in the mixing reactor.
8. The construction method according to claim 7, wherein: the stay time of the mixed liquid in the box body is longer than or equal to the reaction time of various liquids.
9. The construction method according to claim 8, wherein: the reaction duration is determined by external reaction tests.
10. The construction method according to claim 9, wherein: the staying time of various liquids in the box body is controlled by the control valves arranged on the liquid output pipe (5) and the liquid input pipe (4) to control the amount of the input and/or output liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210368841.2A CN114522648A (en) | 2022-04-08 | 2022-04-08 | Mixing reactor for automatically and rapidly mixing solution and construction method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210368841.2A CN114522648A (en) | 2022-04-08 | 2022-04-08 | Mixing reactor for automatically and rapidly mixing solution and construction method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN114522648A true CN114522648A (en) | 2022-05-24 |
Family
ID=81627898
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210368841.2A Pending CN114522648A (en) | 2022-04-08 | 2022-04-08 | Mixing reactor for automatically and rapidly mixing solution and construction method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114522648A (en) |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1198448A (en) * | 1966-11-03 | 1970-07-15 | Wool Ind Res Association | Methods and Apparatus for Mixing and Dispensing Solutions |
| CN1170628A (en) * | 1996-02-27 | 1998-01-21 | 普拉塞尔技术有限公司 | Improved reactor system |
| CN1195897A (en) * | 1997-02-03 | 1998-10-14 | 松下电器产业株式会社 | Manufacturing method of active materials for positive electrode in alkaline storage batteries |
| CN101274249A (en) * | 2007-03-28 | 2008-10-01 | 中国石油大学(北京) | Novel liquid-liquid heterophase reactor |
| CN103611454A (en) * | 2013-12-05 | 2014-03-05 | 北京国科安达科技发展有限公司 | Pneumatic stirring device and stirring method thereof |
| CN203572771U (en) * | 2013-11-25 | 2014-04-30 | 武汉钢铁(集团)公司 | Atomic absorption spectrometer mixing sample introduction device |
| KR20160055410A (en) * | 2014-11-10 | 2016-05-18 | 주식회사 포스코 | Apparatus for mixing solution |
| CN107727559A (en) * | 2017-09-12 | 2018-02-23 | 合肥通用机械研究院 | A kind of corrosion testing apparatus and the method using the device |
| CN108273452A (en) * | 2018-01-30 | 2018-07-13 | 浙江工业大学 | A kind of grease epoxidation reactor |
| CN208906035U (en) * | 2018-08-23 | 2019-05-28 | 江西国化实业有限公司 | A kind of medication chemistry apparatus for combining liquids |
| CN114259972A (en) * | 2022-01-07 | 2022-04-01 | 四川宝生药业发展有限公司 | Liquid-liquid two-phase mixing device of chlorine dioxide enhanced reactor |
-
2022
- 2022-04-08 CN CN202210368841.2A patent/CN114522648A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1198448A (en) * | 1966-11-03 | 1970-07-15 | Wool Ind Res Association | Methods and Apparatus for Mixing and Dispensing Solutions |
| CN1170628A (en) * | 1996-02-27 | 1998-01-21 | 普拉塞尔技术有限公司 | Improved reactor system |
| CN1195897A (en) * | 1997-02-03 | 1998-10-14 | 松下电器产业株式会社 | Manufacturing method of active materials for positive electrode in alkaline storage batteries |
| CN101274249A (en) * | 2007-03-28 | 2008-10-01 | 中国石油大学(北京) | Novel liquid-liquid heterophase reactor |
| CN203572771U (en) * | 2013-11-25 | 2014-04-30 | 武汉钢铁(集团)公司 | Atomic absorption spectrometer mixing sample introduction device |
| CN103611454A (en) * | 2013-12-05 | 2014-03-05 | 北京国科安达科技发展有限公司 | Pneumatic stirring device and stirring method thereof |
| KR20160055410A (en) * | 2014-11-10 | 2016-05-18 | 주식회사 포스코 | Apparatus for mixing solution |
| CN107727559A (en) * | 2017-09-12 | 2018-02-23 | 合肥通用机械研究院 | A kind of corrosion testing apparatus and the method using the device |
| CN108273452A (en) * | 2018-01-30 | 2018-07-13 | 浙江工业大学 | A kind of grease epoxidation reactor |
| CN208906035U (en) * | 2018-08-23 | 2019-05-28 | 江西国化实业有限公司 | A kind of medication chemistry apparatus for combining liquids |
| CN114259972A (en) * | 2022-01-07 | 2022-04-01 | 四川宝生药业发展有限公司 | Liquid-liquid two-phase mixing device of chlorine dioxide enhanced reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102719673B (en) | Reactor for continuously leaching valuable metal of electroplating sludge and leaching method thereof | |
| CN209537164U (en) | The mercury that mercury-containing waste water is handled in a kind of Production of PVC makes the transition separator | |
| CN206793616U (en) | A kind of solid-liquid reaction kettle | |
| CN114522648A (en) | Mixing reactor for automatically and rapidly mixing solution and construction method | |
| CN206103869U (en) | Full -automatic integrated liquid fertilizer production facility | |
| CN106219703B (en) | A kind of device and method of carbide slag and PAM combination processing black water | |
| CN110743476B (en) | Multifunctional calcium hydroxide preparation tank and preparation method | |
| CN206046019U (en) | A kind of cement water reducing agent reactor | |
| CN104152684B (en) | A kind of cylinder Horizontal normal pressure strengthening leaching tanks | |
| CN107673311A (en) | A kind of continuous device and method for preparing the high-concentrated sodium hypochlorite aqueous solution | |
| CN206886813U (en) | A kind of integrated form waste water softens clarifier | |
| CN209428370U (en) | Sewage treatment production line teaching practice device | |
| CN208617546U (en) | The chemicals dosing plant of sewage treatment | |
| CN112251602A (en) | Method and device for preparing mixed rare earth chloride by continuous extraction and transformation of rare earth sulfate | |
| CN207175557U (en) | A kind of phosphorus reclaims crystallization reactor | |
| CN207227156U (en) | A kind of chemistry removes hard reaction system | |
| CN106431940B (en) | Reduction with sodium bisulfide produces the device and method of aminoanisole | |
| CN205659677U (en) | Novel integral type reation kettle of production plating bath product | |
| CN207619019U (en) | A kind of continuous device for preparing high-concentrated sodium hypochlorite aqueous solution | |
| CN217796122U (en) | Controllable continuous gas production combination device | |
| CN207016538U (en) | A kind of sulfur-bearing acid copper waste water processing unit | |
| CN214115662U (en) | Device for preparing mixed rare earth chloride by continuous extraction and transformation of rare earth sulfate | |
| CN212236819U (en) | Chemical industry compounding device convenient to divide step classification to mix | |
| CN209081602U (en) | A kind of sewage treatment mechanism | |
| CN208465839U (en) | Activator filling system |
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 |