CN2502777Y - Jet mixer - Google Patents
Jet mixer Download PDFInfo
- Publication number
- CN2502777Y CN2502777Y CN 01249739 CN01249739U CN2502777Y CN 2502777 Y CN2502777 Y CN 2502777Y CN 01249739 CN01249739 CN 01249739 CN 01249739 U CN01249739 U CN 01249739U CN 2502777 Y CN2502777 Y CN 2502777Y
- Authority
- CN
- China
- Prior art keywords
- liquid
- nozzle
- disk distributor
- distributor
- jet mixer
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a jet mixer fully mixing the feed liquid in a liquid-liquid reaction vessel, which comprises a disc distributor (1) and a Venturi nozzle (2). A liquid circulation tube inlet (3) and distribution heads (4), (5) are provided on the disc distributor (1); the shells of the distribution heads (4), (5) and the disc distributor (1) are distributed evenly on the periphery of the disc distributor (1) in right and bevel; the distribution heads are connected with the Venturi nozzle (2) through flanges; the Venturi nozzle (2) comprises a nozzle (6), a suction chamber (7), a mixing tube (8) and a diffusion tube (9). The bottom of the suction chamber (7) is opened with a discharge clearly port (10); the disc distributor (1) is connected with a circulation pump outlet pipe (12) installed in a reaction vessel (11) through the liquid circulation tube inlet (3). The utility model has the advantages of simple structure, convenient installation, good mixing effect and high production yield.
Description
Technical field
The utility model relates to the well-mixed jet mixer of feed liquid in a kind of liquid-liquid reactions still.
Background technology
The mixing general using agitator of liquid-liquid reactions and circulating pump mix the feed liquid in the raw material still in the prior art.Its weak point is that the circulating pump service efficiency is lower, and to accomplish that reaction effect is good, and needing sometimes from circulation fluid, to drop into raw material, the difficulty that the feed liquid in the reactor was mixed in the short time is big, mixed effect is bad, causes the yield of product to be difficult to improve.
Technology contents
The purpose of this utility model is to overcome the deficiencies in the prior art and a kind of well-mixed jet mixer of feed liquid that makes in the liquid-liquid reactions still is provided.
The technical solution of the utility model is: jet mixer is made up of disk distributor and nozzle, some distribution head are arranged on the disk distributor, nozzle is installed on the distribution head, and the disk distributor is installed on the circulating-pump outlet pipe in the reactor by the circulation fluid inlet tube on it.
The further technical scheme of the utility model is: nozzle is a Venturi nozzle, and it comprises jet pipe, suction chamber, mixing tube and anemostat, and jet pipe links to each other with anemostat with mixing tube by suction chamber, and the suction chamber bottom has drain.
The utility model further technical scheme is: distribution head is distributed on the periphery of disk distributor.
The utility model has overcome low, the weak effect of mixing efficiency that prior art exists, and the deficiency that product yield is low has following advantage:
1, simple in structure, easy for installation.
2, good mixing effect, the product yield height: jet mixer produces two kinds of hybrid modes in the course of the work simultaneously: the one, and raw material mixes in the mixing tube of nozzle in the liquid in the sucting reaction still and the circulation fluid, the 2nd, the kinetic energy that goes out liquid owing to nozzle ejection is big, can make the interior liquid of reactor stir, mix, so good mixing effect, the product yield height.
Description of drawings
Below in conjunction with drawings and Examples structure of the present utility model is further described.
Accompanying drawing 1 is a structural representation of the present utility model;
Accompanying drawing 2 is the structural representation of the utility model disk distributor;
Accompanying drawing 3 is the vertical view of accompanying drawing 2;
Accompanying drawing 4 is the structural representation of the utility model Venturi nozzle.
The specific embodiment
As shown in drawings: jet mixer is made up of disk distributor (1) and Venturi nozzle (2), circulation fluid inlet tube (3) and distribution head (4) are arranged on the disk distributor (1), (5), distribution head (4), (5) meet at right angles respectively with the housing of disk distributor (1) and the oblique angle is distributed on the periphery of disk distributor (1), distribution head is connected by flange with Venturi nozzle (2), Venturi nozzle comprises jet pipe (6), suction chamber (7), mixing tube (8) and anemostat (9), jet pipe (6) links to each other with anemostat (9) with mixing tube (8) by suction chamber (7), suction chamber (7) bottom has drain (10), and disk distributor (1) links to each other by the circulating-pump outlet pipe (12) interior with being installed in reactor (11) of the circulation fluid inlet tube (3) on it.The installation dimension of jet mixer and the number of plies are determined according to raw material input port quantity and reactor draw ratio, the quantity of distribution head determines that according to the flow size and the mixed effect of circulating pump the periphery angulation of distribution head and disk distributor is determined according to reactor draw ratio and mixed effect on the size dimension of disk distributor and Venturi nozzle and the disk distributor.
During work, by disk distributor (1) circulation fluid that circulating-pump outlet pipe (12) transports out is passed through distribution head (4), (5) be evenly distributed to Venturi nozzle (2), Venturi nozzle (2) just is equivalent to an ejector vacuum pump, the circulation fluid with certain pressure that the circulating-pump outlet pipe is transported sprays with high-speed jet from Venturi nozzle (2) lining, changes of section by means of each several part in the Venturi nozzle, form certain vacuum, make liquid-liquid reactions still (11) interior feed liquid and transport by circulating-pump outlet pipe (12), the raw material that drops in circulation fluid fully mixes, thereby reach good mixing effect, the purpose that product yield is high.
Claims (5)
1, a kind of jet mixer is characterized in that being made up of disk distributor and nozzle, and some distribution head are arranged on the disk distributor, and nozzle is installed on the distribution head, and the disk distributor is installed on the circulating-pump outlet pipe in the reactor by the circulation fluid inlet tube on it.
2, jet mixer as claimed in claim 1 is characterized in that nozzle is a Venturi nozzle, and it comprises jet pipe, suction chamber, mixing tube and anemostat, and jet pipe links to each other with anemostat with mixing tube by suction chamber, and the suction chamber bottom has drain.
3, jet mixer as claimed in claim 1 or 2 is characterized in that distribution head is distributed on the periphery of disk distributor.
4, jet mixer as claimed in claim 1 or 2, the housing that it is characterized in that distribution head and disk distributor meets at right angles respectively and the oblique angle is distributed on the periphery of disk distributor.
5, jet mixer as claimed in claim 3, the housing that it is characterized in that distribution head and disk distributor meets at right angles respectively and the oblique angle is distributed on the periphery of disk distributor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01249739 CN2502777Y (en) | 2001-09-18 | 2001-09-18 | Jet mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01249739 CN2502777Y (en) | 2001-09-18 | 2001-09-18 | Jet mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2502777Y true CN2502777Y (en) | 2002-07-31 |
Family
ID=33660045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01249739 Expired - Fee Related CN2502777Y (en) | 2001-09-18 | 2001-09-18 | Jet mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2502777Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103002977A (en) * | 2010-05-05 | 2013-03-27 | 沃依特专利有限责任公司 | Process and apparatus for addition of a chemical to a process stream |
| CN106179299A (en) * | 2016-06-24 | 2016-12-07 | 崔建中 | The Preparation equipment of the aerogels of load nano-titanium oxide |
| US9677039B2 (en) | 2009-05-20 | 2017-06-13 | Xyleco, Inc. | Processing biomass |
| US9771520B2 (en) | 2009-05-20 | 2017-09-26 | Xyleco, Inc. | Processing hydrocarbon-containing materials |
-
2001
- 2001-09-18 CN CN 01249739 patent/CN2502777Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9677039B2 (en) | 2009-05-20 | 2017-06-13 | Xyleco, Inc. | Processing biomass |
| US9771520B2 (en) | 2009-05-20 | 2017-09-26 | Xyleco, Inc. | Processing hydrocarbon-containing materials |
| US9969938B2 (en) | 2009-05-20 | 2018-05-15 | Xyleco, Inc. | Processing hydrocarbon-containing materials |
| CN103002977A (en) * | 2010-05-05 | 2013-03-27 | 沃依特专利有限责任公司 | Process and apparatus for addition of a chemical to a process stream |
| CN103002977B (en) * | 2010-05-05 | 2015-11-25 | 沃依特专利有限责任公司 | For chemicals being mixed into the method and apparatus in process streams |
| CN106179299A (en) * | 2016-06-24 | 2016-12-07 | 崔建中 | The Preparation equipment of the aerogels of load nano-titanium oxide |
| CN106179299B (en) * | 2016-06-24 | 2019-08-02 | 英鸿纳米科技股份有限公司 | Load the Preparation equipment of the aerogels of nano-titanium oxide |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203291868U (en) | Jet reaction device | |
| CN101185859B (en) | Jet current atomizing mixer for bioreactor | |
| CN105505749A (en) | Air-liquid dual injection type airlift loop reactor | |
| CN205995420U (en) | A kind of bubble-liquid two-phase jet reactor and bubble-liquid two-phase jet reaction system | |
| CN106076211A (en) | A kind of bubble-liquid two-phase jet reactor and bubble-liquid two-phase jet response system | |
| CN218012101U (en) | Novel emulsification equipment | |
| CN2502777Y (en) | Jet mixer | |
| CN205392370U (en) | Take gas recovery device's gas -liquid mixture reactor for chemical industry | |
| CN219400172U (en) | Horizontal high-yield nano material reactor | |
| CN115322219B (en) | Continuous production system and method for isopropyl titanate | |
| CN205676168U (en) | A kind of carburizing reagent system of injection reactor and nano-calcium carbonate | |
| CN116603481A (en) | Three-layer self-priming stirring type reactor | |
| CN210206433U (en) | Pneumatic spiral desulfurizing tower | |
| CN212741326U (en) | Amino acid biological fermentation rapid reaction system | |
| CN105800659A (en) | Spraying reactor and carbonization reaction system of nano calcium carbonate | |
| CN200963574Y (en) | Fluid driven impeller stirring type reaction device | |
| CN206853685U (en) | A kind of liquid reactions kettle that stirring is aided in using liquid convection | |
| CN221267736U (en) | Jet mixing system | |
| CN221141704U (en) | High-efficient feed supplement frock and system for fermentation cylinder | |
| CN219117429U (en) | Biological fermentation tank with jet stirring device | |
| CN1315565C (en) | Dispersion medium circulation and pipe stirring method | |
| CN212039904U (en) | A high-efficient gas-liquid mixture device for xylene oxidation reaction | |
| CN217725376U (en) | Cyclone gas distributor | |
| CN221452600U (en) | Continuous rapid mass transfer topology reaction device | |
| CN219363371U (en) | Waste acid liquid treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |