CN2766942Y - Single-tube multi-rotary stream body mixing device - Google Patents
Single-tube multi-rotary stream body mixing device Download PDFInfo
- Publication number
- CN2766942Y CN2766942Y CN200420055315.8U CN200420055315U CN2766942Y CN 2766942 Y CN2766942 Y CN 2766942Y CN 200420055315 U CN200420055315 U CN 200420055315U CN 2766942 Y CN2766942 Y CN 2766942Y
- Authority
- CN
- China
- Prior art keywords
- tube
- mixing
- many rotary
- single tube
- flight
- 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 - Lifetime
Links
Images
Abstract
The utility model relates to a single-tube multi-rotary stream body mixing device which comprises a fluid input pipeline and a mixed fluid outlet pipeline. The utility model is characterized in that at least one single-tube multi-rotary stream body mixing tube is arranged between the fluid input pipeline and the mixed fluid outlet pipeline. The inlet end of the fluid input pipeline and the he inlet end of the mixing fluid outlet pipeline are connected, and the outlet end of the mixing fluid outlet pipeline and the he inlet end of the single-tube multi-rotary stream body mixing tube are connected. When a plurality of single-tube multi-rotary stream body mixing tubes are adopted, contiguous two single-tube multi-rotary stream body mixing tubes can be abutted or connected through a connecting tube. The utility model has the advantages that device investment is little; ground occupation is small; mixing effects are good; the device is not provided with any moving member; faults are not easy to occur, production valid time is increased; the system is totally-enclosed without leakage; the utility model is suitable for mixing inflammable, explosive and toxic media. The operating flexibility of the electric hammer friction plate clutch device is large, and the electric hammer friction plate clutch device can be stably operated in a wide operation capacity range.
Description
(1) technical field
The utility model relates to fluid foods mixing arrangement and the married operation process in a kind of industrial production, and what be specifically related to is that liquid-liquid mixes gentle-liquid mixing arrangement.
(2) technical background
Mixing is the uniform operating process that the material of two or more different material or different conditions is reached disperseing mutually each other.Married operation is widely used in industrial production, and comprising in industries such as oil, chemical industry, medicine, agricultural chemicals, dyestuff, paint, and it is the most general to be used for chemical reaction.The typical operation that industrial realization mixes is to mix and spray mixing.Mix to people generally adopt, it uses history longer, and use experience is abundant.Mixing and using maximum occasions is stirred-tank reactor.Mix complex structure, generally invest higherly, floor space is big, the energy consumption height.During the course of reaction that is used for transmitting with heat, heat-transfer area is restricted.Be augmentation of heat transfer, when in still, coiled pipe being housed.Mix when being used for non-atmospheric operation, because the stretching into of turning cylinder, sealing place is leaked easily, causes stopping production when serious, and effective time is produced in influence.Mix when being used for successive reaction, generally need many still series connection, operation control is complicated.The vertical stirred tank of seeing at present though the shaft mounting means is different, is single shaft and stirs.And spray to mix is a kind of fluid high-speed to be flowed aspirate one other fluid, and after two kinds of fluids converged, bumping turbulence occurred and realize mixing.It is little to spray married operation elasticity, can't operate in the output scope of broad.Owing to spray mixing is that fluid collides mutually and turbulence occurs and realize mixing, thereby energy consumption is big.In addition, jet cleaning makes mixed object emulsification occur easily.
(3) summary of the invention
The purpose of this utility model provides a kind of small investment, good energy-conserving effect, floor space is little, mixing efficiency is high, simple to operate, fluid is realized the new mixing arrangement that mixes on the pipeline inner edge limit of flowing.
The technical scheme that adopts is:
Many rotary fluids of single tube mixing arrangement comprises at least one many rotary fluids of single tube mixing tube and fluid intake pipeline and outlet line.
When adopting a plurality of many rotary fluids of single tube mixing tube, dock between adjacent two many rotary fluids of single tube mixing tubes, or connect by junction pipe.
But in many rotary fluids of single tube mixing tube, be installed with the flight that relative static convection cell with pipeline produces cutting, distortion, displacement, distortion, dispersion, amalgamation.
In the mixing tube of many coils of single tube formula fluid mixer, can arrange at least two flights of quantity on the same cross section, flight can be levoform or dextrorotation formula, n flight is one group, the identical or any setting of the rotation direction of one group of flight, and the angle between flight is α=0-180 °.
Along many rotary fluids of single tube mixing tube axis direction, can set firmly many group flights, if a certain group of flight revolves for a left side (right side), then the adjacent set flight revolves for right (left side), can link from beginning to end vertically between group and the group, also can keep certain distance.
The two adjacent groups flight is arranged along the circumference β=0-90 ° of angle that stagger in above-mentioned many rotary fluids of single tube mixing tube.
Can set firmly mandrel in above-mentioned many rotary fluids of single tube mixing tube, flight can be installed on the mandrel.
Above-mentioned mandrel is solid, also can be hollow.
When above-mentioned mandrel is hollow, when being the core pipe, can feed heating or cooling medium in the core pipe as required, carry out exchange heat with fluid in the mixing tube.
There is not relative motion between above-mentioned mandrel or core pipe, flight, mixing tube body.
Many rotary fluids of single tube mixing tube outside can be provided with jacket pipe, is used to feed heating or cooling medium, carries out exchange heat with the mixing tube inner fluid.
Many rotary fluids of single tube mixing tube can singlely use, and also can use by a plurality of serial or parallel connections, when a plurality of serial or parallel connections use, can connect by connecting tube, and connecting mode can use welding, thread connection or flange to connect.
Also can not establish mandrel in above-mentioned many rotary fluids of single tube mixing tube, and above-mentioned flight can with other convection cell rise cutting, distortion, displacement, distortion, dispersion, merge in establish chemical filler and hybrid element replaces.
Many rotary fluids of single tube mixing arrangement can be arranged vertically, horizontally disposed or be in tilted layout, also can be vertically, level, inclination combination arrange.
The above-mentioned do of outside diameter of mandrel is 0-300mm.
Above-mentioned many rotary fluids of single tube mixing tube inside diameter D i is 10-1000mm.
The many rotary fluid mixing of above-mentioned single tube pipe range L is 100-6000mm.
The width of above-mentioned flight should be less than (Di-do)/2.
The length of above-mentioned flight is 0.5-4 times of flight width.
The technical essential of many rotary fluids of single tube mixing arrangement method of operating is: material W 1. to be mixed
1, W
2W
M-1, W
mEnter many rotary fluids of single tube mixing arrangement inlet in proportion through pipeline; When 2. each strand material enters many rotary fluids of single tube mixing arrangement and flows through flight successively, be forced to rotation and produce cutting, distortion, disperse, merge, displacement, distortion, after the flight group of the some of flowing through, just can reach the mixability that needs.3. the material that reaches the regulation mixability is flowed out by outlet; 4. material mobile required motive force in many rotary fluids of single tube mixing arrangement can be provided by pump, potential difference or Compressed Gas etc.
The utlity model has following advantage:
1. equipment investment is few, can save equipment investment 1/3～1/2 with mixing to compare;
2. the plant area area is little, is easy to arrange;
3. do not have moving link, be difficult for breaking down, can increase and produce effective time;
4. system is totally-enclosed, does not have to leak, and can reduce environmental pollution, improves working condition, is particularly suitable for the mixing of inflammable, explosive, poisonous medium;
5. material is a Laminar Flow in pipe, also can realize mixing, and energy consumes low;
6. operating flexibility is big, can stably operate in the broad range of flow;
7. the many rotary fluids of single tube mix the occasion that can be applicable to only take place between fluid physical mixed, also can be applicable to take place between fluid the mixing of the occasion of chemical reaction.
(4) description of drawings
Fig. 1 is the structural representation of a kind of embodiment of the present utility model.
Fig. 2 is second kind of example structure schematic diagram of the present utility model.
Fig. 3 is the axial section of many rotary fluids of single tube mixing tube.
Fig. 4 is a single tube rotary fluid mixing tube transverse cross-sectional view.
Fig. 5 is a right hand helix chip architecture schematic diagram.
Fig. 6 is left-handed flight structural representation.
(5) specific embodiment
Embodiment one
Many rotary fluids of single tube mixing arrangement, comprise the fluid feed line 1 that has three fluid intakes, four many rotary fluids of single tube mixing tubes 2, three sections connecting tubes 3, one section fluid-mixing outlet line 4, a core pipe 7, three kinds of fluids enter many rotary fluids of single tube mixing tube 2 through fluid feed line 1, every many rotary fluids of single tube mixing tube 2 length 3m, nominal diameter 200mm, in to establish core pipe 7 diameters be 32mm, the inner flight 5 or 6 that is provided with is 3 every group, and the angle between same group of flight is α=120 °, the two adjacent groups flight β=60 ° layout that staggers, the flight width is 80mm, and length is 100mm.
Concrete mounting means:
The fluid feed line 1 that has three fluid intakes is connected by flange with the arrival end of many rotary fluids of single tube mixing tube 2; The connection of three sections connecting tubes of four many rotary fluids of single tube mixing tube 2 usefulness, 3 usefulness flanges is arranged vertically; In many rotary fluids of single tube mixing tube 2 core pipe 7 is set; The flight 5,6 that is provided with in many rotary fluids of single tube mixing tube 2, end to end between flight group and the group; The outlet of many rotary fluids of single tube mixing tube 2 connects with mixed material outlet line 4 usefulness flanges, constitutes many rotary fluids of single tube mixing arrangement.This device can mix three kinds of fluids.
Embodiment two
Embodiment two and embodiment one are basic identical, and difference is: have two fluid intakes on the fluid feed line, device mixes two kinds of fluids.
Embodiment three
Embodiment three and embodiment one are basic identical, and difference is that many rotary fluids of single tube mixing tube 2 inner flights 5 that are provided with or 6 are 4 every group, angle α=90 between same group of flight °, the two adjacent groups flight β=45 ° layout that staggers.Many rotary fluids of single tube mixing tube is provided with chuck outward.
Embodiment four
Many rotary fluids of single tube mixing arrangement comprises the fluid feed line 1 that has five fluid intakes, and 4, three kinds of fluids of 3, one sections fluid issuing pipelines of 2, two sections connecting tubes of many rotary fluids of six roots of sensation single tube mixing tube enter many rotary fluids of single tube mixing tube 2 through fluid feed line 1.The length that every single tube revolves mixing tube 2 more is 3m, and nominal diameter is 150mm, in to establish mandrel 7 diameters be 25mm.The inner flight 5 that is provided with or 6 every groups 3, the angle between same group of flight is α=120 °, the β=60 ° layout that staggers between the two adjacent groups flight, flight width 60mm, length 60mm.
Concrete mounting means:
The fluid feed line 1 that has five fluid intakes connects with flange with the inlet of many rotary fluids of single tube mixing tube 2, and per two many rotary fluids of single tube mixing tube 2 usefulness flanges connect forms one group.Three groups of many rotary fluids of single tube mixing tube groups connect horizontally disposed with two sections connecting tubes, 3 usefulness flanges.In many rotary fluids of single tube mixing tube mandrel 7 is set, head and the tail spacing 30mm between flight group and the group.Mixed material outlet line 4 connects with flange with the outlet of many rotary fluids of single tube mixing tube 2, constitutes many rotary fluids of single tube mixing arrangement, and this device can mix five kinds of fluids.
Embodiment five
Embodiment five and embodiment four are basic identical, and difference is that fluid feed line 1 has two fluid intakes, and the length of every many rotary fluids of single tube mixing tube 2 is 5m, and nominal diameter is 500mm, in establish core pipe 7 and be 100mm.Flight width 200mm, length 300mm.Many rotary fluids of single tube mixing tube 2 peripheral hardware chucks, external jacket and core pipe 7 logical heating or cooling mediums.
Embodiment six
Embodiment six and embodiment five are basic identical, and difference is the length 6m of every many rotary fluids of single tube mixing tube 2, and nominal diameter is 800mm, and interior is 250mm for establishing core pipe 7, flight 5,6 width 270mm, and length is 400mm.
Embodiment seven
Many rotary fluids of single tube mixing arrangement comprises 2, the one sections fluid-mixing outlet lines of 1, four many rotary fluid of single tube of fluid feed line mixing tube that have two fluid intakes, and two kinds of fluids enter many rotary fluids of single tube mixing tube 2 through fluid feed line 1.The length of every many rotary fluids of single tube mixing tube 2 is 2m, nominal diameter is 125mm, in establish core pipe 7 nominal diameter 25mm, the inner flight 5 or 6 that is provided with is 3 every group, angle between same group of flight is α=120 °, β=60 ° the layout that staggers between the two adjacent groups flight, the wide 52mm of flight, long 60mm.
Concrete mounting means:
Fluid input tube line 1 connects with flange with the inlet of many rotary fluids of single tube mixing tube 2.Two many rotary fluids of single tube mixing tube 2 usefulness flanges are linked together, and are horizontally disposed, and its outlet connects with mixed material outlet line 4 usefulness flanges, constitute many rotary fluids of single tube mixing arrangement, can mix two kinds of fluids.
Embodiment eight
Embodiment eight and embodiment seven are basic identical, and difference is that four many rotary fluids of single tube mixing tube 2 outsides are provided with external jacket, is linked together with flange to be arranged vertically.
Embodiment nine
Embodiment nine and embodiment seven are basic identical, and difference is that three many rotary fluids of single tube mixing tube 2 usefulness flanges are linked together and level angle at 45 layout.
Embodiment ten
Embodiment ten and embodiment seven are basic identical, and difference is a centreless pipe (or mandrel) 7 in many rotary fluids of single tube mixing tube, with the flight 5,6 in many rotary fluids of chemical filler replacement single tube mixing tube 2.
Claims (8)
1, many rotary fluids of single tube mixing arrangement, comprise fluid input tube line (1), many rotary fluids of single tube mixing tube (2) and fluid-mixing outlet line (4), it is characterized in that between fluid input tube line (1) and fluid-mixing outlet line (4), being provided with at least one many rotary fluids of single tube mixing tube (2); Be installed with a plurality of flights (5), (6) in many rotary fluids of single tube mixing tube (2); Fluid input tube line (1) links with many rotary fluids of single tube mixing tube (2) arrival end, and fluid-mixing outlet line (4) links with the port of export of many rotary fluids of single tube mixing tube (2); When between fluid input tube line (1) and fluid-mixing outlet line (4) a plurality of many rotary fluids of single tube mixing tubes (2) being set, can adopt butt joint or connecting tube (3) to connect between adjacent two many rotary fluids of single tube mixing tubes (2).
2, many rotary fluids of single tube mixing arrangement according to claim 1 is characterized in that being installed with mandrel (7) in many rotary fluids of single tube mixing tube (2), and mandrel (7) can be solid shafting, also can be hollow shaft.
3, many rotary fluids of single tube mixing arrangement according to claim 1 is characterized in that can arranging that one group of quantity is the flight of n (5) or (6) on the same cross section in many rotary fluids of single tube mixing tube (2); Flight (5) or (6) can be levoform or dextrorotation formula; Identical or any setting of the rotation direction of one group of flight; Angle between flight is α=0-180 °.
4, many rotary fluids of single tube mixing arrangement according to claim 1, it is characterized in that to be provided with vertically in many rotary fluids of single tube mixing tube (2) many group flights (5), (6), when wherein one group of flight (5) is levoform or dextrorotation formula, then adjacent set flight (6) is dextrorotation formula or levoform, and along the circumferential direction stagger β=0-90 ° of angle of two adjacent groups flight arranged; The two adjacent groups flight can link vertically from beginning to end, also can keep certain distance.
5, according to claim 1,2,3,4,5 described many rotary fluids of single tube mixing arrangements, it is characterized in that: the internal diameter of many rotary fluids of single tube mixing tube (2) is: Di=10-1000mm, the external diameter of mandrel (7) is do=0-300mm, the width of flight (5) or (6) is 0-(Di-do)/2, and the length of flight (5) or (6) is 0.5-4 times of flight width.
6, many rotary fluids of single tube mixing arrangement according to claim 1 is characterized in that many rotary fluids of single tube mixing tube (2) outside can be provided with chuck, also can not be provided with chuck.
7, many rotary fluids of single tube mixing arrangement according to claim 1 is characterized in that fluid feed line (1) is provided with 2 fluid intakes at least.
8, many rotary fluids of single tube mixing arrangement according to claim 1, it is characterized in that many rotary fluids of single tube mixing tube (2) and connecting tube (3) can be vertical, level or be obliquely installed, also can be vertically, level, inclination combination be provided with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200420055315.8U CN2766942Y (en) | 2004-11-30 | 2004-11-30 | Single-tube multi-rotary stream body mixing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200420055315.8U CN2766942Y (en) | 2004-11-30 | 2004-11-30 | Single-tube multi-rotary stream body mixing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2766942Y true CN2766942Y (en) | 2006-03-29 |
Family
ID=36680802
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200420055315.8U Expired - Lifetime CN2766942Y (en) | 2004-11-30 | 2004-11-30 | Single-tube multi-rotary stream body mixing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2766942Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100457699C (en) * | 2006-04-24 | 2009-02-04 | 沈阳化工学院 | Dichloroethane prodn. plant via pipe type direct chloration of ethene, and process thereof |
| CN101343100B (en) * | 2008-08-28 | 2011-05-04 | 重庆交通科研设计院 | Dual treating device for wastewater of construction |
-
2004
- 2004-11-30 CN CN200420055315.8U patent/CN2766942Y/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100457699C (en) * | 2006-04-24 | 2009-02-04 | 沈阳化工学院 | Dichloroethane prodn. plant via pipe type direct chloration of ethene, and process thereof |
| CN101343100B (en) * | 2008-08-28 | 2011-05-04 | 重庆交通科研设计院 | Dual treating device for wastewater of construction |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101061321A (en) | Piping | |
| CN1781586A (en) | Single tube multiple swirler mixing device and its mixing operation method | |
| CN1191276A (en) | Axial turbine of tubocharger | |
| CN1740574A (en) | Ejector capable of raising the cavitation performance of centrifugal pump | |
| CN2766942Y (en) | Single-tube multi-rotary stream body mixing device | |
| CN1920469A (en) | Pipe type fluid turbulence device capable of strengthening mass and heat transfer and operation method thereof | |
| CN1939580A (en) | Static spiral mixer in tube | |
| CN113663546A (en) | Multistage static mixer and use method thereof | |
| CN101890253A (en) | Extraction multi-chamber mixer used in antibiotic production | |
| CN201735210U (en) | Extraction multi-chamber mixer used in antibiotic production | |
| CN1435275A (en) | Multistage circulation reactor | |
| CN201848235U (en) | Tube type gas-liquid reactor for synchronous swirling and jetting | |
| CN1807270A (en) | Fluid magnetization tube , magnetization device and magnetization system | |
| CN211621868U (en) | Pipeline connecting structure of sewage pipeline | |
| CN200998645Y (en) | Pipe fluid destabilization device capable of reinforcing mass transfer and heat transfer | |
| CN105060475A (en) | Jet mixing water distributing stirring device | |
| CN217083462U (en) | Turbulent flow device and tubular heat exchanger | |
| CN1321990C (en) | Apparatus and method for monotubular multi-spiral static mixed tube style chlorohydrination of propene for production of epoxypropane | |
| CN111154928A (en) | Environment-friendly leather laser cutting machine with reliable work | |
| CN2841135Y (en) | State in-tube spiral mixer | |
| CN1817912A (en) | Olefin polymerizing reactor | |
| CN209338358U (en) | A kind of sludge at low temperature pyrohydrolysis processing unit | |
| CN1022464C (en) | Static mixer for powder material | |
| CN214106745U (en) | Energy-saving automatic reaction material stirring type efficient mixer | |
| CN210891720U (en) | Spiral guide plate of slag cooler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CX01 | Expiry of patent term |
Expiration termination date: 20141130 Granted publication date: 20060329 |