CN205308342U - Heterogeneous reaction separation integration whirl reactor that mixes - Google Patents
Heterogeneous reaction separation integration whirl reactor that mixes Download PDFInfo
- Publication number
- CN205308342U CN205308342U CN201521033049.3U CN201521033049U CN205308342U CN 205308342 U CN205308342 U CN 205308342U CN 201521033049 U CN201521033049 U CN 201521033049U CN 205308342 U CN205308342 U CN 205308342U
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- China
- Prior art keywords
- mixing chamber
- guide vane
- cavity
- liquid flow
- static mixer
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- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The utility model discloses a heterogeneous reaction separation integration whirl reactor that mixes, include: feed liquor pipe, barrel, inlet pipe, feeding buffer tank, mixed cavity, fiaring cone, guide blade, liquid flow distributor, static mixer, conical duct, ejection of compact cavity and discharge gate, its characterized in that: be provided with mixed cavity in the barrel, it has been provided with the feed liquor pipe to mix the cavity upper end, feed liquor pipe and the mutual fixed connection of mixed cavity, the external cover of hybrid chamber is equipped with the feeding buffer tank, the feeding buffer tank with mix the mutual fixed connection of cavity, feeding buffer tank one side is provided with the feed liquor pipe, feed liquor pipe with the mutual fixed connection of feeding buffer tank, it is provided with guide blade to mix the cavity lower extreme. The utility model discloses be provided with liquid flow distributor and static mixer, the axial back mixing is few, can realize flash mixed, has easy operation and easily goes, mixes fast and move reliable and stable advantage.
Description
Technical field
This utility model relates to a kind of Integral cyclone reactor, particularly relates to a kind of heterogeneous hybrid reaction isolation integral Cyclonic reactor.
Background technology
At present, inhomogeneous reaction process is widely used in the engineering fields such as petrochemical industry, biological respinse, environmental conservation, and one of key of inhomogeneous reaction is to realize biphase high efficient mixed, be fully contacted, it is achieved biphase complete reaction and improve reaction rate. In general, mixed process is by main diffusion, eddy diffusivity and molecule diffusion under forced convertion effect, is finally reached molecular level Homogeneous phase mixing. Industry generally adopts mechanical agitation, design tortuous flow path, the high-speed impact of liquid or the mode turbulization such as injection at elevated pressures, to increase the mixing efficiency of liquid. The general type of conventional catalyst cracking reactor assembly: oil gas, promoting inner reaction tube formation gas-solid mixture, the fast separation structure sharp separation of boosted pipe end outlet, enters oil gas collection chamber then through cyclone separator, then introduces fractionating column through oil transfer line. In the last few years, in order to adapt to heavy crude, residual oil feature, catalytic cracking riser reactor has been carried out a series of improvement by many oil companies and research institution, specifically include that feed zone pre-lifting technology, heavy oil feed nozzle technology, sectional feeding technology, riser reaction terminating technology, riser end rapid separation, reclaimable catalyst high efficiency steam stripping technology, highly efficient regeneration technology etc., but owing to the time scale of mixing even between several hours, is usually used in the reaction system that reaction rate is slower in a few minutes. And, for partial reaction process, occur along with the prolongation in response time and the intensification of the extent of reaction have secondary response, produce non-purpose product, the serious economy reducing system.This just requires quickly mixing and reacting of Cyclonic reactor, and the raw material of product and part unreacted is carried out sharp separation after completing by primary response, and removes reactor, stops between product, the generation of secondary adverse reaction between product and raw material. Additionally, consider from the angle improving production efficiency, it is necessary to realizing continuous operation, course of reaction and separation process carry out simultaneously, feature and engineer applied present situation based on above inhomogeneous reaction, it is therefore desirable to a kind of integrated reaction and separation equipment carrying out quickly mixing.
Utility model content
Technical problem to be solved in the utility model is for above-mentioned the deficiencies in the prior art, provide a kind of heterogeneous hybrid reaction isolation integral Cyclonic reactor, this utility model is provided with liquid flow distribution device and static mixer, axial backmixing is few, can realize quick mixing, have that operation is simple, mixing quickly and the advantage of stable and reliable operation.
The technical solution of the utility model is: a kind of heterogeneous hybrid reaction isolation integral Cyclonic reactor, including: feed tube, cylinder, feed pipe, feed surge tank, mixing chamber, fiaring cone, guide vane, liquid flow distribution device, static mixer, conical pipe, discharging cavity and discharging opening, it is characterized in that: in described cylinder, be provided with mixing chamber, described mixing chamber upper end has been provided with feed tube, described feed tube and mixing chamber are mutually permanently connected, feed surge tank it is arranged with outside described mixing chamber, described feed surge tank and described mixing chamber are mutually permanently connected, described feed surge tank side is provided with feed tube, described feed tube and described feed surge tank are mutually permanently connected, described mixing chamber lower end is provided with guide vane, described guide vane and cylinder are connected with each other, described guide vane center is provided with fiaring cone, described fiaring cone and described guide vane are connected with each other, described guide vane lower end is provided with liquid flow distribution device, described liquid flow distribution device and described cylinder are connected with each other, it is provided with static mixer in described cylinder, described static mixer and described cylinder are connected with each other, described cylinder lower end is provided with discharging cavity, described discharging cavity and described cylinder are mutually permanently connected, described discharging cavity lower end is provided with discharging opening.
Further, described static mixer is orifice-plate type static mixer.
Further, described liquid flow distribution device is porose disc formula liquid flow distribution device.
Further, described conical pipe lower end is connected to exhaustor.
The beneficial effects of the utility model are in that: this utility model can realize reaction, isolation integral: this utility model is provided with fiaring cone and guide vane, the quantity of guide vane can be adjusted as required, the axially-movable of raw material and catalytic fluid is become screw by guide vane, provide the blending space of raw material and catalytic liquid, this utility model is provided with mixing chamber, mixing chamber can make raw material enter guide vane runner time distribution more uniform. Conical pipe can prevent the deposition of raw material, makes turbulivity improve, and contacting efficiency improves. This utility model is provided with liquid flow distribution device and static mixer, and axial backmixing is few, it is possible to achieve quickly mix, have that operation is simple, mixing quickly and the advantage of stable and reliable operation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein: 1, feed tube 2, cylinder 3, feed pipe
4, feed surge tank 5, mixing chamber 6, fiaring cone
7, guide vane 8, liquid flow distribution device 9, static mixer
10, conical pipe 11, exhaustor 12, discharging cavity
13, discharging opening
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is made brief description.
As shown in Figure 1, a kind of heterogeneous hybrid reaction isolation integral Cyclonic reactor, including: feed tube 1, cylinder 2, feed pipe 3, feed surge tank 4, mixing chamber 5, fiaring cone 6, guide vane 7, liquid flow distribution device 8, static mixer 9, conical pipe 10, discharging cavity 12 and discharging opening 13, it is characterized in that: in described cylinder 2, be provided with mixing chamber 5, described mixing chamber 5 upper end has been provided with feed tube 1, described feed tube 1 is mutually permanently connected with mixing chamber 5, it is arranged with feed surge tank 4 outside described mixing chamber 5, described feed surge tank 4 is mutually permanently connected with described mixing chamber 5, described feed surge tank 4 side is provided with feed tube 1, described feed tube 1 is mutually permanently connected with described feed surge tank 4, described mixing chamber 5 lower end is provided with guide vane 7, described guide vane 7 is connected with each other with cylinder 2, described guide vane 7 center is provided with fiaring cone 6, described fiaring cone 6 is connected with each other with described guide vane 7, described guide vane 7 lower end is provided with liquid flow distribution device 8, described liquid flow distribution device 8 is connected with each other with described cylinder 2, it is provided with static mixer 9 in described cylinder 2, described static mixer 9 is connected with each other with described cylinder 2, described cylinder 2 lower end is provided with discharging cavity 12, described discharging cavity 12 is mutually permanently connected with described cylinder 2, described discharging cavity 12 lower end is provided with discharging opening 13. this utility model is provided with fiaring cone and guide vane, the quantity of guide vane can be adjusted as required, the axially-movable of raw material and catalytic fluid is become screw by guide vane, provide the blending space of raw material and catalytic liquid, this utility model is provided with mixing chamber, mixing chamber can make raw material enter guide vane runner time distribution more uniform. conical pipe can prevent the deposition of raw material, makes turbulivity improve, and contacting efficiency improves. this utility model is provided with liquid flow distribution device and static mixer, and axial backmixing is few, it is possible to achieve quickly mix, have that operation is simple, mixing quickly and the advantage of stable and reliable operation.
Above example is only in order to illustrate the technical solution of the utility model, it is impossible to limit scope of the present utility model with this; The amendment that technical scheme described in foregoing embodiments is carried out, or to the equivalent replacement that wherein portion of techniques feature carries out, the essence not making appropriate technical solution departs from the spirit and scope of each embodiment technical scheme of this utility model, all should still belong in the scope that this utility model patent contains.
Claims (4)
1. a heterogeneous hybrid reaction isolation integral Cyclonic reactor, including: feed tube, cylinder, feed pipe, feed surge tank, mixing chamber, fiaring cone, guide vane, liquid flow distribution device, static mixer, conical pipe, discharging cavity and discharging opening, it is characterized in that: in described cylinder, be provided with mixing chamber, described mixing chamber upper end has been provided with feed tube, described feed tube and mixing chamber are mutually permanently connected, feed surge tank it is arranged with outside described mixing chamber, described feed surge tank and described mixing chamber are mutually permanently connected, described feed surge tank side is provided with feed tube, described feed tube and described feed surge tank are mutually permanently connected, described mixing chamber lower end is provided with guide vane, described guide vane and cylinder are connected with each other, described guide vane center is provided with fiaring cone, described fiaring cone and described guide vane are connected with each other, described guide vane lower end is provided with liquid flow distribution device, described liquid flow distribution device and described cylinder are connected with each other, it is provided with static mixer in described cylinder, described static mixer and described cylinder are connected with each other, described cylinder lower end is provided with discharging cavity, described discharging cavity and described cylinder are mutually permanently connected, described discharging cavity lower end is provided with discharging opening.
2. the heterogeneous hybrid reaction isolation integral Cyclonic reactor of one according to claim 1, it is characterised in that: described static mixer is orifice-plate type static mixer.
3. the heterogeneous hybrid reaction isolation integral Cyclonic reactor of one according to claim 1, it is characterised in that: described liquid flow distribution device is porose disc formula liquid flow distribution device.
4. the heterogeneous hybrid reaction isolation integral Cyclonic reactor of one according to claim 1, it is characterised in that: described conical pipe lower end is connected to exhaustor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521033049.3U CN205308342U (en) | 2015-12-09 | 2015-12-09 | Heterogeneous reaction separation integration whirl reactor that mixes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521033049.3U CN205308342U (en) | 2015-12-09 | 2015-12-09 | Heterogeneous reaction separation integration whirl reactor that mixes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205308342U true CN205308342U (en) | 2016-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521033049.3U Withdrawn - After Issue CN205308342U (en) | 2015-12-09 | 2015-12-09 | Heterogeneous reaction separation integration whirl reactor that mixes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205308342U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105363405A (en) * | 2015-12-09 | 2016-03-02 | 天津大港油田滨港集团博弘石油化工有限公司 | Heterogeneous phase mixing, reaction and separation integrated cyclone reactor |
-
2015
- 2015-12-09 CN CN201521033049.3U patent/CN205308342U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105363405A (en) * | 2015-12-09 | 2016-03-02 | 天津大港油田滨港集团博弘石油化工有限公司 | Heterogeneous phase mixing, reaction and separation integrated cyclone reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20160615 Effective date of abandoning: 20171114 |