CN203678149U - Combined gas-solid separator for treating high concentration - Google Patents

Combined gas-solid separator for treating high concentration Download PDF

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Publication number
CN203678149U
CN203678149U CN201320871971.4U CN201320871971U CN203678149U CN 203678149 U CN203678149 U CN 203678149U CN 201320871971 U CN201320871971 U CN 201320871971U CN 203678149 U CN203678149 U CN 203678149U
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CN
China
Prior art keywords
guide vane
gas
tube wall
solid
separation
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Expired - Fee Related
Application number
CN201320871971.4U
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Chinese (zh)
Inventor
孙茂生
谢绪扬
马汉卿
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China University of Petroleum East China
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China University of Petroleum East China
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Priority to CN201320871971.4U priority Critical patent/CN203678149U/en
Application granted granted Critical
Publication of CN203678149U publication Critical patent/CN203678149U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a combined gas-solid separator for treating high concentration. According to the technical scheme, an inlet pipe is connected to the lateral wall of the upper part of a cylinder body, a conical ash hopper is arranged at the bottom of the cylinder body, and an exhaust pipe is connected to the top part of the cylinder body; a gas-solid separation device is arranged in the inner cavity of the cylinder body and comprises a first-stage guide vane, a side seam, a second-stage guide vane, a diversion core pipe, an anti-re-entrainment cone and a separation tube wall, wherein the first-stage guide vane is arranged on the upper part of the separation tube wall, and a plurality of side seams are formed in the tube wall of the lower part of the first-stage guide vane; the second-stage guide vane is arranged on the lower part of the side seams; the anti-re-entrainment cone is arranged at the lowest end of the separation tube wall; an exhaust pipe is arranged at the center of the separation tube wall. The combined gas-solid separator has the beneficial effects that the gas-solid separation efficiency can be improved by adopting the two-stage separation mode, but pressure drop of the equipment is hardly increased, the direct-current and countercurrent inversion modes are effectively combined, the advantages of each separation mode are sufficiently utilized, and the problem of separating high solid concentration can be solved.

Description

A kind of combined gas solid separator of processing higher concentration
Technical field
The utility model relates to a kind of device of gas solid separation of petrochemical industry, particularly a kind of combined gas solid separator of processing higher concentration.
Background technology
At present, equipment about gas solid separation is a lot, but for the gas solid separation research that contains higher concentration and few, and this operating mode is more common, such as catalytic cracking fourth stage separator is exactly for this operating mode, at the scene in application, adopt cut flow-type separator more, there is certain effect, but higher owing to entering to suck catalyst concn, the effect of this single-stage separator is still difficult to reach requirement, the on-the-spot circumstances that often occurs critical spray nozzle wearing and tearing, and too much solid catalyst is discharged in atmosphere, contaminated environment, therefore, be necessary very much separator herein to be improved.
Summary of the invention
The purpose of this utility model is exactly in view of the foregoing defects the prior art has, and a kind of combined gas solid separator of processing higher concentration is provided, and its principle based on centrifugation is utilized direct current separation to reverse to separate with adverse current and combined.
Its technical scheme is: comprise that separator is by inlet tube, blast pipe, gas-solid separating device, cylindrical shell, ash bucket, in described cylindrical shell upper portion side wall, connect inlet tube, bottom is the ash bucket of taper, top connects blast pipe, described cylinder lumen is provided with gas-solid separating device, gas-solid separating device comprises first order guide vane, latasuture, second level guide vane, shunting core pipe, anti-back-mixing is bored and is separated tube wall, the top that separates tube wall is provided with first order guide vane, the tube wall of the bottom of first order guide vane is provided with many latasutures, second level guide vane is installed in the bottom of latasuture, what separate tube wall is anti-back-mixing cone bottom, the center of described separation tube wall is provided with blast pipe.
Above-mentioned blast pipe outer end connects gas fairlead, and the bottom of blast pipe is shunting core pipe.
The beneficial effects of the utility model are: the mode that adopts two-stage to separate, improve gas solid separation efficiency, the pressure drop that does not simultaneously cause equipment increases how many, effectively direct current and adverse current inversion mode are combined, make full use of the advantage of every kind of separate mode, reach the separation problem that solves higher solids concentrations, be applicable to process the gas solid separation of higher concentration.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model;
Accompanying drawing 2 is schematic diagrames of guide vane A-A;
Accompanying drawing 3 is schematic diagrames of tube wall latasuture B-B;
Accompanying drawing 4 is schematic diagrames of shunting core pipe C-C;
In upper figure: inlet tube 1, blast pipe 2, first order guide vane 3, latasuture 4, second level guide vane 5, shunting core pipe 6, anti-back-mixing cone 7, cylindrical shell 8, ash bucket 9, gas fairlead 10, separation tube wall 11.
Detailed description of the invention
1-4 by reference to the accompanying drawings, the utility model will be further described:
The utility model comprises that separator is by inlet tube 1, blast pipe 2, gas-solid separating device, cylindrical shell 8, ash bucket 9, in described cylindrical shell 8 upper portion side wall, connect inlet tube 1, bottom is the ash bucket 9 of taper, top connects blast pipe 2, described cylindrical shell 8 inner chambers are provided with gas-solid separating device, gas-solid separating device comprises first order guide vane 3, latasuture 4, second level guide vane 5, shunting core pipe 6, anti-back-mixing cone 7 with separate tube wall 11, the top that separates tube wall 11 is provided with first order guide vane 3, the tube wall of the bottom of first order guide vane 3 is provided with many latasutures 4, second level guide vane 5 is installed in the bottom of latasuture 4, what separate tube wall 11 is anti-back-mixing cone 7 bottom, described separation tube wall 11 center is provided with blast pipe 2.
Above-mentioned blast pipe 2 outer ends connect gas fairlead 10, and the bottom of blast pipe 2 is shunting core pipe 6.
When use, gas-solid mixture enters from separator inlet 1, enters first order guide vane 3 and makes and revolve, due to the effect of centrifugal force, solid particle is thrown to limit wall, during through the latasuture 4 of tube wall, discharge from latasuture, then flow into rewinding tank along wall downwards by gravity, be also attended by a small amount of gas simultaneously and discharge, the increase of gas causes the rising of cavity inside pressure, in the time that pressure reach a certain height, gas can enter in blast pipe by gas fairlead 10, and pressure keeps constant afterwards; Now in separator tube, solid concentration declines, and then enters second level guide vane 5 and further makes and revolve, under the effect of centrifugal force, solid is thrown to wall, enters ash bucket by gravity current, and separator center pressure is low, gas, to center flow, is then discharged from blast pipe 2.Finally, contained solid is all collected in ash bucket, discharges from discharge gate, and clean gas is discharged from blast pipe, has realized the gas solid separation of higher concentration.The existence of shunting core pipe 6, has improved separating effect, has reduced short-circuit flow; Anti-back-mixing cone 7 prevent the separated particle getting off again back-mixing enter in separator.In addition, the direction of cracking of first order guide vane, second level guide vane, tube wall latasuture and shunting core pipe is identical, is beneficial to separation.

Claims (2)

1. process the combined gas solid separator of higher concentration for one kind, it is characterized in that: comprise that separator is by inlet tube (1), blast pipe (2), gas-solid separating device, cylindrical shell (8), ash bucket (9), in described cylindrical shell (8) upper portion side wall, connect inlet tube (1), bottom is the ash bucket (9) of taper, top connects blast pipe (2), described cylindrical shell (8) inner chamber is provided with gas-solid separating device, gas-solid separating device comprises first order guide vane (3), latasuture (4), second level guide vane (5), anti-back-mixing is bored (7) and is separated tube wall (11), the top that separates tube wall (11) is provided with first order guide vane (3), the tube wall of the bottom of first order guide vane (3) is provided with many latasutures (4), second level guide vane (5) is installed in the bottom of latasuture (4), what separate tube wall (11) is anti-back-mixing cone (7) bottom, the center of described separation tube wall (11) is provided with blast pipe (2).
2. a kind of combined gas solid separator of processing higher concentration according to claim 1, is characterized in that: described blast pipe (2) outer end connects gas fairlead (10), and the bottom of blast pipe (2) is shunting core pipe (6).
CN201320871971.4U 2013-12-27 2013-12-27 Combined gas-solid separator for treating high concentration Expired - Fee Related CN203678149U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320871971.4U CN203678149U (en) 2013-12-27 2013-12-27 Combined gas-solid separator for treating high concentration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320871971.4U CN203678149U (en) 2013-12-27 2013-12-27 Combined gas-solid separator for treating high concentration

Publications (1)

Publication Number Publication Date
CN203678149U true CN203678149U (en) 2014-07-02

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320871971.4U Expired - Fee Related CN203678149U (en) 2013-12-27 2013-12-27 Combined gas-solid separator for treating high concentration

Country Status (1)

Country Link
CN (1) CN203678149U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115477279A (en) * 2022-09-15 2022-12-16 山东建筑大学 Cyclone reactor for producing hydrogen by solar-driven methane thermal cracking

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115477279A (en) * 2022-09-15 2022-12-16 山东建筑大学 Cyclone reactor for producing hydrogen by solar-driven methane thermal cracking
CN115477279B (en) * 2022-09-15 2023-11-28 山东建筑大学 Rotational flow reactor for preparing hydrogen by thermally cracking methane driven by solar energy

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C53 Correction of patent for invention or patent application
CB03 Change of inventor or designer information

Inventor after: Sun Maosheng

Inventor after: Xie Xuyang

Inventor after: Ma Hanqing

Inventor after: Wang Jianjun

Inventor after: Jin Youhai

Inventor before: Sun Maosheng

Inventor before: Xie Xuyang

Inventor before: Ma Hanqing

COR Change of bibliographic data

Free format text: CORRECT: INVENTOR; FROM: SUN MAOSHENG XIE XUYANG MA HANQING TO: SUN MAOSHENG XIE XUYANG MA HANQING WANG JIANJUN JIN YOUHAI

CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140702

Termination date: 20141227

EXPY Termination of patent right or utility model