CN101564623A - Method and device for separating gas from solid and sharing solid - Google Patents
Method and device for separating gas from solid and sharing solid Download PDFInfo
- Publication number
- CN101564623A CN101564623A CNA2008103012325A CN200810301232A CN101564623A CN 101564623 A CN101564623 A CN 101564623A CN A2008103012325 A CNA2008103012325 A CN A2008103012325A CN 200810301232 A CN200810301232 A CN 200810301232A CN 101564623 A CN101564623 A CN 101564623A
- Authority
- CN
- China
- Prior art keywords
- solid
- canvas
- gas
- separator
- high pressure
- 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.)
- Granted
Links
Images
Abstract
The invention discloses a method and a device for separating gas from solid and sharing the solid. The method comprises the following steps that: a mixed gas containing a powder solid is blown into a separating device through a feeding port; the separating device is provided with an inclined baffle plate; the powder solid impacts the baffle plate, then changes the movement direction and drops on a canvas in a current dividing device; the lower side of the canvas is provided with a high-pressure air inlet, and a high-pressure air current makes the powder solid writhe and spread through canvas clearance; the same height of the bucket wall of the current dividing device is provided with two or more than two discharging ports; and when the stacking height of the powder solid exceeds the discharging ports, solid granules averagely overflow from the different discharging ports. The device has the advantages of small occupied area, low manufacturing cost, high separation efficiency, good separation effect, low powder material content in the separated gas and lightened load of a dust removing system. The separated powder material can be automatically and averagely divided into a plurality of portions, which is favorable for storage and convenient for facilitating the subsequent production process.
Description
Technical field
The present invention relates to a kind of gas solid separation and divide equally the method and the device of solid, belong to the gas solid separation technical field.
Background technology
In the granular material course of conveying of carbon industry and aluminium industry, adopt high pressure draught that granular material is carried out channelization usually and carry.Feed high pressure draught in the pipeline, granular material by under the drive of gases at high pressure along with air-flow flows in pipeline, what flow in the pipeline is the dusty gas of carrying granular material secretly.Owing to be mixed with solid powder and a large amount of gas in the pipeline, can't directly conveyance conduit be directly delivered to subordinate's transloading equipment or warehouse.Existing gas-solid separating device adopts natural sedimentation, and this method separative efficiency is low, poor effect, and gas separates not thorough with solid, and in the gas after the separation, granular material content is still very high, has strengthened the load of dust pelletizing system.Owing to reasons such as technology and storage warehouses, often the granular material after separating need be divided into some parts and handle in addition.Existing gas-solid separator also can't carry out material five equilibrium to be handled.
Summary of the invention
The object of the present invention is to provide a kind of floor space little, the gas solid separation that the cost cost is low is also divided equally the method and the device of solid, and it has the separative efficiency height, good separating effect, and in the gas after the separation, granular material content is low, can alleviate the load of dust pelletizing system.And the granular material automatic average break into portions after separating can be helped storing, also be convenient to can well overcome the deficiencies in the prior art in the carrying out smoothly of postorder production technology.
The present invention realizes like this, gas solid separation of the present invention and the method for dividing equally solid are: the mist that will contain powdery solid is blown into separator through charging aperture, be provided with the baffle plate of inclination in the separator, change the direction of motion behind the powdery solid impingement baffles, fall on the canvas in the part flow arrangement, the separation off gas mouth of the gas after the gas solid separation on separator is connected with dust pelletizing system; Be provided with the high pressure air inlet below canvas, the gap that high pressure draught sees through canvas is seethed powdery solid and is shakeout, and the high pressure draught that sees through the canvas gap is connected with dust pelletizing system from the separation panel gas port on the part flow arrangement; Bucket wall equal height at part flow arrangement is provided with two or more discharging openings, and when the height of powdery solid accumulation surpassed discharging opening, solid particle on average overflowed from different discharging openings simultaneously.
Above-mentioned gas solid separation is also divided equally in the method for solid, and the place is provided with spoiler at described high pressure air inlet, makes high pressure draught act on the canvas bottom uniformly; The canvas below is provided with porous plate, and high pressure draught is avoided along the canvas PARALLEL FLOW, strengthens the impact dynamics of air-flow, also canvas is played a supporting role simultaneously.
Aforesaid gas solid separation is also divided equally in the method for solid, is provided with inspection socket on described separator, is convenient to separator inside is overhauled or cleared up.
Gas solid separation of the present invention and the device of dividing equally solid are: it is made of separator 1 and part flow arrangement 2 two parts; The below of separator 1 is connected with part flow arrangement 2; Separator 1 comprises separating barrel 3, and separating barrel 3 is provided with separation off gas mouth 4, is provided with one or one baffle plate 5 to tilt and to install in the separating barrel 3, and separating barrel 3 walls relative with baffle plate 5 are provided with one or more charging aperture 6; Part flow arrangement 2 comprises shunting bucket 7 and bottom 8, divides comb bucket 7 bottoms to be connected with bottom 8, accompanies canvas 9 and porous plate 10 in the junction; Shunting bucket 7 is provided with separation panel gas port 11, divides the sidewall equal height of comb bucket 7 to be provided with two or more discharging openings 12; The bottom of bottom 8 is provided with high pressure air inlet 13, and high pressure air inlet 13 places are provided with spoiler 14.
Above-mentioned gas solid separation is also divided equally in the device of solid, and described baffle plate 5 is connected with the separating barrel wall through shaped steel 15, and baffle plate 5 is provided with feedstock direction inclination angle at 45.
Aforesaid gas solid separation is also divided equally in the device of solid, and described separator 1 is provided with inspection socket 16, and inspection socket 16 places are provided with cover plate 17, and cover plate 17 is provided with handle 18.
Compared with prior art, gas solid separation provided by the present invention is also divided equally the method and the device of solid, and floor space is little, the cost cost is low, and has separative efficiency height, good separating effect, in the gas after the separation, granular material content is low, can alleviate the load of dust pelletizing system.And the granular material automatic average break into portions after separating can be helped storing, also be convenient to carrying out smoothly of postorder production technology.
Description of drawings
Accompanying drawing 1 is a structural representation of the present invention;
Accompanying drawing 2 is front views of the present invention.
Being labeled as in the accompanying drawing: 1-separator, 2-part flow arrangement, 3-separating barrel, 4-separation off gas mouth, 5-baffle plate, 6-charging aperture, 7-shunts bucket, 8-bottom, 9-canvas, the 10-porous plate, 11-separation panel gas port, 12-discharging opening, 13-high pressure air inlet, 14-spoiler, 15-shaped steel, the 16-inspection socket, 17-cover plate, 18-handle.
The specific embodiment
Embodiment: the gas solid separation of the present invention and the method for dividing equally solid as depicted in figs. 1 and 2 shown in.Method of the present invention is that the gases at high pressure pipeline of conveying powder material is connected with charging aperture 6 on the device of the present invention, in order to improve separative efficiency, charging aperture 6 can be established a plurality of, in the separating barrel 3 relative, be provided with and baffle plates 5 that 3 one-tenth 45 degree of charging aperture tilt with charging aperture 6, the air-flow band granular material and is impinged upon on the baffle plate 5, because 5 one-tenth 45 degree of baffle plate are obliquely installed, behind the granular material impingement baffles 5, on the canvas 9 of direction change in falling into the part flow arrangement that is located at separator 1 below, gas pressure after the gas solid separation reduces, pass from the gap of two or more baffle plates, enter dust pelletizing system from the separation off gas mouth 4 that is located at separating barrel 3 tops, portion gas may enter part flow arrangement 2 with granular material, also can enter dust pelletizing system from the separation panel gas port 11 that is located on the part flow arrangement 2.After granular material enters part flow arrangement, be deposited on the canvas 9, for granular material is shakeout, be convenient to from the average outflow of different discharging opening 12, below canvas, be provided with high pressure admission mouth 13, gases at high pressure blow to canvas 9 from the below makes the granular material on the canvas 9 be in the state that seethes that does not stop, the plane of granular material keeps level, equal height on shunting bucket 7 sidewalls of part flow arrangement 2 is provided with a plurality of discharging openings 12, and the umber that can be divided into is as required opened the discharging opening 12 of required umber, as needs granular material is divided into two parts, can open two discharging openings 12, be divided into five parts, can open 5 discharging openings 5 as needs.Because granular material is under the effect of gases at high pressure, remaining is to be in flat state, so the granular material deal that different discharging openings 12 flows out is identical.For high pressure draught is impacted canvas uniformly, 13 places are provided with spoiler 14 at the high pressure air inlet, are provided with porous plate 10 below under the canvas 9, can make air-flow even on the one hand, the plane parallel that also prevents air-flow and canvas 9 on the one hand flows, and can strengthen the impact dynamics of air-flow.Porous plate 10 also can be played a supporting role to canvas 9 simultaneously.The gases at high pressure that see through canvas 9 are discharged from the separation panel gas port 11 that is located on the part flow arrangement, enter dust pelletizing system.Discharging opening 12 also has portion gas also can flow out with granular material from discharging opening 12 except granular material flows out, but that pressure has fallen is very low, can not impact to next stage equipment.For the ease of the inside of separator is overhauled and is cleared up, on separator, also be provided with inspection socket 16, inspection socket 16 is provided with cover plate 17, during operate as normal, cover plate 17 is fixed by bolts on the inspection socket 16, and inspection socket 16 is blocked, and opens cover plate 17 when needing maintenance or cleaning, for the ease of operation, on cover plate 17, be provided with handle 18.
Gas solid separation of the present invention is also divided equally the device of solid, as depicted in figs. 1 and 2.It is by being made of separator 1 and part flow arrangement 2 two parts; The below of separator 1 is connected with part flow arrangement 2; Separator 1 comprises separating barrel 3, and separating barrel 3 is provided with separation off gas mouth 4, is provided with two baffle plates 5 that tilt to install in the separating barrel 3, and baffle plate 5 is connected with the separating barrel wall through shaped steel 15, and the shaped steel 15 of present embodiment is the channel-section steel that adopts, also available angle steel.Baffle plate 5 is provided with feedstock direction inclination angle at 45.Separating barrel 3 walls relative with baffle plate 5 are provided with two charging apertures 6; Part flow arrangement 2 comprises shunting bucket 7 and bottom 8, divides comb bucket 7 bottoms to be connected with bottom 8, accompanies canvas 9 and porous plate 10 in the junction; Shunting bucket 7 is provided with separation panel gas port 11, divides the sidewall equal height of comb bucket 7 to be provided with six discharging openings 12; The bottom of bottom 8 is provided with high pressure air inlet 13, and high pressure air inlet 13 places are provided with spoiler 14.Separator 1 is provided with inspection socket 16, and inspection socket 16 places are provided with cover plate 17, and during operate as normal, cover plate 17 usefulness bolts are blocked inspection socket 16, when maintenance or cleaning separator, takes off cover plate 17, and cover plate 17 is provided with handle 18 with handled easily.
Claims (6)
1. a gas solid separation and the method for dividing equally solid, it is characterized in that: this method is that the mist that will contain powdery solid is blown into separator through charging aperture, be provided with the baffle plate of inclination in the separator, change the direction of motion behind the powdery solid impingement baffles, fall on the canvas in the part flow arrangement, the separation off gas mouth of the gas after the gas solid separation on separator is connected with dust pelletizing system; Be provided with the high pressure air inlet below canvas, the gap that high pressure draught sees through canvas is seethed powdery solid and is shakeout, and the high pressure draught that sees through the canvas gap is connected with dust pelletizing system from the separation panel gas port on the part flow arrangement; Bucket wall equal height at part flow arrangement is provided with two or more discharging openings, and when the height of powdery solid accumulation surpassed discharging opening, solid particle on average overflowed from different discharging openings simultaneously.
2. gas solid separation according to claim 1 and the method for dividing equally solid is characterized in that: the place is provided with spoiler at described high pressure air inlet, makes high pressure draught act on the canvas bottom uniformly; The canvas below is provided with porous plate, and high pressure draught is avoided along the canvas PARALLEL FLOW, strengthens the impact dynamics of air-flow, also canvas is played a supporting role simultaneously.
3. gas solid separation according to claim 1 and the method for dividing equally solid is characterized in that: be provided with inspection socket on described separator, be convenient to separator inside is overhauled or cleared up.
4. a gas solid separation and divide equally the device of solid, it is characterized in that: it is made of separator (1) and part flow arrangement (2) two parts; The below of separator (1) is connected with part flow arrangement (2); Separator (1) comprises separating barrel (3), separating barrel (3) is provided with separation off gas mouth (4), be provided with one or the baffle plate (5) to tilt and to install in the separating barrel (3), separating barrel (3) wall relative with baffle plate (5) is provided with one or more charging aperture (6); Part flow arrangement (2) comprises shunting bucket (7) and bottom (8), divides comb bucket (7) bottom to be connected with bottom (8), accompanies canvas (9) and porous plate (10) in the junction; Shunting bucket (7) is provided with separation panel gas port (11), divides the sidewall equal height of comb bucket (7) to be provided with two or more discharging openings (12); The bottom of bottom (8) is provided with high pressure air inlet (13), and high pressure air inlet (13) locates to be provided with spoiler (14).
5. gas solid separation according to claim 4 is also divided equally the device of solid, and it is characterized in that: described baffle plate (5) is connected with separating barrel (3) wall through shaped steel (15), and baffle plate (5) is provided with feedstock direction inclination angle at 45.
6. gas solid separation according to claim 4 is also divided equally the device of solid, and it is characterized in that: described separator (1) is provided with inspection socket (16), and inspection socket (16) locates to be provided with cover plate (17), and cover plate (17) is provided with handle (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008103012325A CN101564623B (en) | 2008-04-22 | 2008-04-22 | Method and device for separating gas from solid and sharing solid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008103012325A CN101564623B (en) | 2008-04-22 | 2008-04-22 | Method and device for separating gas from solid and sharing solid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101564623A true CN101564623A (en) | 2009-10-28 |
| CN101564623B CN101564623B (en) | 2012-07-04 |
Family
ID=41281096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008103012325A Expired - Fee Related CN101564623B (en) | 2008-04-22 | 2008-04-22 | Method and device for separating gas from solid and sharing solid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101564623B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101773754A (en) * | 2010-03-26 | 2010-07-14 | 贵阳铝镁设计研究院 | Bag-type dust remover for dry purifying system |
| CN101721934B (en) * | 2009-12-31 | 2012-09-05 | 哈尔滨工业大学 | Combined block type gas-solid mixing strengthening device |
| CN106268515A (en) * | 2016-08-09 | 2017-01-04 | 新奥科技发展有限公司 | Segregation apparatus and there is the supercritical reaction system of this segregation apparatus |
| CN111714933A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Overpressure relief device for reducing material splashing of multiphase reactor and multiphase reaction system |
| CN111714934A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Overpressure relief device for reducing gas-liquid entrainment phenomenon and multiphase reaction system |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1052641A (en) * | 1991-01-24 | 1991-07-03 | 机械电子工业部兰州石油机械研究所 | A kind of gas and dust separating device |
| CN200998629Y (en) * | 2007-01-08 | 2008-01-02 | 陈美青 | Preprocessing device of the dust wiper |
| CN100592931C (en) * | 2007-05-11 | 2010-03-03 | 贵阳铝镁设计研究院 | Gas and solid separating method and device for gas transporting material system |
| CN201189425Y (en) * | 2008-04-22 | 2009-02-04 | 贵阳铝镁设计研究院 | Gas-solid separating and solid equal-division device |
-
2008
- 2008-04-22 CN CN2008103012325A patent/CN101564623B/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101721934B (en) * | 2009-12-31 | 2012-09-05 | 哈尔滨工业大学 | Combined block type gas-solid mixing strengthening device |
| CN101773754A (en) * | 2010-03-26 | 2010-07-14 | 贵阳铝镁设计研究院 | Bag-type dust remover for dry purifying system |
| CN106268515A (en) * | 2016-08-09 | 2017-01-04 | 新奥科技发展有限公司 | Segregation apparatus and there is the supercritical reaction system of this segregation apparatus |
| CN106268515B (en) * | 2016-08-09 | 2019-08-13 | 新奥环保技术有限公司 | Separator and supercritical reaction system with the separator |
| CN111714933A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Overpressure relief device for reducing material splashing of multiphase reactor and multiphase reaction system |
| CN111714934A (en) * | 2019-03-22 | 2020-09-29 | 中国石油化工股份有限公司 | Overpressure relief device for reducing gas-liquid entrainment phenomenon and multiphase reaction system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101564623B (en) | 2012-07-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101564623B (en) | Method and device for separating gas from solid and sharing solid | |
| CN2628165Y (en) | Compound dry coal dressing apparatus | |
| AU2010352883B2 (en) | Apparatus for pneumatic vacuum separation of bulk materials | |
| CN201357018Y (en) | Low resistance inertial dust separator | |
| EP2390208A1 (en) | Hopper assembly | |
| CN100592931C (en) | Gas and solid separating method and device for gas transporting material system | |
| US5108471A (en) | Single mode wet and dry vacuum vehicle | |
| CN201189425Y (en) | Gas-solid separating and solid equal-division device | |
| CN201337869Y (en) | Dust removal unit for urea cooling fluidized bed | |
| CN201950028U (en) | Impurity-removing and warehouse-entering system for raw material | |
| CN101912844A (en) | Domestic waste winnowing method and winnowing device | |
| CN110585806A (en) | Boundary separation dust collecting equipment | |
| CN1024907C (en) | Recovery separator for powder spray | |
| CN211585624U (en) | Novel fish feed processing is with removing dust device | |
| CN210786530U (en) | Boundary separation dust collecting equipment | |
| CN111960126A (en) | Environment-friendly storage bin | |
| CN2578281Y (en) | Combined segregator for pneuamtic bulk material conveying | |
| CN201552069U (en) | Cyclone separator for manufacturing spherical graphite | |
| CN213965563U (en) | High-efficiency dust remover | |
| CN216171045U (en) | Dust remover with pre-separation function | |
| CN218089481U (en) | White spirit powder yeast production system | |
| CN217410098U (en) | Metal powder dust collector | |
| CN212757918U (en) | Flue gas dust removal and purification device | |
| CN216678619U (en) | Aluminum ash and aluminum extraction separation system | |
| CN216368591U (en) | Sedimentation separator for target spraying equipment and target spraying equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| ASS | Succession or assignment of patent right |
Owner name: GUIYANG ALUMINUM AND MAGNESIUM DESIGN INSTITUTE CO Free format text: FORMER OWNER: GUIYANG ALUMINIUM AND MAGNESIUM DESIGN INST. Effective date: 20110609 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 550004 NO. 208, BEIJING ROAD, GUIYANG CITY, GUIZHOU PROVINCE TO: 550081 NO. 2, JINZHU ROAD, JINYANG NEW DISTRICT, GUIYANG CITY, GUIZHOU PROVINCE |
|
| TA01 | Transfer of patent application right |
Effective date of registration: 20110609 Address after: 550081 Guiyang Province, Jinyang New District, Zhu Zhu Road, No. 2 Applicant after: Guiyang Aluminum & Magnesium Design Institute Co., Ltd. Address before: 550004 No. 208, Beijing Road, Guiyang, Guizhou Applicant before: Guiyang Aluminium and Magnesium Design Inst. |
|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120704 Termination date: 20160422 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |