专利摘要:
An apparatus for separating dust, dirt and the like from particulate material utilizes a flow of carrier fluid which passes through the particulate material on a grid or screen. The heavier particulate material falls through the grid while the lighter material as well as the dust, dirt and the like are entrained in the fluid and carried upwardly. A portion of the entrained material precipitates out of the carrier fluid into a vertical collecting bin whereupon it is discharged into another flow of carrier fluid. A sensor within the collecting bin senses the level of the collected precipitated material and reduces the velocity of the carrier fluid when the material in the collecting bin exceeds a predetermined level.
公开号:SU1063287A3
申请号:SU813235851
申请日:1981-01-29
公开日:1983-12-23
发明作者:Шмидт Виллибальд
申请人:Villibald Shmidt;
IPC主号:
专利说明:

(Y)
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2. The device according to claim 1, which is based on the fact that the device is equipped with valves installed at the outlet of the loading hopper and at the outlet of the collecting tank,
Zch / device according to claim 1, of which the side wall of the collecting tank is installed
 with the possibility of vertical movement.
4. Device POP.1, distinguished by the fact that the device is equipped with a centrifugal pneumatic dust collector connected to the ventilation openings by means of nozzles.
The invention relates to a device for separating bulk & jpoB materials by specific gravity. . A device for separating bulk materials is known, which includes a grate, a pneumo-separation channel, an air supply device, loading and unloading devices 1. A disadvantage of this device is the low efficiency of the separation process. The closest to the invention by technical essence and the achieved result is a device for separating particles by specific gravity, including a grate located in the casing, a feed hopper mounted on the edge of the grate, a vertical air separator and an air supply unit for the air under the grate with C2J nozzles. A disadvantage of the known device is the low quality of the separation process. The purpose of the invention is to improve the quality of the separation process. The goal is achieved by the fact that a device for separating particles by specific gravity, including a grate located in the casing, a hopper mounted on the edge of the grate, a vertical air separator and ventilation units for air supply under the grate with nozzles, is worn on the edge of the grate, opposite to the loading hopper is a collection tank with a filling degree sensor and with an outlet opening which is in communication with the pneumatic separator. At the same time, the device is equipped with a rod with valves installed at the outlet of the loading hopper and at the outlet of the collecting tank. The side wall of the collecting container is installed with the possibility of vertical movement. In addition, the device is equipped with an centrifugal pneumatic dust collector connected to the ventilation installations by means of nozzles. FIG. Figure 1 shows the proposed device (General View; Fig. 2 - section A-A in Fig. 1. A device for separating particles by specific weight comprises a housing 1 with a hopper 2, a distribution capacity 3 and a grid 4. At the lower end A supply valve 5 is provided to the distribution tank 3. A screening-kada surface 6 is installed under the grid 4. At the edge of the grid 4 opposite to the loading core 2, a collection container 7 is installed, at the lower end of which there is a supply valve 8, the valves 5 and 8 are connected between each other 9. For; team capacity of 7 a pneumatic separator 10 is located. In the view above the grill 4 there are control valves 11 and 12, between which there is a partition 13, which changes: the direction of air flow. The pneumatic separator 10 is closed by a control valve 14. Behind the control, valves 11, 12 and 14 and the direction of the air the flow is a fixture .15 for separating the lighter particles, in which a burnout is installed. An ledge 16, which directs the airflow, carries lighter particles and dust, and a screw 17 for removing light particles. Behind the device 15, a centrifugal pneumatic binder 18 / is installed relative to the inner side of the wall of which a nozzle 19 is installed. The latter is connected to a ventilation unit 20. The centrifugal pneumatic dust collector 18 is serviced by two ventilation units 21 and 22, which are installed in The engines 23 and 24, installed on both sides of the casing 1, are connected to the grinding units 21 and 22 by means of nozzles 25 and 26, forming a closed air system. A regulating valve 27 is installed in the pipe 25, a regulating valve 28 is installed in the pipe 28.- 28. A filling sensor 29 is installed in the collecting tank 7, and an outlet 30 is connected, which communicates with the pneumatic sampler 10. The side wall of the 31 collecting tank 7 possibility of vertical movement. The device works as follows. Particles from the hopper 2 are fed to the inclined grid 4, where they are sieved by an air stream passing upwards. Heavier particles sink through the grate down to the screening surface 6. The lighter particles and dust are trapped by the air stream upwards. Since the grating.4 is installed obliquely, the bulk materials sweep, which results in the uptake of heavier particles by upward flow, especially with a large supply of bulk materials. These heavier particles, trapped upward by the air flow, together with the overwhelming amount of the part, related in their weight to the boundary region, fall into collection tank 7, which is mounted above the lower end of the lattice. The restricting wall 31 of the collection tank 7, facing the pit valve 5, can be installed at different heights, which roughly regulates the proportion of bulk materials entering the collection tank 7, which depends there the bulk material falls into the vertical pneumo. : separator 1-0, through which from below: part of the air flow goes upwards. At the lower end of the collection container 7, there is a supply gate 8, which defines a cross-sectional area that permits free-flowing from the collection container 7 to the pneumatic separator 10-. The light particles from the pneumatic separator 10 fall into the device 15 to remove the light particles, where they are deposited and removed by the screw 7.,; The fill level sensor 29 installed in the collection container 7 outputs a signal corresponding to the position of the level in the collection container 7. This signal controls the airflow through the grill 4. For example, the signal is sent to a frequency regulator that adjusts the frequency and, therefore, the number of revolutions of the engine, which causes the fan 20 to rotate. In this case, the regulation occurs in such a way that the number of revolutions of the Fan 20 decreases with increasing filling level of the collecting tank 7. When the filling level in the collecting tank 7 is lowered, therefore, it increases by the number of a fan 20. The air-borne note, passing from the bottom up to the worm 4, increases the level of Kjiti, like loosening of the bulk material. The feed dampers 5 and 8 serve to coordinate the delivery of the material to the grid 4 through the distribution tank 3 to supply it to the pneumatic separator 10, in order to be able to control the number of particles that fall into the collection tank, the latter has a side wall that faces - Vertical movement. For installation, adjustment and adjustment of the air flow between them, control valves are installed behind the grille and pneumatic separator, in the direction of the air flow, to regulate the cross-sectional area of the air flow pass. The use of the proposed unit for the separation of particles by specific gravity will improve the quality of separation.
2
21
fig 2
-22
权利要求:
Claims (4)
[1]
1. DEVICE FOR SEPARATION OF PARTICLES BY SEPARATE WEIGHT, including a grate, located on the casing), a loading hopper mounted on the edge of the grate, vertical air : separator and ventilation units for supplying air under the grate with nozzles, © t la I mean, in order to improve the quality of the separation process, it provides., '.
wife installed on the edge of the grill, opposite / loading bun- / keru, a collection tank with a fill level sensor and with an outlet that is in communication with the air separator.
[2]
2. The device according to π. 1, characterized in that the device is equipped with a draft with shutters installed at the outlet of the loading hopper and at the outlet of • c6op J capacity.
[3]
3 · “‘ The device according to claim 1, wherein the side wall of the collecting tank is mounted ’with the possibility of vertical movement.
[4]
4. The device according to claim 1, with the proviso that the device is equipped with a centrifugal pneumatic dust collector connected to the ventilation units by means of nozzles.
device
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同族专利:
公开号 | 公开日
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GB2067925B|1983-06-02|
FR2474353A1|1981-07-31|
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引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题
RU2747997C1|2018-04-27|2021-05-18|Бюлер Гмбх|Automatic intake adjustment|US372015A|1887-10-25|Chop grader and purifier |
US482424A|1892-09-13|Fuel-feeder |
US250983A|1881-12-13|Machine for separating ores |
CA624488A|1961-07-25|R. Macpherson Arthur|Classification of particulate material|
US616189A|1898-12-20|Separating-machine |
US490285A|1893-01-24|hig-ginbottom|
US21945A|1858-11-02|Ghaut-separator |
US556148A|1896-03-10|higginbottom |
US850959A|1906-10-08|1907-04-23|Richard Och|Middlings-purifier.|
US1517596A|1922-04-08|1924-12-02|Albert H Stebbins|Pneumatic sizer|
US1597261A|1922-11-29|1926-08-24|Bishop John Frederick|Grain, fibrous, and other material purifying machine|
US1801195A|1927-10-31|1931-04-14|Hydrotator Company|Process of and apparatus for separating mixed materials|
US2001331A|1929-12-07|1935-05-14|Peale Davis Company|Process and mechanism for separating intermixed divided materials|
US2000472A|1934-02-23|1935-05-07|James A Muzzio|Egg separator|
US2477935A|1944-11-24|1949-08-02|Keighley Lab Ltd|Combined screening and air separation of pulverulent material|
GB677103A|1950-04-03|1952-08-06|Simon Ltd Henry|Improvements in aspirators for cereal products|
AT172223B|1950-06-02|1952-08-25|Andreas Dipl Ing Deller|Method and device for cleaning and sorting seed grain and other granular material|
US2713942A|1950-07-26|1955-07-26|Kalker Trieurfabrik Fabr|Apparatus for classifying and cleaning a granular material|
US2952357A|1955-11-03|1960-09-13|Union Oil Co|Solids elutriation apparatus|
US2968399A|1956-10-31|1961-01-17|Linde Maskiner Ab|Machine for cleaning grain, seed and the like|
US3061096A|1960-09-19|1962-10-30|Roy E Wyer|Automatic sifter and fan control means for combines|
DE1167635B|1960-12-20|1964-04-09|Happle U Sohn K G Maschinenfab|Device for cleaning and sorting grain, seeds or the like.|
FR1327882A|1962-04-12|1963-05-24|Tripette & Renaud|Improvements to grain cleaners by ventilation|
US3255882A|1962-10-15|1966-06-14|Duval Sulphur & Potash Company|Flotation froth level control|
GB1011207A|1963-09-27|1965-11-24|Collectron Ltd|Improvements in or relating to apparatus for separating solid particles of differentsizes|
US3348676A|1964-08-05|1967-10-24|Int Harvester Co|Rotary cleaning unit|
US3349912A|1964-10-12|1967-10-31|Head Wrightson & Co Ltd|Fluidized bed separator|
DE1932312A1|1969-06-26|1971-01-21|Hauni Werke Koerber & Co Kg|Device for pneumatic sifting out of tobacco stems from a mixture of tobacco leaf parts and tobacco stems|
US4178232A|1976-03-24|1979-12-11|Cargill, Incorporated|Apparatus for separating solid materials|
DE2748336A1|1977-10-28|1979-05-03|Heinz Jaeger|CIRCULATION SEVER|SE446158B|1981-12-10|1986-08-18|Kamas Ind Ab|DEVICE FOR MACHINES FOR SEPARATION OF MATERIALS WITH DIFFERENT AERODYNAMIC PROPERTIES|
SE430386B|1982-03-03|1983-11-14|Kamas Ind Ab|CONTROL DEVICE FOR SORTING AND CLEANING MACHINES WITH A SALL|
DE3321326C2|1983-06-13|1987-11-26|Paul 8100 Garmisch-Partenkirchen De Freisl|
US4646759A|1984-01-06|1987-03-03|Philip Morris Incorporated|Vibrating trough tobacco separator and classifier|
DE3410573C2|1984-03-22|1986-03-13|Gebrüder Bühler AG, Uzwil|Device for cleaning semolina|
DE3706134C2|1987-02-26|1988-12-29|Maschinenfabrik G.W. Barth Ludwigsburg Gmbh & Co, 7140 Ludwigsburg, De|
US4991721A|1988-08-15|1991-02-12|Iowa State University Research Foundation, Inc.|Automation of an air-screen seed cleaner|
DE4118675A1|1991-06-07|1992-12-10|Lindemann Maschfab Gmbh|AIR SUPPORTED SEPARATOR|
DE19506059A1|1995-02-22|1996-08-29|Deere & Co|Method for automatically regulating at least a portion of the crop processing in a harvesting machine|
DE19606890A1|1996-02-23|1997-08-28|Peter Sendrowski|Separation of plastic containers from nonplastic culture medium and cylindrical process chamber|
US20040106366A1|2002-08-26|2004-06-03|Robinson Robert A.|Portable pipe restoration system|
US20060085212A1|2004-08-10|2006-04-20|Kenny Garry R|Optimization of a materials recycling facility|
US7008304B1|2004-08-17|2006-03-07|Media Blast & Abrasives, Inc.|Abrasive and dust separator|
US20060037293A1|2004-08-17|2006-02-23|Storer Ron D|Blast medium pot|
US20070202781A1|2006-02-28|2007-08-30|Media Blast & Abrasives, Inc.|Blast media nozzle and nozzle assembly|
JP5446037B2|2009-06-01|2014-03-19|株式会社サタケ|Purifier|
RU2460592C2|2010-10-07|2012-09-10|Государственное научное учреждение Зональный научно-исследовательский институт сельского хозяйства Северо-Востока имени Н.В. Рудницкого Российской академии сельскохозяйственных наук|Pneumatic separation device of grain and seed-cleaning machine|
EP2704858B1|2011-05-03|2019-02-20|Bühler AG|Device and method for separating feedstock into at least one light material fraction and a heavy material fraction|
RU2497605C2|2012-02-07|2013-11-10|Виктор Федорович Веденьев|Air separator|
RU2513391C2|2012-02-09|2014-04-20|Федеральное государственное унитарное предприятие Проектно-конструкторское бюро НИИСХ Северо-Востока Российской академии сельскохозяйственных наук|Machine for fractionation and purification from impurities of grain material|
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US9623539B2|2014-07-07|2017-04-18|Media Blast & Abrasive, Inc.|Carving cabinet having protective carving barrier|
RU2622052C1|2016-04-15|2017-06-09|Федеральное государственное бюджетное научное учреждение "Федеральный научный агроинженерный центр ВИМ" |Gravitationally-pneumatic grain-treating machine|
RU2654985C1|2017-02-27|2018-05-23|Федеральное государственное бюджетное научное учреждение "Федеральный аграрный научный центр Северо-Востока имени Н.В. Рудницкого" |Fractional pneumatic separator|
RU2670155C1|2017-06-26|2018-10-18|Алексей Андреевич Орлов|Air-cleaning system of grain separator|
RU2737927C1|2020-03-04|2020-12-04|Общество с ограниченной ответственностью Научно-производственная фирма "Агромаш"|Pneumatic separating system of grain cleaning machine|
RU2743367C1|2020-06-01|2021-02-17|Общество с ограниченной ответственностью Научно-производственная фирма "Агромаш"|Sieve part of grain cleaning machine|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE19803003308|DE3003308C1|1980-01-30|1980-01-30|Device for separating heavier grains of a bulk material from lighter grains and dust|
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