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US4133749A Expired / Lapsed US ⏱️ 0.0 years remaining

Process of separating solid granular metallurgical products and their precursors and apparatus

Assignee: GEA Group AG
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Filing: 1977-02-28
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Granted: 1979-01-09
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Expires: 1997-02-28
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Abstract

Abstract A process and apparatus for separating solid granular metallurgical products. A plurality of linearly vibrating screens are housed, one over the other, each inclining more than the one above and each having a smaller mesh opening than the one above and 1.5 to 15 times larger than the desired parting size. The solids are fed onto the uppermost screen at the upper end thereof and are deflected in the direction of inclination of the screen. The finer solids initially fall through freely and on screens having smaller mesh openings and are also deflected in the direction of inclination of the screen. The coarsest solids fraction is withdrawn as overflow from the uppermost screen, finer solids fractions are withdrawn as overflow from following screens, and solids which have passed through all screens are withdrawn as a finest fraction. A gaseous fluid is flowed through at least part of the working space required for screening approximately transversely to the direction in which the solids pass through the screens. The solids having a lower specific gravity are entrained between vertically adjacent screens by the gaseous flow and gaseous fluid laden with the solids of lower specific gravity flow into a separating chamber with the solids being separated from the gas stream in the separating chamber.

Inventors

  • 👤 Horst Jelinek
  • 👤 Gerd Elsenheimer
  • 👤 Bernhard Klersy

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 23:12
CPC Classifications
B; B07; B07B; B07B4/00; B07B4/08

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 373 words
In a process of separating solid granular metallurgical products and their precursors by providing a plurality of linearly vibrating inclined screens spatially arranged one over the other, in a housing, each screen having an inclination greater than that of the screen above and wherein the width of the mesh openings in each screen is less than that of the screen above and the width of the mesh openings of each screen is 1.5 to 15 times larger than the desired parting size, and feeding the solids to be separated onto the uppermost screen at the upper end of said housing, the coarser solids being deflected in the direction of inclination of said uppermost screen, the finer solids initially falling through freely and onto lower screens having smaller mesh openings being deflected also in the direction of inclination of said lower screens, the coarsest solids fraction being withdrawn as overflow from said uppermost screen, finer solids fractions being withdrawn as overflow from following screens, and solids which have passed through all screens being withdrawn as a finest fraction, the improvement which comprises flowing a gaseous fluid through at least part of the working space required for screening in a direction approximately transverse to the direction in which said solids pass through said screens at a rate and in an amount to effect entrainment of those solids having a lower specific gravity between successive adjacent screens by said gaseous fluid flowing through said working space and to effect the resulting gaseous fluid laden with said solids of lower specific gravity to flow into a separating chamber, and separating at least the coarser of said solids of lower specific gravity from the flowing gaseous fluid in said separating chamber, wherein said separating step includes providing a separating plate in the separating chamber which is rearwardly and upwardly inclined and has a forward edge extendible generally parallel to the level of each of said screens, separating said coarser solids on said plate by sliding same down on said plate and withdrawing same through a discharge opening from the lower portions of said separating chamber, and withdrawing said gaseous fluid and the finer solids entrained thereby upwardly behind said plate through the upper portions of said separating chamber.
Claim 2
Dependent Claim 373 words
In a process of separating solid granular metallurgical products and their precursors by providing a plurality of linearly vibrating inclined screens spatially arranged one over the other, in a housing, each screen having an inclination greater than that of the screen above and wherein the width of the mesh openings in each screen is less than that of the screen above and the width of the mesh openings of each screen is 1.5 to 15 times larger than the desired parting size, and feeding the solids to be separated onto the uppermost screen at the upper end of said housing, the coarser solids being deflected in the direction of inclination of said uppermost screen, the finer solids initially falling through freely and onto lower screens having smaller mesh openings being deflected also in the direction of inclination of said lower screens, the coarsest solids fraction being withdrawn as overflow from said uppermost screen, finer solids fractions being withdrawn as overflow from following screens, and solids which have passed through all screens being withdrawn as a finest fraction, the improvement which comprises flowing a gaseous fluid through at least part of the working space required for screening in a direction approximately transverse to the direction in which said solids pass through said screens at a rate and in an amount to effect entrainment of those solids having a lower specific gravity between successive adjacent screens by said gaseous fluid flowing through said working space and to effect the resulting gaseous fluid laden with said solids of lower specific gravity to flow into a separating chamber, and separating at least the coarser of said solids of lower specific gravity from the flowing gaseous fluid in said separating chamber, wherein said separating step includes providing a separating plate in the separating chamber which is rearwardly and upwardly inclined and has a forward edge extendible generally parallel to the level of each of said screens, separating said coarser solids on said plate by sliding same down on said plate and withdrawing same through a discharge opening from the lower portions of said separating chamber, and withdrawing said gaseous fluid and the finer solids entrained thereby upwardly behind said plate through the upper portions of said separating chamber.
Claim 3
Dependent Claim 40 words
A process according to claim 1, wherein the separating step includes separating the coarser solids of those contained in the flowing gaseous fluid in said separating chamber with the finer solids entrained by said gaseous fluid leaving said separating chamber.
Claim 4
Dependent Claim 32 words
A process according to claim 1, further comprising selecting the parting size between said coarser and finer solids by adjusting at least one of the inclination or height of said separating plate.
Claim 5
Dependent Claim 86 words
A process according to claim 1, further comprising providing a flat separating plate in said separating chamber arranged spatially below said separating plate, said flat separating plate having a forward edge extendible generally parallel to each of said screens, deflecting the coarse solids of low specific gravity having passed through one or more of said screens out of the flowing gaseous liquid by impinging on said flat separating plate and sealing said discharge opening in said lower portion of said separating chamber from said separating chamber.
Claim 6
Dependent Claim 33 words
A process according to claim 4, further comprising selecting the parting size between said coarser and finer solids by adjusting at least one of the inclination or height of said flat separating plate.
Claim 7
Dependent Claim 23 words
A process according to claim 1, further comprising effecting separation by feeding additional gaseous fluid into said separating chamber at a controlled rate.
Claim 8
Dependent Claim 30 words
A process according to claim 1, further comprising causing said gaseous fluid to flow at different rates through the particle size fractions disposed in the working space between said screens.
Claim 9
Dependent Claim 58 words
A process according to claim 7, wherein the step of causing different flow rates comprises providing an enclosure preceding said housing, passing said gaseous fluid through said enclosure, and providing a plurality of dampers in said enclosure capable of adjusting the rate of flow of said gaseous fluid passing through said enclosure and through said particle size fractions.
Claim 10
Dependent Claim 12 words
A process according to claim 1, wherein said gaseous fluid comprises air.
Claim 11
Dependent Claim 14 words
A process according to claim 1, wherein said gaseous fluid comprises an inert gas.
Claim 12
Dependent Claim 31 words
A process according to claim 1, further comprising feeding said solids to be separated into said housing and directing said solids laterally with respect to the flow of said gaseous liquid.
Claim 13
Dependent Claim 327 words
In combination, an apparatus for separating solid granular metallurgical products and their precursors comprising a housing including a plurality of linearly vibrating inclined screens spatially arranged one over the other, wherein each screen has an inclination greater than that of the screen above and the size of the mesh openings in each screen is less than that of the screen above, means for feeding the solids to be separated into said housing and onto said screens whereby said solids pass through said screens in decreasing particle size, a separating chamber in flowing communication with said housing and comprising upper and lower separating plates disposed one above the other, said lower separating plate comprising a flat body, and a discharge opening in the upper and lower portion of said separating chamber, a source of gaseous fluid flowable through said housing between said screens transverse to the direction in which the particles pass through the screens and into said separating chamber to effect entrainment of those solids having a lower specific gravity between adjacent screens and the flowing thereof into said separating chamber, wherein said upper and lower separating plates are disposed rearwardly and upwardly inclined with respect to the gaseous flow and said upper separating plate has a forward edge extendible generally parallel to the level of each of said screens, the coarser solids having lower specific gravity being separable on said upper plate by sliding down said upper plate and being withdrawable through the discharge opening in the lower portion of said separating chamber, said gaseous fluid and the finer solids of lower specific gravity entrained thereby being withdrawable upwardly behind said upper plate through the upper portion of said chamber, the coarse solids of low specific gravity passing through one or more of said screens being impingeable on and deflectable by said lower plate out of said gaseous fluid, said lower plate being provided also with means for separating said discharge opening from said separating chamber.
Claim 14
Dependent Claim 327 words
In combination, an apparatus for separating solid granular metallurgical products and their precursors comprising a housing including a plurality of linearly vibrating inclined screens spatially arranged one over the other, wherein each screen has an inclination greater than that of the screen above and the size of the mesh openings in each screen is less than that of the screen above, means for feeding the solids to be separated into said housing and onto said screens whereby said solids pass through said screens in decreasing particle size, a separating chamber in flowing communication with said housing and comprising upper and lower separating plates disposed one above the other, said lower separating plate comprising a flat body, and a discharge opening in the upper and lower portion of said separating chamber, a source of gaseous fluid flowable through said housing between said screens transverse to the direction in which the particles pass through the screens and into said separating chamber to effect entrainment of those solids having a lower specific gravity between adjacent screens and the flowing thereof into said separating chamber, wherein said upper and lower separating plates are disposed rearwardly and upwardly inclined with respect to the gaseous flow and said upper separating plate has a forward edge extendible generally parallel to the level of each of said screens, the coarser solids having lower specific gravity being separable on said upper plate by sliding down said upper plate and being withdrawable through the discharge opening in the lower portion of said separating chamber, said gaseous fluid and the finer solids of lower specific gravity entrained thereby being withdrawable upwardly behind said upper plate through the upper portion of said chamber, the coarse solids of low specific gravity passing through one or more of said screens being impingeable on and deflectable by said lower plate out of said gaseous fluid, said lower plate being provided also with means for separating said discharge opening from said separating chamber.
Claim 15
Dependent Claim 35 words
An apparatus according to claim 12, further comprising means for adjusting the inclination and/or height of said upper and lower separating plates to effect selection of the parting size between said coarser and finer solids.
Claim 16
Dependent Claim 59 words
An apparatus according to claim 13, wherein an enclosure is provided preceding said housing, said gaseous fluid being passable through said enclosure, a plurality of dampers having means for adjusting the rate of flow of said gaseous fluid through said enclosure and through said solids entrained between said screens and into said separating chamber being provided in said enclosure.

References Cited (Backward Citations)

US1232947A Cited
US2041591A Cited
US2210103A Cited
US2354311A Cited
US2765079A Cited
US3044619A Cited
GB942995A Cited
DE2306412A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-01-08 1982-07-10 1983-01-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-01-08 1986-07-10 1987-01-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-01-08 1990-07-10 1991-01-09 $7700.00 Window Closed / Lapsed

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