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US3972816A Expired / Lapsed US ⏱️ 0.0 years remaining

Oil extractor

Assignee: Change Inc
•
Filing: 1974-08-23
•
Granted: 1976-08-03
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Expires: 1994-08-23
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Abstract

Abstract Method and means for separating emulsified and entrained oils from water, machine coolants, and substantially any other liquid comprising initially directing a flow stream into an inlet trap for removing relatively large particles from the flow stream, passing the flow stream through a centrifuge for removing substantially all of the entrained solids in the flow stream, moving the flow stream through a de-emulsifier for coalescing of the emulsified oil into droplets sufficiently large for processing in a separator and for filtering any remaining solids from the flow stream, providing a backwash action from the de-emulsifier for recycling of said finally removed solids through the centrifuge, passing the flow stream through a separator for separation of the oil from the other liquid components of the flow stream whereby the separated oil and clean effluent may be removed from the system. The de-emulsifier comprises a chamber containing a bulk dense granular material, preferably water wettable, and the flow stream is directed into the chamber in a downflowing manner through the granular material for mechanically breaking the emulsion into two phases and separating the solids therefrom. The separator comprises a centrally disposed entrance or spreader tube discharging the flow stream radially outwardly through a body of granular media contained within a cylindrical housing concentrically disposed with respect to the entrance tube. The oil and water, or other liquid, are separated during passage of the flow stream through the granular media whereby the oil percolates upwardly through a water reservoir for collection in a collector, and the water or other liquid flows downwardly by gravity for discharge through a suitable valve.

Inventors

  • 👤 Paul Mail
  • 👤 Charles R. Ferrin
  • 👤 Richard J. Ely

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 23:15
CPC Classifications
B; B01; B01D; B01D17/00; B01D17/02; B01D17/04; B01D17/045; B01D17/08; Y; Y10; Y10S; Y10S210/00; Y10S210/05

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 213 words
An apparatus for extracting solids and oil from an effluent and comprising filter trap means for initially receiving the effluent therethrough, centrifuge means in communication with the filter trap for receiving the filtered effluent therefrom and separating the effluent into lighter and heavier components, de-emulsifier means in communication with the centrifuge means for receiving the lighter components therefrom, said de-emulsifier being provided with a granular bed for filtering the effluent and to create a mixture having two distinctive phases, said de-emulsifier means including a housing to receive said effluent means to pass said effluent downwardly through said granular bed, horizontal tray means provided in said housing upon which said granular bed rests, vertical and central riser tube means through said granular bed and housing which is in open communication with said tray means to discharge said two phase mixture, and backwash means to clear said granular bed, separator means in communication with the de-emulsifier means for receiving the two phase mixture therefrom, removable granular filled cartridge means provided in said separator means for receiving the two phase mixture therein, means provided in said cartridge means for flowing said mixture radially outward therethrough thereby separating the two phases of the mixture, and means for independent discharge of the two separated phases from the separator.
Claim 2
Independent Claim 213 words
An apparatus for extracting solids and oil from an effluent and comprising filter trap means for initially receiving the effluent therethrough, centrifuge means in communication with the filter trap for receiving the filtered effluent therefrom and separating the effluent into lighter and heavier components, de-emulsifier means in communication with the centrifuge means for receiving the lighter components therefrom, said de-emulsifier being provided with a granular bed for filtering the effluent and to create a mixture having two distinctive phases, said de-emulsifier means including a housing to receive said effluent means to pass said effluent downwardly through said granular bed, horizontal tray means provided in said housing upon which said granular bed rests, vertical and central riser tube means through said granular bed and housing which is in open communication with said tray means to discharge said two phase mixture, and backwash means to clear said granular bed, separator means in communication with the de-emulsifier means for receiving the two phase mixture therefrom, removable granular filled cartridge means provided in said separator means for receiving the two phase mixture therein, means provided in said cartridge means for flowing said mixture radially outward therethrough thereby separating the two phases of the mixture, and means for independent discharge of the two separated phases from the separator.
Claim 3
Dependent Claim 31 words
In an apparatus for extracing oil from an effluent, de-emulsifier means as set forth in claim 1 wherein the granular bed comprises a body of water wettable granules of preselected sizes.

References Cited (Backward Citations)

US3178024A Cited
US3444077A Cited
US3381823A Cited
US3471401A Cited
US3491882A Cited
US3853753A Cited
US3764008A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-03 1980-02-02 1980-08-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-03 1984-02-02 1984-08-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-03 1988-02-02 1988-08-03 $7700.00 Window Closed / Lapsed

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