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US4662990A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus for recovering dry solids from aqueous solids mixtures

Assignee: AMERICAN BIOTHERM COMPANY LLC
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Filing: 1985-10-23
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Granted: 1987-05-05
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Expires: 2005-10-23
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Abstract

Abstract A continuous process and apparatus for drying aqueous solids by evaporation using a fluidizing oil and a surfactant wherein the fluidizing oil and surfactant are recovered and recycled separately or together. The aqueous solids may, or may not, have a heavy, natural oil associated with them.

Inventors

  • 👤 Anthony J. Bonanno

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 22:46
CPC Classifications
B; B01; B01D; B01D1/00; B01D1/26; F; F26; F26B; F26B7/00; Y; Y10; Y10S; Y10S159/00; Y10S159/25; Y10S159/901; Y10S159/905; Y10S203/00; Y10S203/90

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 378 words
An apparatus for continuously dehydrating aqueous solids, said apparatus comprising: (1) a fluidizing tank disposed to receive a stream of aqueous solids and provided with a stirring or mixing mechanism; (2) a fluidizing oil source; (3) a surfactant source; (4) means for transmitting fluidizing oil from said fluidizing oil source to said fluidizing tank; (5) means for transmitting surfactant from said surfactant source to said fluidizing tank wherein fluidizing oil, aqueous solids and surfactant may be mixed; (6) an evaporator disposed to heat and dehydrate continuously a feed mixture of aqueous solids, fluidizing oil and surfactant and discharge water driven off therefrom as vapor; (7) a conduit extending from said fluidizing tank to said evaporator through which a mixture of aqueous solids, surfactant and fluidizing oil may flow from said tank into the evaporating region of said evaporator; (8) a screen bowl centrifuge disposed to wash and separate anhydrous solids from a mixture of substantially anhydrous solids, fluidizing oil and surfactant; (9) a conduit extending from said evaporator to said screen bowl centrifuge through which may flow a mixture of substantially anhydrous solids, fluidizing oil and surfactant from said evaporator to said centrifuge; (10) means for withdrawing anhydrous solids substantially free of fluidizing oil and surfactant from said centrifuge, and (11) means for withdrawing fluidizing oil and surfactant from said centrifuge and recycling the same to said fluidizing tank for mixing therein with new aqueous solids, that means comprising (i) a crystallizer for treating fluidizing oil and surfactant withdrawn together from said screen bowl centrifuge; (ii) means for conveying fluidizing oil and surfactant to said crystallizer from said screen bowl centrifuge; (iii) a centrifuge other than said screen bowl centrifuge disposed to separate crystallized surfactant from fluidizing oil; (iv) means for conveying a mixture of fluidizing oil and crystallized surfactant from said crystallizer to said other centrifuge; (v) means for recycling fluidizing oil withdrawn from said other centrifuge to said fluidizing tank for mixing therein with new aqueous solids; (vi) a remelt tank for melting the crystallized surfactant withdrawn from said other centrifuge; (vii) means for conveying crystallized surfactant from said other centrifuge to said remelt tank, and (viii) means for conveying surfactant from said remelt tank to said fluidizing tank for mixing therein with new aqueous solids.
Claim 2
Independent Claim 378 words
An apparatus for continuously dehydrating aqueous solids, said apparatus comprising: (1) a fluidizing tank disposed to receive a stream of aqueous solids and provided with a stirring or mixing mechanism; (2) a fluidizing oil source; (3) a surfactant source; (4) means for transmitting fluidizing oil from said fluidizing oil source to said fluidizing tank; (5) means for transmitting surfactant from said surfactant source to said fluidizing tank wherein fluidizing oil, aqueous solids and surfactant may be mixed; (6) an evaporator disposed to heat and dehydrate continuously a feed mixture of aqueous solids, fluidizing oil and surfactant and discharge water driven off therefrom as vapor; (7) a conduit extending from said fluidizing tank to said evaporator through which a mixture of aqueous solids, surfactant and fluidizing oil may flow from said tank into the evaporating region of said evaporator; (8) a screen bowl centrifuge disposed to wash and separate anhydrous solids from a mixture of substantially anhydrous solids, fluidizing oil and surfactant; (9) a conduit extending from said evaporator to said screen bowl centrifuge through which may flow a mixture of substantially anhydrous solids, fluidizing oil and surfactant from said evaporator to said centrifuge; (10) means for withdrawing anhydrous solids substantially free of fluidizing oil and surfactant from said centrifuge, and (11) means for withdrawing fluidizing oil and surfactant from said centrifuge and recycling the same to said fluidizing tank for mixing therein with new aqueous solids, that means comprising (i) a crystallizer for treating fluidizing oil and surfactant withdrawn together from said screen bowl centrifuge; (ii) means for conveying fluidizing oil and surfactant to said crystallizer from said screen bowl centrifuge; (iii) a centrifuge other than said screen bowl centrifuge disposed to separate crystallized surfactant from fluidizing oil; (iv) means for conveying a mixture of fluidizing oil and crystallized surfactant from said crystallizer to said other centrifuge; (v) means for recycling fluidizing oil withdrawn from said other centrifuge to said fluidizing tank for mixing therein with new aqueous solids; (vi) a remelt tank for melting the crystallized surfactant withdrawn from said other centrifuge; (vii) means for conveying crystallized surfactant from said other centrifuge to said remelt tank, and (viii) means for conveying surfactant from said remelt tank to said fluidizing tank for mixing therein with new aqueous solids.
Claim 3
Dependent Claim 12 words
The apparatus of claim 1 wherein said evaporator is a multi-stage evaporator.

References Cited (Backward Citations)

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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) 1990-05-04 1990-11-03 1991-05-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-05-04 1994-11-03 1995-05-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-05-04 1998-11-03 1999-05-05 $7700.00 Window Closed / Lapsed

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