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US4537685A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for separating intermixed solids and liquids

Assignee: LEFCO ACQUISITION Corp
•
Filing: 1983-02-01
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Granted: 1985-08-27
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Expires: 2003-02-01
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Abstract

Abstract A mixture containing solid and liquid components is saturated with a polyelectrolyte compound, over-flocculating the solids contained therein and causing the solids to coalesce into masses or globules. These coalesced masses may then be separated from the liquid component, yielding substantially separated phases.

Inventors

  • 👤 Alvin B. Kennedy, III
  • 👤 Joseph S. Fontaine
  • 👤 Alfred J. Kennard
  • 👤 J. Bruce Morrison

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 11:19
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/52; C02F1/54; C02F11/00; C02F11/12; C02F11/121

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 266 words
A continuous method useful in the separation of intermixed solids and liquid phase components of wastes so as to facilitate the recycling or disposal thereof, comprising the steps of: (a) pretesting a sample of the waste designated for treatment so as to determine the character of solid waste matter and content of suspended and/or settled waste solids, (b) selecting a polyelectrolyte compound calculated to react most effectively with the tested waste, said polyelectrolyte compound being a high molecular weight polymer emulsion selected from the group consisting of cationic, and anionic and non-ionic polymers, (c) calculating a dosage rate determined to overflocculate the waste matter and to achieve optimal efficiency from the polyelectrolyte-waste matter reaction so as to achieve solid waste particles which will freely dewater, which are larger than 20 mesh, and which exhibit an appropriate durability factor to allow separation of the solid waste particles from the liquid phase, (d) air sparging the waste source to promote consistency and fluidity so as to minimize adjustment of the dosage rate of polyelectrolyte compounds to waste matter, (e) continuously diluting the polyelectrolyte compound with water, (f) introducing the diluted polyelectrolyte compound into the waste matter without mechanical agitation at a varying rate so as to achieve over-flocculation of the suspended and/or settled waste solids, (g) separating the over-flocculated solid waste particles from the treated liquid waste with a vibratory shaker screen, (h) recycling all of the treated liquid for further use as a pre-treatment for untreated waste thereby reducing the overall polyelectrolyte requirement for continued treatment, and elminating the need to remove the polyelectrolyte from the liquid.
Claim 2
Dependent Claim 266 words
A continuous method useful in the separation of intermixed solids and liquid phase components of wastes so as to facilitate the recycling or disposal thereof, comprising the steps of: (a) pretesting a sample of the waste designated for treatment so as to determine the character of solid waste matter and content of suspended and/or settled waste solids, (b) selecting a polyelectrolyte compound calculated to react most effectively with the tested waste, said polyelectrolyte compound being a high molecular weight polymer emulsion selected from the group consisting of cationic, and anionic and non-ionic polymers, (c) calculating a dosage rate determined to overflocculate the waste matter and to achieve optimal efficiency from the polyelectrolyte-waste matter reaction so as to achieve solid waste particles which will freely dewater, which are larger than 20 mesh, and which exhibit an appropriate durability factor to allow separation of the solid waste particles from the liquid phase, (d) air sparging the waste source to promote consistency and fluidity so as to minimize adjustment of the dosage rate of polyelectrolyte compounds to waste matter, (e) continuously diluting the polyelectrolyte compound with water, (f) introducing the diluted polyelectrolyte compound into the waste matter without mechanical agitation at a varying rate so as to achieve over-flocculation of the suspended and/or settled waste solids, (g) separating the over-flocculated solid waste particles from the treated liquid waste with a vibratory shaker screen, (h) recycling all of the treated liquid for further use as a pre-treatment for untreated waste thereby reducing the overall polyelectrolyte requirement for continued treatment, and elminating the need to remove the polyelectrolyte from the liquid.
Claim 3
Dependent Claim 36 words
The method of claim 1, wherein the dosage rate of polyelectrolyte compound to waste matter is generally within the range of two hundred to one thousand parts of polymer to one million parts of waste matter.
Claim 4
Dependent Claim 32 words
The method of claim 2, wherein the diluted polyelectrolyte compound is introduced into the waste matter at a varying rate, ranging from a few drops per minute to one-half gallon per minute.

References Cited (Backward Citations)

US3790476A Cited
US3790476B1 Cited
US4093542A Cited
US3956116A Cited
US4303532A Cited
US4330450A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-08-26 1989-02-25 1989-08-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-08-26 1993-02-25 1993-08-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-08-26 1997-02-25 1997-08-27 $7700.00 Window Closed / Lapsed

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