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US4328104A Expired / Lapsed US ⏱️ 0.0 years remaining

Process of demulsifying and converting emulsions of oils, greases and fats

Assignee: Voestalpine AG
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Filing: 1980-05-27
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Granted: 1982-05-04
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Expires: 2000-05-27
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Abstract

Abstract It is proposed to demulsify and convert emulsions of oils, greases, and fats in that these emulsions are processed together with digested sludge or sludge liquor from a biological sewage treatment plant. The emulsions of oils, greases, or fats are fed after a first digesting step and preferably to a separate container. In that second digesting step, the bacteria growing under anaerobic conditions can convert much larger quantities of emulsions and the emulsions can be converted within a shorter time.

Inventors

  • 👤 Reinhart Hanke
  • 👤 Bertalan Treso

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 20:14
CPC Classifications
C; C02; C02F; C02F3/00; C02F3/28; C02F3/286; B; B01; B01D; B01D17/00; B01D17/02; B01D17/04; Y; Y02; Y02E; Y02E50/00; Y02E50/30

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 126 words
A process of demulsifying and coverting emulsions of oils, greases, and fats wherein the emulsions are processed together with sewage sludges, characterized by adding the emulsion to be demulsified and converted to the second digesting tank of a digested sludge or to a sludge liquor which has been obtained by a biological sewage treatment and has been subjected to a first digesting step, which involves mainly an acid fermentation and makes mainly organic acids and CO 2 available, the resulting mixture is subjected to a second digesting step that is conducted under anaerobic conditions and in an environment which differs from that of the first step and results mainly in an evolution of methane, said two digesting steps being carried out in two separate digesting tanks.
Claim 2
Dependent Claim 126 words
A process of demulsifying and coverting emulsions of oils, greases, and fats wherein the emulsions are processed together with sewage sludges, characterized by adding the emulsion to be demulsified and converted to the second digesting tank of a digested sludge or to a sludge liquor which has been obtained by a biological sewage treatment and has been subjected to a first digesting step, which involves mainly an acid fermentation and makes mainly organic acids and CO 2 available, the resulting mixture is subjected to a second digesting step that is conducted under anaerobic conditions and in an environment which differs from that of the first step and results mainly in an evolution of methane, said two digesting steps being carried out in two separate digesting tanks.
Claim 3
Dependent Claim 36 words
A process according to claim 1, characterized by feeding the emulsion to be converted to a digesting tank for digesting surplus sludge which has been obtained in a biological sewage treatment plant and has been predigested.
Claim 4
Dependent Claim 38 words
A process according to claim 1 or 2, characterized by adding emulsion to the predigested sludge or sludge liquor in an amount of up to 0.25 kg oil per kg of dry sludge solids in a continuous process.
Claim 5
Dependent Claim 42 words
A process according to claim 1 or 2, characterized by adding emulsion to the sludge or to the predigested sludge or sludge liquor in an amount of 0.25 to 1.0 kg oil per kg of dry sludge solids in a batch process.
Claim 6
Dependent Claim 24 words
A process according to claim 1 or 2, characterized by effecting the digestion in an anaerobic environment at temperatures between 20° and 55° C.
Claim 7
Dependent Claim 30 words
A process according to claim 1 or 2, characterized by effecting in a continuous process the digestion with a residence time of at least 3 days in the digesting tank.
Claim 8
Dependent Claim 22 words
A process according to claim 1 or 2, characterized in that an oil-in-water emulsion to the sludge, digested sludge or sludge liquor.
Claim 9
Dependent Claim 34 words
A process according to claim 1 or 2, characterized by adding oil to the sludge, digested sludge or sludge liquor in such a quantity that a C/N ratio in excess of 10 is obtained.
Claim 10
Dependent Claim 30 words
A process according to claim 1 or 2, characterized by adding the emulsion is added after not less than 10 days, when the digestion is effected at about 35° C.
Claim 11
Dependent Claim 22 words
A process according to claim 1 comprising adding the emulsion after about 14 days and effecting the digestion at about 35° C.
Claim 12
Dependent Claim 31 words
A process according to claim 1 comprising adding oil to the sludge, digested sludge, or sludge liquor in such a quantity that a C/N ratio in excess of 15 is obtained.
Claim 13
Dependent Claim 21 words
A process according to claim 1 comprising effecting the digestion in an anaerobic environment at temperatures between 30° and 45° C.
Claim 14
Dependent Claim 40 words
A process according to claim 1 wherein the emulsion is one from (1) a synthetic oil which is a cutting, cooling, or lubricating fluid, (2) an oil containing sulfur and/or chloride salts, (3) used scrubbing liquor or a degreasing bath.
Claim 15
Dependent Claim 33 words
A process according to claim 13 wherein the emulsion is one from (1) a synthetic oil which is a cutting, cooling, or lubricating fluid or (2) an oil containing sulfur and/or chloride salts.
Claim 16
Dependent Claim 23 words
A process according to claim 14 wherein the emulsion is one from a synthetic oil which is a cutting, cooling, or lubricating fluid.
Claim 17
Dependent Claim 15 words
A process according to claim 1 carried out in the presence of an emulsifying agent.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-05-03 1985-11-02 1986-05-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-05-03 1989-11-02 1990-05-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-05-03 1993-11-02 1994-05-04 $7700.00 Window Closed / Lapsed

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