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US4588418A Expired / Lapsed US ⏱️ 0.0 years remaining

Recycle of reclaimed water in partial oxidation process

Assignee: Millennium Petrochemicals Inc
•
Filing: 1983-02-07
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Granted: 1986-05-13
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Expires: 2003-02-07
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Abstract

Abstract In a partial oxidation process the gaseous effluent from a reactor is contacted with water to cool and remove solid particulates, i.e., ash and soot. The water from this operation is then mixed with an organic extractant, e.g., naphtha, and fed into a decanter to form aqueous and organic phases. The aqueous phase from the decanter is fed to a water flash separator to remove dissolved gases. The solids in a portion of the water flash separator bottoms are further concentrated in a hydrocyclone and thereafter purged. The remaining water is recycled for recontact with the gaseous effluent.

Inventors

  • 👤 William A. Gabler
  • 👤 Frank M. Julian

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 06:37
CPC Classifications
C; C10; C10J; C10J3/00; C10J3/72; C10J3/82; C10J3/84; C10K; C10K1/00; C10K1/04; C10K1/06; C10K1/08; C10K1/10; C10K1/101; C10J2300/00; C10J2300/09; C10J2300/0953; C10J2300/0956; C10J2300/0959; C10J2300/18; C10J2300/1807; C10J2300/1846

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 222 words
In a partial oxidation process for producing gaseous mixtures containing H 2 , CO, water, soot, gaseous materials including one or more of CO 2 , H 2 S, COS, CH 4 , NH 3 and N 2 and between 100 and 700 ppm ash particles comprising materials including vanadium, sulfur, nickel, iron, calcium, sodium, molybdenum, or their reaction products, the particles having an average particle size less than one micrometer, by the partial oxidation of a hydrocarbonaceous feed with an oxygen-containing gas; contacting the gaseous mixture with water in a gas quenching or scrubbing step or both; removing a water stream from this step containing soot; dissolved gaseous materials and suspended ash particles; adding a liquid organic extractant to the stream; feeding the stream to a decanter wherein aqueous and organic phase form; removing from the bottom of the decanter the aqueous phase containing water, dissolved gaseous material, soot and the suspended ash particles; feeding the dissolved aqueous phase to water flash separator wherein the dissolved gases are flashed off; and removing from the bottom of the water flash separator the remaining liquid phase for recycle to the quenching or scrubbing step and purging part of this liquid phase; the improvement comprising concentrating the suspended ash particles in the purge stream using a hydrocyclone having a maximum diameter of 10 mm.
Claim 2
Dependent Claim 222 words
In a partial oxidation process for producing gaseous mixtures containing H 2 , CO, water, soot, gaseous materials including one or more of CO 2 , H 2 S, COS, CH 4 , NH 3 and N 2 and between 100 and 700 ppm ash particles comprising materials including vanadium, sulfur, nickel, iron, calcium, sodium, molybdenum, or their reaction products, the particles having an average particle size less than one micrometer, by the partial oxidation of a hydrocarbonaceous feed with an oxygen-containing gas; contacting the gaseous mixture with water in a gas quenching or scrubbing step or both; removing a water stream from this step containing soot; dissolved gaseous materials and suspended ash particles; adding a liquid organic extractant to the stream; feeding the stream to a decanter wherein aqueous and organic phase form; removing from the bottom of the decanter the aqueous phase containing water, dissolved gaseous material, soot and the suspended ash particles; feeding the dissolved aqueous phase to water flash separator wherein the dissolved gases are flashed off; and removing from the bottom of the water flash separator the remaining liquid phase for recycle to the quenching or scrubbing step and purging part of this liquid phase; the improvement comprising concentrating the suspended ash particles in the purge stream using a hydrocyclone having a maximum diameter of 10 mm.

References Cited (Backward Citations)

US4141695A Cited
US4205963A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1989-05-12 1989-11-11 1990-05-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1993-05-12 1993-11-11 1994-05-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1997-05-12 1997-11-11 1998-05-13 $7700.00 Window Closed / Lapsed

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