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US4282013A Expired / Lapsed US ⏱️ 0.0 years remaining

Vacuum pump operation in a maleic anhydride recovery system

Assignee: Chevron USA Inc
•
Filing: 1977-11-14
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Granted: 1981-08-04
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Expires: 1997-11-14
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Abstract

Abstract In a reduced-pressure process for distilling crude maleic anhydride recovered by separation from an organic absorbent wherein reduced pressure is obtained using a liquid ring-seal vacuum pump, the improvement which comprises sealing the liquid ring-seal vacuum pump by circulating a maleic anhydride absorbent from a regenerating zone through the vacuum pump chamber.

Inventors

  • 👤 Frederick C. Franklin
  • 👤 Stephen G. Paradis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 14:21
CPC Classifications
F; F04; F04C; F04C19/00; F04C19/004; C; C07; C07C; C07C51/00; C07C51/54; C07C51/573

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 300 words
A method for increasing the yield and reducing mechanical vacuum pump fouling from precipitated maleic anhydride in a continuous process for preparing maleic anhydride by vapor phase oxidation of a hydrocarbon feedstock followed by absorption of the maleic anhydride by a liquid organic absorbent therefor in an absorption zone and then stripping of the maleic anhydride from the organic absorbent under reduced pressure conditions, wherein a mechanical vacuum pump means is employed to develop said reduced pressure conditions in said stripping zone of said process, the improvement in recovery of residual maleic anhydride which comprises: (a) flowing vapors containing said residual maleic anhydride from said stripping zone to the central portion of a liquid-ring seal vacuum pump constituting said mechanical pump means; (b) concurrently flowing at least a portion of said stripped organic absorbent into the circumferential ring portion of said liquid-ring seal vacuum pump to form the liquid-ring seal and working liquid of said pump; (c) continuously mixing said vapors with said stripped organic absorbent to form a liquid maleic anhydride-rich organic absorbent phase and a gaseous disposables phase; (d) withdrawing the resultant liquid maleic anhydride-rich organic absorbent phase and reduced gaseous disposables phase from said pump; (e) separating said gaseous disposables phase from said liquid maleic anhydride-rich organic absorbent phase and venting said separated gaseous disposables phase; (f) passing a portion of said liquid maleic anhydride-rich organic absorbent phase to said absorption zone of said process to recycle said maleic anhydride; (g) passing the remainder of said liquid maleic anhydride-rich organic absorbent phase into the circumferential ring portion of said pump to maximize the concentration of maleic anhydride therein; whereby said method substantially eliminates vapor phase maleic anhydride from said gaseous disposables phase and from contact with portions of said mechanical vacuum pump exposed to ambient atmospheric conditions.
Claim 2
Independent Claim 300 words
A method for increasing the yield and reducing mechanical vacuum pump fouling from precipitated maleic anhydride in a continuous process for preparing maleic anhydride by vapor phase oxidation of a hydrocarbon feedstock followed by absorption of the maleic anhydride by a liquid organic absorbent therefor in an absorption zone and then stripping of the maleic anhydride from the organic absorbent under reduced pressure conditions, wherein a mechanical vacuum pump means is employed to develop said reduced pressure conditions in said stripping zone of said process, the improvement in recovery of residual maleic anhydride which comprises: (a) flowing vapors containing said residual maleic anhydride from said stripping zone to the central portion of a liquid-ring seal vacuum pump constituting said mechanical pump means; (b) concurrently flowing at least a portion of said stripped organic absorbent into the circumferential ring portion of said liquid-ring seal vacuum pump to form the liquid-ring seal and working liquid of said pump; (c) continuously mixing said vapors with said stripped organic absorbent to form a liquid maleic anhydride-rich organic absorbent phase and a gaseous disposables phase; (d) withdrawing the resultant liquid maleic anhydride-rich organic absorbent phase and reduced gaseous disposables phase from said pump; (e) separating said gaseous disposables phase from said liquid maleic anhydride-rich organic absorbent phase and venting said separated gaseous disposables phase; (f) passing a portion of said liquid maleic anhydride-rich organic absorbent phase to said absorption zone of said process to recycle said maleic anhydride; (g) passing the remainder of said liquid maleic anhydride-rich organic absorbent phase into the circumferential ring portion of said pump to maximize the concentration of maleic anhydride therein; whereby said method substantially eliminates vapor phase maleic anhydride from said gaseous disposables phase and from contact with portions of said mechanical vacuum pump exposed to ambient atmospheric conditions.

References Cited (Backward Citations)

US2574644A Cited
US3045716A Cited
US3261847A Cited
US3818680A Cited
US3891680A Cited
US3965123A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-03 1985-02-02 1985-08-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-03 1989-02-02 1989-08-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-03 1993-02-02 1993-08-04 $7700.00 Window Closed / Lapsed

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