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US5082551A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydroconversion effluent separation process

Assignee: Chevron USA Inc
•
Filing: 1990-07-25
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Granted: 1992-01-21
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Expires: 2010-07-25
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Abstract

Abstract A hydroconversion effluent separation process is provided. The effluent from the hydroconversion zone is passed to a hot high pressure separation zone. The gas phase from that zone is then passed to a cold high pressure separation zone while the liquid hydrocarbon bottoms is passed to a hot low pressure separation zone. The gas phase is partially condensed in the cold high pressure separation zone to obtain a hydrogen-rich gas and a liquid hydrocarbon bottoms. A portion of the hydrogen-rich gas is recycled to the hydroconversion zone. A second portion is sent to a hydrogen purification step, most preferably by membrane separation, and the purified gas is recycled to the hydroconversion zone. The overhead from the hot low pressure separation is fed to a cold low pressure separation zone. The gas phase from the cold low pressure separation zone is recycled to the hydroconversion zone. Preferably, two cold low pressure separation zones are utilized in the process.

Inventors

  • 👤 Bruce E. Reynolds
  • 👤 Donald A. Bea
  • 👤 Robert W. Bachtel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 19:38
CPC Classifications
C; C10; C10G; C10G49/00; C10G49/22; C10G49/007

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 296 words
A process for separating gases from a hydroconversion zone reaction effluent comprising: (a) effecting a hot high pressure separation of the effluent by reducing the temperature of the effluent to produce a first gas phase comprising hydrogen, contaminant gases, and gaseous hydrocarbons and a first liquid phase comprising hydrocarbons, and separating the first gas phase from the first liquid phase; (b) effecting a cold high pressure separation of the first gas phase by reducing the temperature of the first gas phase to form a first hydrogen-rich gas product and a second liquid phase, and separating the second liquid phase from the first hydrogen-rich gas; (c) effecting a hot low pressure separation of the first liquid phase by reducing the pressure of the first liquid phase to form a second gas phase comprising hydrogen and gaseous hydrocarbons and a third liquid phase comprising hydrocarbons, and separating the second gas phase from the third liquid phase; (d) effecting a cold low pressure separation of the second gas phase by reducing the temperature thereof to form a second hydrogen-rich and a fourth liquid phase comprising hydrocarbons, and separating the fourth liquid phase from the second hydrogen-rich gas; (e) recycling the second hydrogen-rich gas to the hydroconversion zone; (f) subjecting said first hydrogen-rich gas product to the removal of contaminants comprising H 2 S to produce a hydrogen-rich, contaminant-removal treated gas and recycling a first portion of said hydrogen-rich, contaminant-removal treated gas to the hydroconversion zone; (g) purifying a second portion of said hydrogen-rich, contaminant-removal treated gas to obtain a purified hydrogen-rich gas of at least 95 volume percent hydrogen, wherein the purification is carried out using membranes to separate the purified hydrogen-rich gas from the first hydrogen-rich gas; and (h) recycling the purified hydrogen-rich gas to the hydroconversion zone.
Claim 2
Dependent Claim 296 words
A process for separating gases from a hydroconversion zone reaction effluent comprising: (a) effecting a hot high pressure separation of the effluent by reducing the temperature of the effluent to produce a first gas phase comprising hydrogen, contaminant gases, and gaseous hydrocarbons and a first liquid phase comprising hydrocarbons, and separating the first gas phase from the first liquid phase; (b) effecting a cold high pressure separation of the first gas phase by reducing the temperature of the first gas phase to form a first hydrogen-rich gas product and a second liquid phase, and separating the second liquid phase from the first hydrogen-rich gas; (c) effecting a hot low pressure separation of the first liquid phase by reducing the pressure of the first liquid phase to form a second gas phase comprising hydrogen and gaseous hydrocarbons and a third liquid phase comprising hydrocarbons, and separating the second gas phase from the third liquid phase; (d) effecting a cold low pressure separation of the second gas phase by reducing the temperature thereof to form a second hydrogen-rich and a fourth liquid phase comprising hydrocarbons, and separating the fourth liquid phase from the second hydrogen-rich gas; (e) recycling the second hydrogen-rich gas to the hydroconversion zone; (f) subjecting said first hydrogen-rich gas product to the removal of contaminants comprising H 2 S to produce a hydrogen-rich, contaminant-removal treated gas and recycling a first portion of said hydrogen-rich, contaminant-removal treated gas to the hydroconversion zone; (g) purifying a second portion of said hydrogen-rich, contaminant-removal treated gas to obtain a purified hydrogen-rich gas of at least 95 volume percent hydrogen, wherein the purification is carried out using membranes to separate the purified hydrogen-rich gas from the first hydrogen-rich gas; and (h) recycling the purified hydrogen-rich gas to the hydroconversion zone.
Claim 3
Dependent Claim 56 words
A process in accordance with claim 1 further comprising: (i) effecting a second cold low pressure separation by reducing the pressure of the second liquid phase to form a third gas phase comprising contaminant gases and gaseous hydrocarbons, and a fifth liquid phase comprising hydrocarbons; and separating the third gas phase from the fifth liquid phase.
Claim 4
Dependent Claim 23 words
A process in accordance with claim 2 wherein the hydrogen content of the first hydrogen-rich gas is at least about 75% by volume.
Claim 5
Dependent Claim 24 words
A process in accordance with claim 3 wherein the hydrogen content of the first hydrogen-rich gas is at least about 80 percent by volume.
Claim 6
Dependent Claim 70 words
A process in accordance with claim 1 wherein hydrotreating is carried out in the hydroconversion zone, the feed to the hydroconversion zone is a heavy oil boiling mostly above 650° F., the hydroconversion zone is operated at a temperature above 700° F. and the hydroconversion reaction zone effluent is cooled to a temperature between 750° F. and 650° F. prior to separating the first gas from the first liquid phase.
Claim 7
Dependent Claim 45 words
A process in accordance with claim 5 wherein the temperature at which the step (a) separation is affected and the temperature at which the step (b) separation is affected are adjusted to obtain at least 80 volume percent hydrogen content for the first hydrogen-rich gas.
Claim 8
Dependent Claim 24 words
A process in accordance with claim 6 wherein the temperature at which the step (a) separation is effected is 675° F. to 725° F.
Claim 9
Dependent Claim 87 words
A process in accordance with claim 1 wherein the temperature of the effluent is reduced to between about 400° F. and 750° F. in step (a); the temperature of the first gas phase is reduced to between about 90° F. and 200° F. in step (b); the pressure of the first liquid phase is reduced to between about 100 psig and 1000 psig in step (c); and the temperature of the second gas phase is reduced to between about 90° F. and 200° F. in step (d).
Claim 10
Dependent Claim 18 words
A process in accordance with claim 1 wherein the membrane separation is carried out using hollow fiber membranes.

References Cited (Backward Citations)

US3471398A Cited
US3598720A Cited
US3607726A Cited
US4159937A Cited
US4457834A Cited
US4673488A Cited
US4925573A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-01-20 1995-07-22 1996-01-21 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-01-20 1999-07-22 2000-01-21 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-01-20 2003-07-22 2004-01-21 $7700.00 Window Closed / Lapsed

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