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US4256476A Expired / Lapsed US ⏱️ 0.0 years remaining

Low temperature process for the recovery of ethane from thermal hydrocracking vent gases

Assignee: IFP Energies nouvelles
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Filing: 1979-05-04
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Granted: 1981-03-17
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Expires: 1999-05-04
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Abstract

Abstract The present invention provides a method for recovering ethane from a gaseous mixture comprising hydrogen, methane, ethane, and aromatics, comprising subjecting the gaseous mixture to a series of condensing steps to separate the components and flashing the so-obtained ethane to produce a substantially pure ethane product stream.

Inventors

  • 👤 Edward H. Van Baush

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 23:55
CPC Classifications
F; F25; F25J; F25J3/00; F25J3/06; F25J3/063; F25J3/0655; C; C07; C07C; C07C7/00; C07C7/005; F25J3/0605; F25J3/062; F25J3/0635; F25J3/064; F25J2210/00; F25J2210/12

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 494 words
A process for separating ethane from a gaseous feed comprising a mixture of hydrogen, alkanes, aromatics and alkyl aromatics comprising: (a) feeding the gaseous feed to a first condenser to condense the aromatics and alkyl aromatics in the feed; (b) feeding the product of (a) to a first phase separator to obtain an overhead vapor product and a bottom liquid product which contains substantially all of the aromatics present in the feed; (c) feeding the overhead vapor product successively to a second and a third condenser to condense the ethane contained therein; (d) feeding the product of (c) to a second phase separator to obtain an overhead vapor product and a bottom liquid product comprising primarily ethane; (e) feeding the overhead vapor product of (d) to a fourth condenser to condense the methane contained therein; (f) feeding the product of (e) to a third phase separator to obtain an overhead vapor product comprising primarily hydrogen and a bottom liquid product comprising primarily methane; (g) feeding the overhead vapor product of (f) successively to the fourth, third, second, and first condensers and combining the bottom vapor product from the first phase separator of (b) with the overhead vapor product of (f) leaving the second condenser to obtain a product stream having ambient temperature and pressure and comprising the hydrogen and the aromatics present in the feed; (h) feeding the bottom liquid product from the third phase separator in (f) to the fourth, third, second, and first condensers in succession to obtain a fuel gas stream comprising the methane present in the feed and having ambient temperature and pressure; (i) feeding the bottom liquid product from the second phase separator of (d) to the third condenser to heat the liquid to a gas-liquid mixture; (j) feeding the gas-liquid mixture of (i) to a fourth phase separator to obtain an overhead vapor product comprising primarily methane and a bottom liquid product comprising primarily ethane; (k) throttling the liquid product of (i) and feeding the throttled product of the third condenser to heat the liquid product to form a gas-liquid mixture; (l) feeding the gas-liquid mixture of (k) to a first ethane flash drum to obtain an overhead vapor product comprising methane and ethane and a bottom liquid product which is substantially pure ethane; (m) feeding the overhead vapor product of (l) to the third condenser to condense the ethane; (n) feeding the product of (m) to a second ethane flash drum to obtain an overhead vapor product containing primarily methane and a bottom liquid product containing primarily ethane; (o) combining the bottom liquid products of steps (m) and (n) to form a liquid ethane-containing stream and feeding the ethane stream to the second and first condensers in succession to heat the ethane stream to ambient temperature and pressure; and (p) combining the overhead vapor product from step (n) with the bottom product of (g) and feeding the combined product to the second and first condensers in succession.
Claim 2
Dependent Claim 494 words
A process for separating ethane from a gaseous feed comprising a mixture of hydrogen, alkanes, aromatics and alkyl aromatics comprising: (a) feeding the gaseous feed to a first condenser to condense the aromatics and alkyl aromatics in the feed; (b) feeding the product of (a) to a first phase separator to obtain an overhead vapor product and a bottom liquid product which contains substantially all of the aromatics present in the feed; (c) feeding the overhead vapor product successively to a second and a third condenser to condense the ethane contained therein; (d) feeding the product of (c) to a second phase separator to obtain an overhead vapor product and a bottom liquid product comprising primarily ethane; (e) feeding the overhead vapor product of (d) to a fourth condenser to condense the methane contained therein; (f) feeding the product of (e) to a third phase separator to obtain an overhead vapor product comprising primarily hydrogen and a bottom liquid product comprising primarily methane; (g) feeding the overhead vapor product of (f) successively to the fourth, third, second, and first condensers and combining the bottom vapor product from the first phase separator of (b) with the overhead vapor product of (f) leaving the second condenser to obtain a product stream having ambient temperature and pressure and comprising the hydrogen and the aromatics present in the feed; (h) feeding the bottom liquid product from the third phase separator in (f) to the fourth, third, second, and first condensers in succession to obtain a fuel gas stream comprising the methane present in the feed and having ambient temperature and pressure; (i) feeding the bottom liquid product from the second phase separator of (d) to the third condenser to heat the liquid to a gas-liquid mixture; (j) feeding the gas-liquid mixture of (i) to a fourth phase separator to obtain an overhead vapor product comprising primarily methane and a bottom liquid product comprising primarily ethane; (k) throttling the liquid product of (i) and feeding the throttled product of the third condenser to heat the liquid product to form a gas-liquid mixture; (l) feeding the gas-liquid mixture of (k) to a first ethane flash drum to obtain an overhead vapor product comprising methane and ethane and a bottom liquid product which is substantially pure ethane; (m) feeding the overhead vapor product of (l) to the third condenser to condense the ethane; (n) feeding the product of (m) to a second ethane flash drum to obtain an overhead vapor product containing primarily methane and a bottom liquid product containing primarily ethane; (o) combining the bottom liquid products of steps (m) and (n) to form a liquid ethane-containing stream and feeding the ethane stream to the second and first condensers in succession to heat the ethane stream to ambient temperature and pressure; and (p) combining the overhead vapor product from step (n) with the bottom product of (g) and feeding the combined product to the second and first condensers in succession.
Claim 3
Dependent Claim 41 words
The process of claim 1 wherein the temperature of the gas-liquid mixture obtained in step (i) is increased by increasing the amount of overhead vapor product obtained in step (f) which is bypassed around the warm end of the third condenser.
Claim 4
Dependent Claim 28 words
The process of claim 1 wherein the temperature of the gas-liquid mixture obtained in step (i) is increased by depressing the rate of vaporization in the third condenser.
Claim 5
Dependent Claim 38 words
The process of claim 1 wherein the temperature of the gas-liquid mixture obtained in step (i) is increased by bypassing a portion of the bottom liquid product from the fourth phase separator to the first ethane flash drum.
Claim 6
Dependent Claim 38 words
The process of claim 1 wherein the temperature of the gas-liquid mixture obtained in step (i) is decreased by feeding the overhead vapor product from the second ethane flash drum to the warm end of the third condenser.
Claim 7
Dependent Claim 42 words
The process of claim 1 wherein the temperature of the gas-liquid mixture obtained in step (i) is decreased by feeding a portion of the bottom liquid product from the second phase separator to the liquid product stream from the fourth phase separator.

References Cited (Backward Citations)

US3373574A Cited
US3626705A Cited
US3691779A Cited
US3796059A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-03-16 1984-09-15 1985-03-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-03-16 1988-09-15 1989-03-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-03-16 1992-09-15 1993-03-17 $7700.00 Window Closed / Lapsed

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