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US3907920A Expired / Lapsed US ⏱️ 0.0 years remaining

Two-stage hydropyrolysis-cracking process for producing ethylene

Assignee: ConocoPhillips Co
•
Filing: 1974-03-25
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Granted: 1975-09-23
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Expires: 1994-03-25
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Abstract

Abstract Ethylene along with methane may be produced by an integrated process involving a first stage hydropyrolysis of a hydrocarbon oil in the presence of hydrogen followed by cracking of the hydropyrolysis effluent, separating and recycling the hydrogen and ethane and recovering the methane and ethylene.

Inventors

  • 👤 Charles M Starks

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 20:17
CPC Classifications
C; C10; C10G; C10G65/00; C10G65/02; C10G65/12; C10G2400/00; C10G2400/20; Y; Y02; Y02P; Y02P30/00; Y02P30/40

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 197 words
A PROCESS FOR PRODUCING ETHYLENE FROM HIGHER HYDROCARBONS COMPRISING A. INTRODUCING A HYDROCARBON OIL AND HYDROGEN TO A FIRST STAGE HYDROPYROLYSIS ZONE, THE MOL RATIO OF HYDROGEN TO HYDROCARBON OIL BEING AT LEAST 1/1, B. HYDROPROLYZING THE HYDROCARBON OIL IN THE PRESENCE OF THE HYDROGEN IN SAID ZONE UNDER CONDITION OF TEMPERATURES IN THE RANGE OF ABOUT 600*C 600*C TO 900*C, PRESSURES OF AT LEAST ABOUT 5 ATMOSPHERES GAUGE AND RESIDENCE TIME IN THE RANGE OF ABOUT 0.1 TO 60 SECONDS, TO PROSUCE A HYDROPYROLYSIS EFFLUENT, C. INTRODUCING SUBSTANTIALLY ALL OF THE HYDROPYROLYSIS EFFUENT TO A SECOND-STAGE CRACKING ZONE AND SUBJECTING SAID EFFUENT TO CRACKING CONDITIONS OF TEMPERATURES IN THE RANGE OF ABOUT 750*C TO 900*C, PRESSURES NOT IN EXCESS OF ABOUT 2 ATMOSPHERES GAUGE AND RESIDENCE TIMES IN THE RANGE OF ABOUT 0.01 TO 10 SECONDS, TO PRODUCE A CRACKING ZONE EFFLUENT, D. SEPARATING SAID CRACKING ZONE EEFFLUENT INTO A HYDROGEN STREAM, A METHANE STREAM, AMN ETHYLENE STREAM, AN ETHANE STREAM, AND A HIGHER HYDROCARBON STREAM, E. RECYCLING THE HYDROGEN STREAM TO THE FIRST STAGE HYDROPROLYSIS ZNE AND RECYCLING THE ETHANE STREAM TO THE SECOND-STAGE CRACKING ZONE, F. AND RECOVERING THE METHANE STREAM AND ETHYLENE STREAM.
Claim 2
Dependent Claim 197 words
A PROCESS FOR PRODUCING ETHYLENE FROM HIGHER HYDROCARBONS COMPRISING A. INTRODUCING A HYDROCARBON OIL AND HYDROGEN TO A FIRST STAGE HYDROPYROLYSIS ZONE, THE MOL RATIO OF HYDROGEN TO HYDROCARBON OIL BEING AT LEAST 1/1, B. HYDROPROLYZING THE HYDROCARBON OIL IN THE PRESENCE OF THE HYDROGEN IN SAID ZONE UNDER CONDITION OF TEMPERATURES IN THE RANGE OF ABOUT 600*C 600*C TO 900*C, PRESSURES OF AT LEAST ABOUT 5 ATMOSPHERES GAUGE AND RESIDENCE TIME IN THE RANGE OF ABOUT 0.1 TO 60 SECONDS, TO PROSUCE A HYDROPYROLYSIS EFFLUENT, C. INTRODUCING SUBSTANTIALLY ALL OF THE HYDROPYROLYSIS EFFUENT TO A SECOND-STAGE CRACKING ZONE AND SUBJECTING SAID EFFUENT TO CRACKING CONDITIONS OF TEMPERATURES IN THE RANGE OF ABOUT 750*C TO 900*C, PRESSURES NOT IN EXCESS OF ABOUT 2 ATMOSPHERES GAUGE AND RESIDENCE TIMES IN THE RANGE OF ABOUT 0.01 TO 10 SECONDS, TO PRODUCE A CRACKING ZONE EFFLUENT, D. SEPARATING SAID CRACKING ZONE EEFFLUENT INTO A HYDROGEN STREAM, A METHANE STREAM, AMN ETHYLENE STREAM, AN ETHANE STREAM, AND A HIGHER HYDROCARBON STREAM, E. RECYCLING THE HYDROGEN STREAM TO THE FIRST STAGE HYDROPROLYSIS ZNE AND RECYCLING THE ETHANE STREAM TO THE SECOND-STAGE CRACKING ZONE, F. AND RECOVERING THE METHANE STREAM AND ETHYLENE STREAM.
Claim 3
Dependent Claim 30 words
A process according to claim 1 wherein the hydrocarbon oil has a density of less than about 0.99 and a Conradson carbon content of less than about 20 weight percent.
Claim 4
Dependent Claim 43 words
A process according to claim 1 wherein the conditions of hydropyrolysis are temperatures in the range of about 700*C to 850*C, pressures in the range of about 5 to 100 atmospheres gauge and residence times in the range of 0.5 to 20 seconds.
Claim 5
Dependent Claim 23 words
A process according to claim 3 wherein the hydrogen to hydrocarbon oil mol ratio is in the range of about 3/1 to 30/1.
Claim 6
Dependent Claim 16 words
A process according to claim 3 wherein water is also introduced to the first-stage hydropyrolysis zone.
Claim 7
Dependent Claim 42 words
A process according to claim 3 wherein the second-stage cracking zone conditions are temperatures in the range of about 800*C to 850*C, pressures not in excess of about 1 atmosphere gauge and residence times in the range of 0.1 to 1 second.
Claim 8
Dependent Claim 20 words
A process according to claim 1 wherein the higher hydrocarbon stream is hydrogenated and recycled to the first-stage hydropyrolysis zone.
Claim 9
Dependent Claim 35 words
A process according to claim 1 wherein the higher hydrocarbon stream is separated into an aromatics stream and a remaining stream, recovering the aromatics stream and recycling the remaining stream to the first-stage hydropyrolysis zone.
Claim 10
Dependent Claim 15 words
A process according to claim 8 wherein the remaining stream is hydrogenated prior to recycling.

References Cited (Backward Citations)

US2089616A Cited
US2245819A Cited
US3373220A Cited
US3511771A Cited
US3839484A Cited
US3842138A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-22 1979-03-24 1979-09-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-22 1983-03-24 1983-09-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-22 1987-03-24 1987-09-23 $7700.00 Window Closed / Lapsed

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