US3862898A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the production of olefinically unsaturated hydrocarbons
Assignee: MW Kellogg Co
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Filing: 1973-07-30
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Granted: 1975-01-28
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Expires: 1993-07-30
Abstract
Abstract Hydrocarbon feedstock containing petroleum residuum is catalytically cracked in a heavy oil cracking unit to produce a naphtha feed suitable for processing by steam pyrolysis to olefins. By the process integration disclosed, internal gas compression energy requirements for olefins recovery are furnished by steam generated in the heavy oil cracking unit.
Inventors
- 👤 Harold B Boyd
- 👤 James R Lambrix
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 18:00
CPC Classifications
C; C10; C10G; C10G51/00; C10G51/02; C10G2400/00; C10G2400/20
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
142 words
A PROCESS FOR THE PRODUCTION OF OLEFINICALLY UNSATURATED HYDROCARBONS WHICH COMPRISES THE STEPS OF: A. INTRODUCING A HYDROCARBON FEEDSTOCK COMPRISING PETROLEUM RESIDUUM INTO THE CATALYTIC CRACKING ZONE OF A HEAVY OIL CRACKING UNIT IN THE PRESENCE OF FLUIDIZED CRACKING CATALYST AT CRACKING CONDITIONS TO PRODUCE A CATALYTICALLY CRACKED EFFLUENT INCLUDING A CRACKED NAPHTHA FRACTION; B. REGENERATING SAID FLUIDIZED CRACKING CATALYST IN THE REGENERATION ZONE OF THE HEAVY OIL CRACKING UNIT; C. PRODUCING HIGH PRESSURE STEAM IN SAID REGENERATION ZONE BY INDIRECT HEAT EXCHANGE; D. PASSING THE CRACKED NAPHTHA FRACTION TO A THERMAL PYROLYSIS ZONE AND THERMALLY CRACKING SAID FRACTION TO PRODUCE A THERMALLY CRACKED EFFLUENT CONTAINING OLEFINICALLY UNSATURATED HYDROCARBONS; E. EXPANDING SAID HIGH PRESSURE STEAN FROM STEP (C) TO PROVIDE AT LEAST PART OF THE GAS COMPRESSION ENERGY REQUIRED FOR RECOVERY OF THE OLEFINICALLY UNSATURATED HYDROCARBONS; AND F. RECOVERING OLEFINICALLY UNSATURATED HYDROCARBONS.
Claim 2
Dependent Claim
142 words
A PROCESS FOR THE PRODUCTION OF OLEFINICALLY UNSATURATED HYDROCARBONS WHICH COMPRISES THE STEPS OF: A. INTRODUCING A HYDROCARBON FEEDSTOCK COMPRISING PETROLEUM RESIDUUM INTO THE CATALYTIC CRACKING ZONE OF A HEAVY OIL CRACKING UNIT IN THE PRESENCE OF FLUIDIZED CRACKING CATALYST AT CRACKING CONDITIONS TO PRODUCE A CATALYTICALLY CRACKED EFFLUENT INCLUDING A CRACKED NAPHTHA FRACTION; B. REGENERATING SAID FLUIDIZED CRACKING CATALYST IN THE REGENERATION ZONE OF THE HEAVY OIL CRACKING UNIT; C. PRODUCING HIGH PRESSURE STEAM IN SAID REGENERATION ZONE BY INDIRECT HEAT EXCHANGE; D. PASSING THE CRACKED NAPHTHA FRACTION TO A THERMAL PYROLYSIS ZONE AND THERMALLY CRACKING SAID FRACTION TO PRODUCE A THERMALLY CRACKED EFFLUENT CONTAINING OLEFINICALLY UNSATURATED HYDROCARBONS; E. EXPANDING SAID HIGH PRESSURE STEAN FROM STEP (C) TO PROVIDE AT LEAST PART OF THE GAS COMPRESSION ENERGY REQUIRED FOR RECOVERY OF THE OLEFINICALLY UNSATURATED HYDROCARBONS; AND F. RECOVERING OLEFINICALLY UNSATURATED HYDROCARBONS.
Claim 3
Dependent Claim
29 words
The process of claim 1 wherein at least a portion of the expanded high pressure steam is mixed with the cracked naphtha fraction fed to the thermal pyrolysis zone.
Claim 4
Dependent Claim
23 words
The process of claim 1 wherein the catalytic cracking zone includes a transfer line reactor and the cracking catalyst is a zeolite catalyst.
Claim 5
Dependent Claim
17 words
The process of claim 1 wherein the olefinically unsaturated hydrocarbon contain from two to four carbon atoms.
Claim 6
Dependent Claim
13 words
The process of claim 1 wherein the hydrocarbon feedstock is crude petroleum oil.
Claim 7
Dependent Claim
15 words
The process of claim 1 wherein tHe hydrocarbon feedstock is a pertroleum residue containing fraction.
Claim 8
Dependent Claim
17 words
The process of claim 1 wherein the hydrocarbon feedstock is an atmospheric residuum boiling above about 600*F.
Claim 9
Dependent Claim
118 words
AN INTEGRATED PROCESS FOR THE PRODUCTION OF OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS COMPRISING THE STEPS OF: A. INTRODUCING HYDROCARBON FEEDSTOCK CONTAINING PETROLEUM RESIDUUM INTO THE CATALYTIC CRACKING ZONE OF A HEAVY OIL CRACKING UNIT IN THE PRESENCE OF FLUIDIZED CRACKING CATALYST AT CRACKING CONDITIONS TO PRODUCE CATALYTICALLY CRACKED EFFLUENT INCLUDING A CRACKED NAPHTHA FRACTION; B. PASSING THE CRACKED NAPHTHA FRACTION TO A THERMAL PRYROLYSIS ZONE AT THERMAL CRACKING CONDITIONS TO PRODUCE A THERMALLY CRACKED EFFLUENT CONTAINING PYROLYSIS OIL, OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS; C. SEPARTING PYROLYSIS OIL FROM THE THERMALLY CRACKED EFFLUENT; D. PASSING PYROLYSIS OIL TO THE CATALYTIC CRACKING ZONE OF THE HEAVY OIL CRACKING UNIT; AND E. RECOVERING OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS.
Claim 10
Dependent Claim
118 words
AN INTEGRATED PROCESS FOR THE PRODUCTION OF OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS COMPRISING THE STEPS OF: A. INTRODUCING HYDROCARBON FEEDSTOCK CONTAINING PETROLEUM RESIDUUM INTO THE CATALYTIC CRACKING ZONE OF A HEAVY OIL CRACKING UNIT IN THE PRESENCE OF FLUIDIZED CRACKING CATALYST AT CRACKING CONDITIONS TO PRODUCE CATALYTICALLY CRACKED EFFLUENT INCLUDING A CRACKED NAPHTHA FRACTION; B. PASSING THE CRACKED NAPHTHA FRACTION TO A THERMAL PRYROLYSIS ZONE AT THERMAL CRACKING CONDITIONS TO PRODUCE A THERMALLY CRACKED EFFLUENT CONTAINING PYROLYSIS OIL, OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS; C. SEPARTING PYROLYSIS OIL FROM THE THERMALLY CRACKED EFFLUENT; D. PASSING PYROLYSIS OIL TO THE CATALYTIC CRACKING ZONE OF THE HEAVY OIL CRACKING UNIT; AND E. RECOVERING OLEFINICALLY UNSATURATED HYDROCARBONS AND AROMATIC COMPOUNDS.
Claim 11
Dependent Claim
152 words
An integrated process for the production of olefinically unsaturated hydrocarbons comprising the steps of: a. introducing hydrocarbon feedstock containing petroleum residuum into the catalytic cracking zone of a heavy oil cracking unit in the presence of fluidized cracking catalyst to produce a catalytically cracked effluent including a cracked naphtha fraction; b. regenerating said fluidized cracking catalyst in the regeneration zone of a heavy oil cracking unit; c. producing high pressure steam in said regeneration zone by indirect heat exchanage; d. passing the cracked naphtha fraction to a thermal pyrolysis zone to produce a thermally cracked effluent containing olefinically unsaturated hydrocarbons; e. cooling thermally cracked effluent in a quench zone; f. producing high pressure steam in the quench zone by indirect heat exchange; g. exapnding high pressure steam from steps (c) and (f) to provide the gas compression energy required for a recovery of olefinically unsaturated hydrocarbons; and h. recovering olefinically unsaturated hydrocarbons.
Claim 12
Dependent Claim
152 words
An integrated process for the production of olefinically unsaturated hydrocarbons comprising the steps of: a. introducing hydrocarbon feedstock containing petroleum residuum into the catalytic cracking zone of a heavy oil cracking unit in the presence of fluidized cracking catalyst to produce a catalytically cracked effluent including a cracked naphtha fraction; b. regenerating said fluidized cracking catalyst in the regeneration zone of a heavy oil cracking unit; c. producing high pressure steam in said regeneration zone by indirect heat exchanage; d. passing the cracked naphtha fraction to a thermal pyrolysis zone to produce a thermally cracked effluent containing olefinically unsaturated hydrocarbons; e. cooling thermally cracked effluent in a quench zone; f. producing high pressure steam in the quench zone by indirect heat exchange; g. exapnding high pressure steam from steps (c) and (f) to provide the gas compression energy required for a recovery of olefinically unsaturated hydrocarbons; and h. recovering olefinically unsaturated hydrocarbons.
Claim 13
Dependent Claim
23 words
The process of claim 9 wherein a portion of the expanded high pressure steam is passed to the thermal pyrolysis zone as diluent.
Claim 14
Dependent Claim
46 words
The rpocess of claim 9 wherein a. flue gas is recovered from the regeneration zone and passed to a carbon monoxide boiler; b. high pressure steam is produced in the carbon monoxide boiler; and c. high pressure steam is recovered as a product of the process.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1978-01-27 | 1978-07-29 | 1979-01-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-01-27 | 1982-07-29 | 1983-01-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-01-27 | 1986-07-29 | 1987-01-28 | $7700.00 | Window Closed / Lapsed |