US2731394A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Conversion of heavy hydrocarbon oils
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1951-05-25
•
Granted: 1956-01-17
•
Expires: 1971-05-25
Abstract
No abstract record available.
Inventors
- 👤 Clark E Adams
- 👤 Robert W Krebs
- 👤 Jr Charles N Kimberlin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 19:40
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/18; B01J8/24; B01J8/26; B01J8/28; C; C10; C10G; C10G11/00; C10G11/14; C10G11/16
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
251 words
IN THE PROCESS OF PRODUCING LOWER BOILING HYDROCARBONS FROM HEAVY HYDROCARBONACEOUS RESIDUES WHICH TEND TO PRODUCE FINELY DIVIDED CONTAMINANTS FOR CATALYST BY COKING SAID RESIDUES IN CONTACT WITH A DENSE, TURBULENT, FLUIDIZED MASS OF CATALYTICALLY SUBSTANTIALLY INERT SOLIDS MAINTAINED AT A COKING TEMPERATURE IN A COKING ZONE AND PASSING THE VOLATILE COKING PRODUCTS INCLUDING ENTRAINED PARTICLES OF HEAVY LIQUID WITHOUT INTERMEDIATE CONDENSATION OF CONSTITUENTS DESIRABLE FOR CRACKING THROUGH A DENSE FLUIDIZED MASS OF CRACKING CATALYST MAINTAINED AT A CRACKING TEMPERATURE, THE IMPROVEMENT WHICH COMPRISES MAINTAINING IN A VERTICAL ELONGATED CONTACTING ZONE A LOWER DENSE FLUIDIZED MASS CATALYTICALLY INERT SOLIDS AT A COKING TEMPERATURE, AN INTERMEDIATE SEPARATE DENSE FLUIDIZED MASS OF CATALYTICALLY INERT SOLIDS WHICH IS MAINTAINED AT A TEMPERATURE NOT EXCEEDING THE COKING TEMPERATURE IN THE LOWER MASS AND SUFFICIENTLY LOW TO COLLECT HIGH BOILING HYDROCARBONS FROM COKED VAPOR PRODUCTS IN SUFFICIENT QUANTITIES TO SEPARATE CATALYST CONTAMINANT MATERIALS FROM SAID VAPOR PRODUCTS BY ADHESION, AND AN UPPER SEPARATE DENSE FLUIDIZED MASS OF CRACKING CATALYST MAINTAINED AT SAID CRACKING TEMPERATURE, FEEDING SAID RESIDUES TO SAID LOWER MASS, PASSING VOLTATILE EFFLUENT OF SAID LOWER MASS IN SERIES UPWARDLY THROUGH SAID INTERMEDIATE AND UPPER MASSES, SEPARATING THE ENTRAINED LIQUID PARTICLES AND FINELY DIVIDED CONTAMINANTS IN SAID INTERMEDIATE MASS BY ADHESION AS AFORESAID, WITHDRAWING CATALYTICALLY CRACKED VOLATILE PRODUCTS FROM SAID UPPER MASS, PASSING SOLIDS FROM SAID INTERMEDIATE MASS TO A SEPARATE RECONDITIONING ZONE, REMOVING CONSTITUENTS UNDESIRABLE IN CATALYTIC CRACKING FROM SAID SOLIDS IN SAID RECONDITIONING ZONE AND RETURNING SOLIDS SO RECONDITIONED TO SAID INTERMEDIATE MASS.
Claim 2
Dependent Claim
251 words
IN THE PROCESS OF PRODUCING LOWER BOILING HYDROCARBONS FROM HEAVY HYDROCARBONACEOUS RESIDUES WHICH TEND TO PRODUCE FINELY DIVIDED CONTAMINANTS FOR CATALYST BY COKING SAID RESIDUES IN CONTACT WITH A DENSE, TURBULENT, FLUIDIZED MASS OF CATALYTICALLY SUBSTANTIALLY INERT SOLIDS MAINTAINED AT A COKING TEMPERATURE IN A COKING ZONE AND PASSING THE VOLATILE COKING PRODUCTS INCLUDING ENTRAINED PARTICLES OF HEAVY LIQUID WITHOUT INTERMEDIATE CONDENSATION OF CONSTITUENTS DESIRABLE FOR CRACKING THROUGH A DENSE FLUIDIZED MASS OF CRACKING CATALYST MAINTAINED AT A CRACKING TEMPERATURE, THE IMPROVEMENT WHICH COMPRISES MAINTAINING IN A VERTICAL ELONGATED CONTACTING ZONE A LOWER DENSE FLUIDIZED MASS CATALYTICALLY INERT SOLIDS AT A COKING TEMPERATURE, AN INTERMEDIATE SEPARATE DENSE FLUIDIZED MASS OF CATALYTICALLY INERT SOLIDS WHICH IS MAINTAINED AT A TEMPERATURE NOT EXCEEDING THE COKING TEMPERATURE IN THE LOWER MASS AND SUFFICIENTLY LOW TO COLLECT HIGH BOILING HYDROCARBONS FROM COKED VAPOR PRODUCTS IN SUFFICIENT QUANTITIES TO SEPARATE CATALYST CONTAMINANT MATERIALS FROM SAID VAPOR PRODUCTS BY ADHESION, AND AN UPPER SEPARATE DENSE FLUIDIZED MASS OF CRACKING CATALYST MAINTAINED AT SAID CRACKING TEMPERATURE, FEEDING SAID RESIDUES TO SAID LOWER MASS, PASSING VOLTATILE EFFLUENT OF SAID LOWER MASS IN SERIES UPWARDLY THROUGH SAID INTERMEDIATE AND UPPER MASSES, SEPARATING THE ENTRAINED LIQUID PARTICLES AND FINELY DIVIDED CONTAMINANTS IN SAID INTERMEDIATE MASS BY ADHESION AS AFORESAID, WITHDRAWING CATALYTICALLY CRACKED VOLATILE PRODUCTS FROM SAID UPPER MASS, PASSING SOLIDS FROM SAID INTERMEDIATE MASS TO A SEPARATE RECONDITIONING ZONE, REMOVING CONSTITUENTS UNDESIRABLE IN CATALYTIC CRACKING FROM SAID SOLIDS IN SAID RECONDITIONING ZONE AND RETURNING SOLIDS SO RECONDITIONED TO SAID INTERMEDIATE MASS.
References Cited (Backward Citations)
US2367351A
Cited
US2388055A
Cited
US2448135A
Cited
US2525925A
Cited
US2548875A
Cited
US2483485A
Cited
US2690990A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1959-01-16 | 1959-07-18 | 1960-01-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1963-01-16 | 1963-07-18 | 1964-01-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1967-01-16 | 1967-07-18 | 1968-01-17 | $7700.00 | Window Closed / Lapsed |