US3264209A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Simultaneously coking iron ore and cracking hydrocarbons
Assignee: Phillips Petroleum Co
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Filing: 1962-10-22
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Granted: 1966-08-02
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Expires: 1982-10-22
Abstract
No abstract record available.
Inventors
- 👤 Ii Francis M Files
- 👤 Jr Orvill Horton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 05:53
CPC Classifications
C; C21; C21B; C21B13/00; C21B13/0033; C10; C10G; C10G11/00; C10G11/14; C10G11/18
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
242 words
A PROCESS FOR SIMULTANEOUSLY UPGRADING HYDROCARBONS, PRODUCING COKE, AND COKING IRON ORE WHICH COMPRISES THE STEPS OF: (1) COMMINUTING SAID IRON ORE TO A PARTICLE SIZE SUITABLE FOR FLUIDIZING WITH A GAS; (2) PASSING COMMINUTED ORE FROM STEP (1) TO AT LEAST ONE OF A FLUIDIZED-BED HYDROCARBON CRACKING ZONE AND A FLUIDIZED BED BURNING ZONE; (3) PASSING SEPARATE STREAMS OF HEAVY, COKE-FORMING HYDROCARBON OIL AND HOT IRON ORE INTO SAID CRACKING ZONE AND CONTAINING SAID OIL AND IRON ORE THEREIN UNDER CRACKING AND COKING CONDITIONS INCLUDING A TEMPERATURE IN THE RANGE OF 900 TO 1000*F. SO AS TO CRACK SAID OIL AND LAY DOWN COKE ON SAID IRON ORE; (4) RECOVERING CRACKED HYDROCARBONS FROM STEP (3) AS A PRODUCT; (5) PASSING COKE-ORE FROM STEP (3) TO THE BURNING ZONE OF STEP (2) AND BURNING A PORTION OF THE COKE THEREFROM WITH O2-CONTAINING GAS TO RAISE THE TEMPERATURE TURE OF SAID ORE TO THE RANGE OF 1000 TO 1200*F. AND SUBSTANTIALLY ABOVE SAID CRACKING TEMPERATURE AND TO PARTIALLY REDUCE SAME; (6) PASSING A PORTION OF THE HOT ORE FROM STEP (5) TO STEP (3) TO MAINTAIN SAID CRACKING TEMPERATURE AND CATALYZE THE CRACKING REACTION; (7) CONTACTING ORE FROM STEP (1) WITH A SUBSTANTIAL PORTION OF THE HOT OFF-GAS FROM STEP (5) TO SUBSTANTIALLY PREHEAT SAME PRIOR TO STEP (3 2 (8) PASSING A PORTION OF THE COKED AND PARTIALLY REDUCED ORE FROM STEP (5) TO AN ORE REDUCTION FURNACE TO PRODUCE PIG IRON.
Claim 2
Dependent Claim
242 words
A PROCESS FOR SIMULTANEOUSLY UPGRADING HYDROCARBONS, PRODUCING COKE, AND COKING IRON ORE WHICH COMPRISES THE STEPS OF: (1) COMMINUTING SAID IRON ORE TO A PARTICLE SIZE SUITABLE FOR FLUIDIZING WITH A GAS; (2) PASSING COMMINUTED ORE FROM STEP (1) TO AT LEAST ONE OF A FLUIDIZED-BED HYDROCARBON CRACKING ZONE AND A FLUIDIZED BED BURNING ZONE; (3) PASSING SEPARATE STREAMS OF HEAVY, COKE-FORMING HYDROCARBON OIL AND HOT IRON ORE INTO SAID CRACKING ZONE AND CONTAINING SAID OIL AND IRON ORE THEREIN UNDER CRACKING AND COKING CONDITIONS INCLUDING A TEMPERATURE IN THE RANGE OF 900 TO 1000*F. SO AS TO CRACK SAID OIL AND LAY DOWN COKE ON SAID IRON ORE; (4) RECOVERING CRACKED HYDROCARBONS FROM STEP (3) AS A PRODUCT; (5) PASSING COKE-ORE FROM STEP (3) TO THE BURNING ZONE OF STEP (2) AND BURNING A PORTION OF THE COKE THEREFROM WITH O2-CONTAINING GAS TO RAISE THE TEMPERATURE TURE OF SAID ORE TO THE RANGE OF 1000 TO 1200*F. AND SUBSTANTIALLY ABOVE SAID CRACKING TEMPERATURE AND TO PARTIALLY REDUCE SAME; (6) PASSING A PORTION OF THE HOT ORE FROM STEP (5) TO STEP (3) TO MAINTAIN SAID CRACKING TEMPERATURE AND CATALYZE THE CRACKING REACTION; (7) CONTACTING ORE FROM STEP (1) WITH A SUBSTANTIAL PORTION OF THE HOT OFF-GAS FROM STEP (5) TO SUBSTANTIALLY PREHEAT SAME PRIOR TO STEP (3 2 (8) PASSING A PORTION OF THE COKED AND PARTIALLY REDUCED ORE FROM STEP (5) TO AN ORE REDUCTION FURNACE TO PRODUCE PIG IRON.
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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) | 1969-08-01 | 1970-01-31 | 1970-08-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1973-08-01 | 1974-01-31 | 1974-08-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1977-08-01 | 1978-01-31 | 1978-08-02 | $7700.00 | Window Closed / Lapsed |