US3317419A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Multiple-stage cascade hydrorefining of contaminated charge stocks
Assignee: Universal Oil Products Co
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Filing: 1964-06-01
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Granted: 1967-05-02
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Expires: 1984-06-01
Abstract
No abstract record available.
Inventors
- 👤 John T Fortman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 05:35
CPC Classifications
C; C10; C10G; C10G47/00; C10G65/00; C10G65/02; C10G65/12
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
305 words
A PROCESS FOR HYDROREFINING A HYDROCARBON CHARGE STOCK COMPRISING HYDROCARBON BOILONG ABOVE THE GASOLINE BOILING RANGE, AND CONTAINING A CONTAMINANT SELECTED FROM THE GROUP CONSISTING OF NITROGENOUS COMPOUNDS AND SULFUROUS COMPOUNDS, WHICH PROCESS COMPRISES THE STEPS OF: (A) HYDROCRACKING AND HYDROREFINING SAID CHARGE STOCK IN ADMIXTURE WITH HYRDOGEN AT A TEMPERATURE IN THE RANGE OF FROM ABOUT600*F. TO ABOUT 850*F. IN A FIRST REACTION ZONE CONTAINING A HYDROREFINING CATALYTIC COMPOSITE; (B) SEPARATING THE NORMALLY LIQUID PRODUCT EFFLUENT FROM SAID FIRST REACTION ZONE INTO A FIRST LIGHT FRACTION, HAVING AN END BOILING POINT OF FROM ABOUT 400* F. TO ABOUT 650*F. AND A HEAVIER FRACTION; (C) COMBINING AT LEAST A PORTION OF SAID FIRST LIGHT FRACTION WITH A HYDROCARBON MIXTURE HAVING AN INITIAL BOILING POINT OF FROM ABOUT 300*F. TO ABOUT 450*F. AND CONTAINING AT LEAST ONE OF THE AFORESAID CONTAMINANTS, AND REACTING THE RESULTING MIXTURE WITH HYDROGEN AT A TEMPERATURE WITHIN SAID RANGE IN A SECOND REACTION ZONE CONTAINING A HYDROREFINING CATRALYTIC COMPOSITE AND MAINTAINED UNDER LESS SEVERE CONVERSION CONDITIONS THAN SAID FIRST ZONE; (D) SEPARATING THE NORMALLY LIQUID PRODUCT EFFLUENT FROM SAID SECOND REACTION ZONE INTO A SECOND LIGHT FRACTION, HAVING AN END BOILING POINT WITHIN THE RANGE OF FROM ABOUT 300*F. TO ABOUT 450*F., AND A HYDROREFINED SECOND HEAVY FRACTION; (E) COMBINING AT LEAST A PORTION OF SAID SECOND LIGHT FRACTION WITH A HYDROCARBON MIXTURE, HAVING AN END BOILING POINT OF FROM 300*F. TO ABOUT 450*F. AND CONTAINING AT LEAST ONE OF THE AFORESAID CONTAMINANTS, REACTING THE RESULTING MIXTURE WITH HYDROGEN AT A TEMPERATURE WITHIN SAID RANGE IN A THIRD REACTION ZONE CONTAINING A HYDROREFINING CATALYTIC COMPOSITE AND MAINTAINED UNDER CONDITIONS TO EFFECT HYDROGENATIVE HYDROREFINING OF SAID MIXTURE WITH MINIMUM HYDROCRACKING; AND, (F) SEPARATING THE PRODUCT EFFLUENT FROM SAID THIRD REACTION ZONE INTO A NORMALLY GASEOUS PHASE AND A HYDROREFINED THIRD HEAVY FRACTION.
Claim 2
Dependent Claim
305 words
A PROCESS FOR HYDROREFINING A HYDROCARBON CHARGE STOCK COMPRISING HYDROCARBON BOILONG ABOVE THE GASOLINE BOILING RANGE, AND CONTAINING A CONTAMINANT SELECTED FROM THE GROUP CONSISTING OF NITROGENOUS COMPOUNDS AND SULFUROUS COMPOUNDS, WHICH PROCESS COMPRISES THE STEPS OF: (A) HYDROCRACKING AND HYDROREFINING SAID CHARGE STOCK IN ADMIXTURE WITH HYRDOGEN AT A TEMPERATURE IN THE RANGE OF FROM ABOUT600*F. TO ABOUT 850*F. IN A FIRST REACTION ZONE CONTAINING A HYDROREFINING CATALYTIC COMPOSITE; (B) SEPARATING THE NORMALLY LIQUID PRODUCT EFFLUENT FROM SAID FIRST REACTION ZONE INTO A FIRST LIGHT FRACTION, HAVING AN END BOILING POINT OF FROM ABOUT 400* F. TO ABOUT 650*F. AND A HEAVIER FRACTION; (C) COMBINING AT LEAST A PORTION OF SAID FIRST LIGHT FRACTION WITH A HYDROCARBON MIXTURE HAVING AN INITIAL BOILING POINT OF FROM ABOUT 300*F. TO ABOUT 450*F. AND CONTAINING AT LEAST ONE OF THE AFORESAID CONTAMINANTS, AND REACTING THE RESULTING MIXTURE WITH HYDROGEN AT A TEMPERATURE WITHIN SAID RANGE IN A SECOND REACTION ZONE CONTAINING A HYDROREFINING CATRALYTIC COMPOSITE AND MAINTAINED UNDER LESS SEVERE CONVERSION CONDITIONS THAN SAID FIRST ZONE; (D) SEPARATING THE NORMALLY LIQUID PRODUCT EFFLUENT FROM SAID SECOND REACTION ZONE INTO A SECOND LIGHT FRACTION, HAVING AN END BOILING POINT WITHIN THE RANGE OF FROM ABOUT 300*F. TO ABOUT 450*F., AND A HYDROREFINED SECOND HEAVY FRACTION; (E) COMBINING AT LEAST A PORTION OF SAID SECOND LIGHT FRACTION WITH A HYDROCARBON MIXTURE, HAVING AN END BOILING POINT OF FROM 300*F. TO ABOUT 450*F. AND CONTAINING AT LEAST ONE OF THE AFORESAID CONTAMINANTS, REACTING THE RESULTING MIXTURE WITH HYDROGEN AT A TEMPERATURE WITHIN SAID RANGE IN A THIRD REACTION ZONE CONTAINING A HYDROREFINING CATALYTIC COMPOSITE AND MAINTAINED UNDER CONDITIONS TO EFFECT HYDROGENATIVE HYDROREFINING OF SAID MIXTURE WITH MINIMUM HYDROCRACKING; AND, (F) SEPARATING THE PRODUCT EFFLUENT FROM SAID THIRD REACTION ZONE INTO A NORMALLY GASEOUS PHASE AND A HYDROREFINED THIRD HEAVY FRACTION.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1970-05-01 | 1970-10-31 | 1971-05-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1974-05-01 | 1974-10-31 | 1975-05-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1978-05-01 | 1978-10-31 | 1979-05-02 | $7700.00 | Window Closed / Lapsed |