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US3317419A Expired / Lapsed US ⏱️ 0.0 years remaining

Multiple-stage cascade hydrorefining of contaminated charge stocks

Assignee: Universal Oil Products Co
•
Filing: 1964-06-01
•
Granted: 1967-05-02
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Expires: 1984-06-01
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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)

US2587987A Cited
US2773008A Cited
US2951032A Cited
US3133013A Cited

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

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