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US3069349A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon isomerization process

Assignee: Union Oil Company of California
•
Filing: 1958-06-16
•
Granted: 1962-12-18
•
Expires: 1978-06-16
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Abstract

No abstract record available.

Inventors

  • 👤 Henry C Meiners

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 03:53
CPC Classifications
C; C10; C10G; C10G25/00; C10G25/02; C10G25/03; C07; C07C; C07C9/00; C07C9/14; C07C9/16; Y; Y10; Y10S; Y10S585/00; Y10S585/8995; Y10S585/906

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 247 words
THE PROCESS FOR UPGRADING A HYDROCARBON MIXTURE COMPRISING A STRAIGHT-CHAIN AND NON-STRAIGHT-CHAIN HYDROCARBONS BOILING WITHIN THE GASOLINE BOILING RANGE, WHICH COMPRISES (1) CONTACTING SAID MIXTURE IN THE VAPOR PHASE WITH A SOLID GRANULAR LEAN ADSORBENT ESSENTIALLY COMPRISING A PARTIALLY DEHYDRATED ZEOLITIC METALLO ALUMINO SILICATE HAVING PORES OF SUBSTANTIALLY UNIFORM DIAMETER BETWEEN ABOUT 4.5 A. AND ABOUT 5.5 A., SAID CONTACTING BEING EFFECTED AT A TEMPERATURE BELOW ABOUT 800*F. AND UNDER AT LEAST ATMOSPHERIC PRESSURE, WHEREBY THERE IS OBTAINED A RICH ADSORBENT CONTAINING ADSORBED STRAIGHT-CHAIN HYDROCARBON COMPONENTS OF SAID MIXTURE AND A RAFFINATE PRODUCT WHICH IS RICH IN NON-STRAIGHT-CHAIN COMPONENTS OF SAID MIXTURE; (2) SEPARATING SAID RAFFINATE PRODUCT FROM SAID RICH ADSORBENT; (3) REDUCING THE PRESSURE ON SAID RICH ADSORBENT TO A VALUE BETWEEN ABOUT 0.2 P.S.I.A. AND ABOUT 2.0 P.S.I.A. IN THE SUBSTANTIAL ABSENCE OF AN ADDED STRIPPING FLUID, WHEREBY THERE IS PRODUCED A DESORBED EXTRACT GAS COMPRISING DESORBED STRAIGHT-CHAIN HYDROCARBONS AND A PARTIALLY DESORBED ADSORBENT; (4) CONTACTING SAID PARTIALLY DESORBED ADSORBENT WITH HYDROGEN IN AN AMOUNT NO GREATER THAN THAT REQUIRED IN THE ISOMERIZATION OF SUBSEQUENT STEP (6) AND AT A PRESSURE BETWEEN ABOUT 0.2 P.S.I.A. AND ABOUT 2.0 P.S.I.A., WHEREBY THERE IS OBTAINED AT LEAN ADSORBENT AND AN EFFUENT GAS COMPRISING HYDROGEN AND STRAIGHT-CHAIN HYDROCARBONS; (5) ADMIXING SAID HYDROGEN-CONTAINING EFFUENT GAS WITH SAID EXTRACT GAS; AND (6) SUBJECTING THE RESULTING MIXTURE TO ISOMERIZING CONDITIONS IN THE PRESENCE OF AN ISOMERIZATION CATALYST, WHEREBY THE STRAIGHT-CHAIN HYDROCARBON COMPONENTS OF SAID RESULTING MIXTURE ARE ISOMERIZED TO BRANCHED-CHAIN HYDROCARBONS.
Claim 2
Dependent Claim 247 words
THE PROCESS FOR UPGRADING A HYDROCARBON MIXTURE COMPRISING A STRAIGHT-CHAIN AND NON-STRAIGHT-CHAIN HYDROCARBONS BOILING WITHIN THE GASOLINE BOILING RANGE, WHICH COMPRISES (1) CONTACTING SAID MIXTURE IN THE VAPOR PHASE WITH A SOLID GRANULAR LEAN ADSORBENT ESSENTIALLY COMPRISING A PARTIALLY DEHYDRATED ZEOLITIC METALLO ALUMINO SILICATE HAVING PORES OF SUBSTANTIALLY UNIFORM DIAMETER BETWEEN ABOUT 4.5 A. AND ABOUT 5.5 A., SAID CONTACTING BEING EFFECTED AT A TEMPERATURE BELOW ABOUT 800*F. AND UNDER AT LEAST ATMOSPHERIC PRESSURE, WHEREBY THERE IS OBTAINED A RICH ADSORBENT CONTAINING ADSORBED STRAIGHT-CHAIN HYDROCARBON COMPONENTS OF SAID MIXTURE AND A RAFFINATE PRODUCT WHICH IS RICH IN NON-STRAIGHT-CHAIN COMPONENTS OF SAID MIXTURE; (2) SEPARATING SAID RAFFINATE PRODUCT FROM SAID RICH ADSORBENT; (3) REDUCING THE PRESSURE ON SAID RICH ADSORBENT TO A VALUE BETWEEN ABOUT 0.2 P.S.I.A. AND ABOUT 2.0 P.S.I.A. IN THE SUBSTANTIAL ABSENCE OF AN ADDED STRIPPING FLUID, WHEREBY THERE IS PRODUCED A DESORBED EXTRACT GAS COMPRISING DESORBED STRAIGHT-CHAIN HYDROCARBONS AND A PARTIALLY DESORBED ADSORBENT; (4) CONTACTING SAID PARTIALLY DESORBED ADSORBENT WITH HYDROGEN IN AN AMOUNT NO GREATER THAN THAT REQUIRED IN THE ISOMERIZATION OF SUBSEQUENT STEP (6) AND AT A PRESSURE BETWEEN ABOUT 0.2 P.S.I.A. AND ABOUT 2.0 P.S.I.A., WHEREBY THERE IS OBTAINED AT LEAN ADSORBENT AND AN EFFUENT GAS COMPRISING HYDROGEN AND STRAIGHT-CHAIN HYDROCARBONS; (5) ADMIXING SAID HYDROGEN-CONTAINING EFFUENT GAS WITH SAID EXTRACT GAS; AND (6) SUBJECTING THE RESULTING MIXTURE TO ISOMERIZING CONDITIONS IN THE PRESENCE OF AN ISOMERIZATION CATALYST, WHEREBY THE STRAIGHT-CHAIN HYDROCARBON COMPONENTS OF SAID RESULTING MIXTURE ARE ISOMERIZED TO BRANCHED-CHAIN HYDROCARBONS.

References Cited (Backward Citations)

US2859256A Cited
US2859170A Cited
US2818449A Cited
US2886509A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1965-12-17 1966-06-18 1966-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1969-12-17 1970-06-18 1970-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1973-12-17 1974-06-18 1974-12-18 $7700.00 Window Closed / Lapsed

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