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US2640802A Expired / Lapsed US ⏱️ 0.0 years remaining

Catalytic desulfurization of petroleum hydrocarbons

Assignee: Anglo Iranian Oil Co Ltd
•
Filing: 1950-11-07
•
Granted: 1953-06-02
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Expires: 1970-11-07
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Abstract

No abstract record available.

Inventors

  • 👤 Porter Frederick Willi Bertram
  • 👤 Northcott Roy Purdy

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 11:28
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/24; C10G2400/00; C10G2400/02

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 307 words
A PROCESS FOR THE HYDROCATALYTIC DESULPHURIZATION OF A SULPHUR-AND-NAPHTHENE CONTAINING CRACKED PETROLEUM NAPHTHA, WHICH PROCESS IS SELFSUPPORTING WITH RESPECT TO THE HYDROGEN NEEDED AND IS PRODUCTIVE OF A DESULPHURIZED CRACKED NAPHTHA HAVING, EXCEPT FOR LOWERED SULPHUR CONTENT, PROPERTIES AND BOILING RANGE SUBSTANTIALLY THE SAME AS THE FEEDSTOCK, COMPRISING THE STEPS OF: PASSING THE SULPHUR-AND-NAPHTHENE CONTAINING CRACKED NAPHTHA AT A SPACE VELOCITY OF FROM ABOUT 0.5 TO ABOUT 1.0 V./V./HR. TO A REACTION ZONE AND CONTACTING THE CRACKED NAPHTHA THEREIN WITH A DEHYDROGENATION-HYDROGENATION CATALYST AND WITH HYDROGEN DERIVED SOLELY FROM THE CRACKED NAPHTHA, SAID CATALYST BEING RESISTANT TO SULPHUR POISONING AND COMBINING ACTIVITY FOR THE DEHYDROGENATION OF NAPHTHENES IN SAID CRACKED NAPHTHA WITH ACTIVITY FOR THE HYDROGENATION OF ORGANICALLY COMBINED SULPHUR IN SAID CRACKED NAPHTHA TO HYDROGEN SULPHIDE; ESTABLISHING A TEMPERATURE IN SAID ZONE IN THE RANGE OF FROM BETWEEN ABOUT 780* F. TO ABOUT 800* F. AT WHICH HYDROGEN IS PRODUCED CONTINUOUSLY FROM SAID CRACKED NAPHTHA; ESTABLISHING A PRESSURE IN SAID ZONE IN THE RANGE OF FROM ABOUT 25 TO ABOUT 75 LBS./SQ. IN. GAUGE, THE TEMPERATURE AND PRESSURE ESTABLISHED WITHIN SAID RANGES BEING CORRELATED TO PROVIDE, FROM THE DEHYDROGENATION OF NAPHTHENES CONTAINED IN SAID CRACKED NAPHTHA, HYDROGEN IN AN AMOUNT AT LEAST EQUAL TO BUT NOT SUBSTANTIALLY IN EXCESS OF THAT REQUIRED TO EFFECT CONVERSION OF SAID ORGANIC SULPHUR COMPOUNDS TO HYDROGEN SULPHIDE AND TO SUPPLY THE HYDROGEN REQUIREMENTS IN SAID REACTION ZONE; SEPARATING A HYDROGEN-RICH GAS MIXTURE FROM THE TREATED PRODUCT, RECYCLING SAID HYDROGEN-RICH GAS MIXTURE TO SAID REACTION ZONE AT A RATE IN THE RANGE OF FROM ABOUT 1000 TO ABOUT 4000 CU. FT./BBL. AT WHICH THE NECESSARY PARTIAL PRESSURE OF HYDROGEN WILL BE MAINTAINED IN SAID ZONE, SAID MIXTURE CONSTITUTING THE WHOLE OF THE HYDROGEN SUPPLIED TO SAID ZONE; AND, RECOVERING THE DESIRED CRACKED NAPHTHA PRODUCT FROM THE RESIDUE OF SAID SEPARATING OPERATION.
Claim 2
Dependent Claim 307 words
A PROCESS FOR THE HYDROCATALYTIC DESULPHURIZATION OF A SULPHUR-AND-NAPHTHENE CONTAINING CRACKED PETROLEUM NAPHTHA, WHICH PROCESS IS SELFSUPPORTING WITH RESPECT TO THE HYDROGEN NEEDED AND IS PRODUCTIVE OF A DESULPHURIZED CRACKED NAPHTHA HAVING, EXCEPT FOR LOWERED SULPHUR CONTENT, PROPERTIES AND BOILING RANGE SUBSTANTIALLY THE SAME AS THE FEEDSTOCK, COMPRISING THE STEPS OF: PASSING THE SULPHUR-AND-NAPHTHENE CONTAINING CRACKED NAPHTHA AT A SPACE VELOCITY OF FROM ABOUT 0.5 TO ABOUT 1.0 V./V./HR. TO A REACTION ZONE AND CONTACTING THE CRACKED NAPHTHA THEREIN WITH A DEHYDROGENATION-HYDROGENATION CATALYST AND WITH HYDROGEN DERIVED SOLELY FROM THE CRACKED NAPHTHA, SAID CATALYST BEING RESISTANT TO SULPHUR POISONING AND COMBINING ACTIVITY FOR THE DEHYDROGENATION OF NAPHTHENES IN SAID CRACKED NAPHTHA WITH ACTIVITY FOR THE HYDROGENATION OF ORGANICALLY COMBINED SULPHUR IN SAID CRACKED NAPHTHA TO HYDROGEN SULPHIDE; ESTABLISHING A TEMPERATURE IN SAID ZONE IN THE RANGE OF FROM BETWEEN ABOUT 780* F. TO ABOUT 800* F. AT WHICH HYDROGEN IS PRODUCED CONTINUOUSLY FROM SAID CRACKED NAPHTHA; ESTABLISHING A PRESSURE IN SAID ZONE IN THE RANGE OF FROM ABOUT 25 TO ABOUT 75 LBS./SQ. IN. GAUGE, THE TEMPERATURE AND PRESSURE ESTABLISHED WITHIN SAID RANGES BEING CORRELATED TO PROVIDE, FROM THE DEHYDROGENATION OF NAPHTHENES CONTAINED IN SAID CRACKED NAPHTHA, HYDROGEN IN AN AMOUNT AT LEAST EQUAL TO BUT NOT SUBSTANTIALLY IN EXCESS OF THAT REQUIRED TO EFFECT CONVERSION OF SAID ORGANIC SULPHUR COMPOUNDS TO HYDROGEN SULPHIDE AND TO SUPPLY THE HYDROGEN REQUIREMENTS IN SAID REACTION ZONE; SEPARATING A HYDROGEN-RICH GAS MIXTURE FROM THE TREATED PRODUCT, RECYCLING SAID HYDROGEN-RICH GAS MIXTURE TO SAID REACTION ZONE AT A RATE IN THE RANGE OF FROM ABOUT 1000 TO ABOUT 4000 CU. FT./BBL. AT WHICH THE NECESSARY PARTIAL PRESSURE OF HYDROGEN WILL BE MAINTAINED IN SAID ZONE, SAID MIXTURE CONSTITUTING THE WHOLE OF THE HYDROGEN SUPPLIED TO SAID ZONE; AND, RECOVERING THE DESIRED CRACKED NAPHTHA PRODUCT FROM THE RESIDUE OF SAID SEPARATING OPERATION.

References Cited (Backward Citations)

US2253308A Cited
US2419029A Cited
US2417308A Cited
US2498559A Cited
US2500146A Cited
US2574446A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1956-06-01 1956-12-01 1957-06-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1960-06-01 1960-12-01 1961-06-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1964-06-01 1964-12-01 1965-06-02 $7700.00 Window Closed / Lapsed

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