Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
198 words
A PROCESS FOR PRODUCING A FUEL OIL, CONTAINING LESS THAN ABOUT 1.0 PERCENT BY WEIGHT OF SULFUR, FROM A SULFUROUS BLACK OIL CHARGE STOCK, WHICH PROCESS COMPRISES THE STEPS OF: A. REACTING SAID CHARGE STOCK WITH AN IMPURE HYDROGEN GAS CONTAINING HYDROGEN SULFIDE, IN A FRIST CATALYSTIC REACTION ZONE, AT DESULFURIZATION CONDITIONS SELECTED TO CONVERT LOWER BOILING SULFUROUS COMPOUNDS INTO HYDROGEN SULFIDE AND HYDROCARBONS; Bo SEPARATING AT LEAST A PORTION OF THE RESULTING FIRST REACTION ZONE EFFLUENT, IN A FRIST SEPARATION ZONE, AT SUBSTANTIALLY THE SAME TEMPERATURE AND PRESSURE, TO PROVIDE A FIRST PRINCIPALLY VAPOROUS PHASE AND A FIRST PRINCIPALLY LIQUID PHASE; C. SEPARATING AT LEAST A PORTION OF SAID FIRST VAPOROUS PHASE, IN A SECOND SEPARATION ZONE, AT SUBSTANTIALLY THE SAME PRESSURE AND A TEMPERATURE IN THE RANGE OF ABOUT 60*F. TO ABOUT 140*F., TO PROVIDE A SECOND PRINCIPALLY VAPOROUS PHASE AND A SECOND PRINCIPALLY LIQUID PHASE; D. REMOVING HYDROGEN SULFIDE FROM SAID SECOND VAPOROUS PHASE, AND REACTING AT LEAST A PORTION OF THE REMAINING RELATIVELY PURE HYDROGEN WITH AT LEAST A PORTION OF SAID PHASE, AND REACTING AT LEAST A PORTION OF SAID DESULFURIZATION CONDITIONS SELECTED TO CONVERT ADDITIONAL SULFUROUS COMPOUNDS INTO HYDROGEN SULFIDE AND HYDROCARBONDS;
Claim 2
Dependent Claim
198 words
A PROCESS FOR PRODUCING A FUEL OIL, CONTAINING LESS THAN ABOUT 1.0 PERCENT BY WEIGHT OF SULFUR, FROM A SULFUROUS BLACK OIL CHARGE STOCK, WHICH PROCESS COMPRISES THE STEPS OF: A. REACTING SAID CHARGE STOCK WITH AN IMPURE HYDROGEN GAS CONTAINING HYDROGEN SULFIDE, IN A FRIST CATALYSTIC REACTION ZONE, AT DESULFURIZATION CONDITIONS SELECTED TO CONVERT LOWER BOILING SULFUROUS COMPOUNDS INTO HYDROGEN SULFIDE AND HYDROCARBONS; Bo SEPARATING AT LEAST A PORTION OF THE RESULTING FIRST REACTION ZONE EFFLUENT, IN A FRIST SEPARATION ZONE, AT SUBSTANTIALLY THE SAME TEMPERATURE AND PRESSURE, TO PROVIDE A FIRST PRINCIPALLY VAPOROUS PHASE AND A FIRST PRINCIPALLY LIQUID PHASE; C. SEPARATING AT LEAST A PORTION OF SAID FIRST VAPOROUS PHASE, IN A SECOND SEPARATION ZONE, AT SUBSTANTIALLY THE SAME PRESSURE AND A TEMPERATURE IN THE RANGE OF ABOUT 60*F. TO ABOUT 140*F., TO PROVIDE A SECOND PRINCIPALLY VAPOROUS PHASE AND A SECOND PRINCIPALLY LIQUID PHASE; D. REMOVING HYDROGEN SULFIDE FROM SAID SECOND VAPOROUS PHASE, AND REACTING AT LEAST A PORTION OF THE REMAINING RELATIVELY PURE HYDROGEN WITH AT LEAST A PORTION OF SAID PHASE, AND REACTING AT LEAST A PORTION OF SAID DESULFURIZATION CONDITIONS SELECTED TO CONVERT ADDITIONAL SULFUROUS COMPOUNDS INTO HYDROGEN SULFIDE AND HYDROCARBONDS;
Claim 3
Dependent Claim
29 words
The process of claim 1 further characterized in that the desulfurization conditions in said first reaction zone include a pressure greater than that imposed upon said second reaction zone.
Claim 4
Dependent Claim
64 words
The process of claim 1 further characterized in that the desulfurization conditions, in said first and second reaction zones include a pressure from about 1,000 to about 3,000 psig., a hydrogen concentration in the range of about 1,000 to about 50, 000 scf./Bbl., a maximum catalyst bed temperature of from 600*F. to about 900*F. and a liquid hourly space velocity of 0.25 to 2.50.
Claim 5
Dependent Claim
25 words
The process of claim 1 further characterized in that at least a portion of said first liquid phase is recycled to said first reaction zone.
Claim 6
Dependent Claim
25 words
The process of claim 1 further characterized in that at least a portion of said third liquid phase is recycled to said second reaction zone.
Claim 7
Dependent Claim
39 words
The process of claim 1 further characterized in that said first and second reaction zones have therein a catalytic composite of a porous carrier material and at least one metallic component from the metals of Groups VI-B and VIII.