Claims Analysis
Total Claims: 15
Claim 1
Independent Claim
329 words
A process comprising the steps of: (1) reacting in a free-flow partial oxidation reaction zone a fuel feed selected from the grup consisting of liquid hydrocarbon fuel, solid carbonaceous fuel, and mixtures thereof with a free-oxygen containing gas in the presence of a temperature moderator at a temperature in the range of about 950° C. to 1925° C. and a pressure in the range of about 1 to 250 atmospheres to produce a raw stream of synthesis gas, reducing gas, or fuel gas; wherein said fuel feed contains at least one metal impurity comprising a Group IV A or V A element selected from the group consisting of As, Ge, Sb, Pb, Sn, Si, and mixtures thereof; and said raw gas stream includes H 2 O, entrained matter; and reaction products of said metal impurities; (2) cooling and scrubbing the hot raw gas stream from (1) with water to reduce its temperature to a value in the range of about 50° C. to 300° C. and to remove said entrained matter; wherein said reaction products of said metal impurities are converted into volatile metal hydrides; (3) contacting the raw gas stream from (2) in a gas-solids contacting zone with a solid sorbent material having a minimum surface area of 10 square meters per gram, at a space velocity in the range of about 300 to 20,000 standard cubic feet of gas (dry basis) per lb. of solid material per hour; and decomposing the volatile metal hydrides in said raw gas stream into their elements comprising hydrogen gas and at least one of said Group IV A and V A metals; (4) depositing on said sorbent material the Group IV A or V A metal entrained in the raw gas stream from (3) in elemental form or as the sulfide or oxide; and (5) removing the gas stream from the gas-solids contacting zone in (3) substantially free-from volatile metal hydrides and in admixture with the supplemental hydrogen produced in (3).
Claim 2
Dependent Claim
329 words
A process comprising the steps of: (1) reacting in a free-flow partial oxidation reaction zone a fuel feed selected from the grup consisting of liquid hydrocarbon fuel, solid carbonaceous fuel, and mixtures thereof with a free-oxygen containing gas in the presence of a temperature moderator at a temperature in the range of about 950° C. to 1925° C. and a pressure in the range of about 1 to 250 atmospheres to produce a raw stream of synthesis gas, reducing gas, or fuel gas; wherein said fuel feed contains at least one metal impurity comprising a Group IV A or V A element selected from the group consisting of As, Ge, Sb, Pb, Sn, Si, and mixtures thereof; and said raw gas stream includes H 2 O, entrained matter; and reaction products of said metal impurities; (2) cooling and scrubbing the hot raw gas stream from (1) with water to reduce its temperature to a value in the range of about 50° C. to 300° C. and to remove said entrained matter; wherein said reaction products of said metal impurities are converted into volatile metal hydrides; (3) contacting the raw gas stream from (2) in a gas-solids contacting zone with a solid sorbent material having a minimum surface area of 10 square meters per gram, at a space velocity in the range of about 300 to 20,000 standard cubic feet of gas (dry basis) per lb. of solid material per hour; and decomposing the volatile metal hydrides in said raw gas stream into their elements comprising hydrogen gas and at least one of said Group IV A and V A metals; (4) depositing on said sorbent material the Group IV A or V A metal entrained in the raw gas stream from (3) in elemental form or as the sulfide or oxide; and (5) removing the gas stream from the gas-solids contacting zone in (3) substantially free-from volatile metal hydrides and in admixture with the supplemental hydrogen produced in (3).
Claim 3
Dependent Claim
30 words
The process of claim 1 wherein said volatile metal hydrides produced in (2) are selected from the group consisting of arsine, germane, stibine, lead hydride, stannane, silane, and mixtures thereof.
Claim 4
Dependent Claim
20 words
The process of claim 1 wherein said solid sorbent material in (3) comprises more than 90.0 wt. % of carbon.
Claim 5
Dependent Claim
26 words
The process of claim 1 wherein said solid sorbent material in (3) is selected from the group consisting of charcoal, graphite, activated carbon, and mixtures thereof.
Claim 6
Dependent Claim
42 words
The process of claim 1 wherein the raw gas stream in (3) is dry and the solid sorbent is selected from the group consisting of a carbonaceous material comprising more than 90 wt. % carbon, silica, alumina, silica-aluminas, silica-magnesias, and mixtures thereof.
Claim 7
Dependent Claim
23 words
The process of claim 1 wherein said solid sorbent material in (3) comprises pellets having a diameter of about 1/16 to 3/4 inch.
Claim 8
Dependent Claim
32 words
The process of claim 1 provided with the steps of recovering said Group IV A or V A metal deposited on said solid sorbent material in (4) in a metals recovery zone.
Claim 9
Dependent Claim
30 words
The process of claim 1 wherein the solid sorbent material in (3) is impregnated with a metal from Group IV A or V A of the Periodic Table of Elements.
Claim 10
Dependent Claim
81 words
The process of claim 1 wherein the hot raw gas stream from (1) comprises H 2 , CO, H 2 O; at least one material from the group CO 2 , H 2 S, COS, CH 4 , N 2 , Ar, NH 3 ; at least one material from the group slag, ash, particulate carbon, and unconverted fuel; and at least one reaction product of a metal selected from the group consisting of As, Ge, Sb, Pb, Sn, and Si.
Claim 11
Dependent Claim
24 words
The process of claim 1 where in (3) said raw gas stream from (2) passes up through a fluidized-bed of said solid sorbent material.
Claim 12
Dependent Claim
98 words
The process of claim 1 wherein the gas-solids contacting zone in (3) comprises two beds of said solid sorbent material in series, and a metal selected from the group consisting of antimony, arsenic, tin, lead, and mixtures thereof is removed at a temperature in the range of about 0° C. to 200° C. from the gas stream in the first bed; and a metal selected from the group consisting of silicon, germanium, and mixtures thereof is removed at a temperature in the range of about 200° C. to 350° C. from the gas stream in the second bed.
Claim 13
Dependent Claim
41 words
The process of claim 11 with the additional step of removing acid-gases selected from the group consisting of CO 2 , H 2 S, COS, and mixtures thereof, from the gas stream prior to said gas stream entering said second bed.
Claim 14
Dependent Claim
32 words
The process of claim 1 where the solid sorbent material is contacted in (3) by the raw gas stream at a temperature in the range of about 0° C. to 350° C.
Claim 15
Dependent Claim
31 words
The process of claim 1 where the solid sorbent material is contacted in (3) by the raw gas stream at temperature in the range of about 50° C. to 250° C.