Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
117 words
A low pollution method of burning a fuel, comprising the steps of: (a) passing the fuel into a dense phase fluidized bed of particles which are fluidized by a fluidizing gas substantially free of non-combustible inert components; (b) partially oxidizing the fuel within the dense phase bed at an elevated partial oxidation temperature to produce a combustible gas which has a low content of non-combustible inert components. (c) passing at least some of the combustible gas to a burner; and (d) burning the combustible gas in a flame at the burner with a combustion-supporting gas to which has been added a non-combustible inert gas to suppress or reduce the formation of pollutants in the resulting flue gas.
Claim 2
Dependent Claim
117 words
A low pollution method of burning a fuel, comprising the steps of: (a) passing the fuel into a dense phase fluidized bed of particles which are fluidized by a fluidizing gas substantially free of non-combustible inert components; (b) partially oxidizing the fuel within the dense phase bed at an elevated partial oxidation temperature to produce a combustible gas which has a low content of non-combustible inert components. (c) passing at least some of the combustible gas to a burner; and (d) burning the combustible gas in a flame at the burner with a combustion-supporting gas to which has been added a non-combustible inert gas to suppress or reduce the formation of pollutants in the resulting flue gas.
Claim 3
Dependent Claim
26 words
A method as in claim 1 in which the partial oxidation of step (b) is effected with oxygen and/or steam substantially free of non-combustible inert substances.
Claim 4
Dependent Claim
16 words
A method as in claim 2 in which the oxygen is obtained by separation from air.
Claim 5
Dependent Claim
12 words
A method as in claim 3 where the non-combustible gas is nitrogen.
Claim 6
Dependent Claim
17 words
A method as in claim 4 in which the nitrogen is obtained by separating oxygen from air.
Claim 7
Dependent Claim
71 words
A method as in claim 5 in which oxygen is separated from air by a procedure comprising liquefying the air, and recovering at least some of the heat made available by the air liquefaction procedure in a fluid selected from one or more of the following: water, steam or other fluid passing to a boiler, or at least part of the gas which is employed to convert fuel to combustible gas.
Claim 8
Dependent Claim
144 words
A method as in claim 1 in which the particles in the dense phase fluidized bed include particles comprising reactive calcium sulfate, and in which the fuel is partially oxidized within the bed at an elevated temperature by the transfer to the fuel of oxygen from calcium sulfate, which is thereby reduced to reactive calcium sulfide, contacting particles comprising reactive calcium sulfide in an oxidizing zone with a gas mixture comprising molecular oxygen and at least one gaseous component which is non-combustible and inert at conditions such that at least some reactive calcium sulfide is converted to reactive calcium sulfate which is re-used for the partial oxidation of further amounts of fuel, and such that a substantially oxygen-free non-combustible inert residue gas at an elevated temperature is produced, and employing said residue gas as the non-combustible inert gas in step (d) of claim 1.
Claim 9
Dependent Claim
48 words
A method as in claim 7 in which the residue gas is cooled by heat exchange with a fluid before addition to the combustion supporting gas, and wherein said fluid is selected from at least one of the following: water, steam or other fluid passing to a boiler.
Claim 10
Dependent Claim
47 words
A method as in claim 8 in which the fuel contains chemically-combined sulfur and/or chemically-combined nitrogen, and in which the fluidized bed comprises particles containing reactive calcium oxide which fixes sulfur from the fuel as reactive calcium sulfide to reduce the sulfur content of the combustible gas.
Claim 11
Dependent Claim
118 words
A boiler installation comprising a dense phase fluidized bed fuel conversion zone wherein a fuel is partially oxidized within a dense phase fluidized bed which is fluidized by a fluidizing gas substantially free of non-combustible inert components to form a combustible gas which has a low content of non-combustible inert components; a burner connected to receive combustible gas from the said fuel conversion zone, means operable to provide a supply of non-combustible inert gas, means operable to provide a supply of combustion-supporting gas, and means for conducting a mixture of said non-combustible inert gas and said combustion-supporting gas to the burner to burn the combustible gas in a flame at the burner with a reduced peak flame temperature.
Claim 12
Dependent Claim
118 words
A boiler installation comprising a dense phase fluidized bed fuel conversion zone wherein a fuel is partially oxidized within a dense phase fluidized bed which is fluidized by a fluidizing gas substantially free of non-combustible inert components to form a combustible gas which has a low content of non-combustible inert components; a burner connected to receive combustible gas from the said fuel conversion zone, means operable to provide a supply of non-combustible inert gas, means operable to provide a supply of combustion-supporting gas, and means for conducting a mixture of said non-combustible inert gas and said combustion-supporting gas to the burner to burn the combustible gas in a flame at the burner with a reduced peak flame temperature.
Claim 13
Dependent Claim
37 words
A method as in claim 7 wherein the transfer to the fuel of oxygen from calcium sulfate is conducted in the presence of a mediating gas and/or vapour moiety for mediating and/or promoting the transfer of oxygen.
Claim 14
Dependent Claim
25 words
The method as in claim 11 wherein the mediating gas and/or vapour moiety is selected from the group consisting of CO and H 2 .
Claim 15
Dependent Claim
36 words
A method as in claim 7 wherein the residue gas is cooled by heat exchange with at least a part of the gas mixture which subsequently is utilized for conversion of calcium sulfide to calcium sulfate.
Claim 16
Dependent Claim
44 words
The method of claim 9 wherein particles containing reactive calcium sulfide are fluidized in a regeneration zone at a regeneration temperature by an oxygen-containing gas whereby reactive calcium sulfide is converted to reactive calcium oxide with the liberation of at least one sulfur moiety.
Claim 17
Dependent Claim
24 words
The method of claim 14 wherein calcium oxide is used for fixing sulfur from further amounts of fuel in the dense phase fluidized bed.