Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
183 words
Method for simultaneous combustion of refuse and chlorinated hydrocarbons in a single furnace having a refuse combustion chamber (, 3) and a separate incineration cell (5) located within at least a portion of the chamber (, 3) comprising the steps of introducing the chlorinated hydrocarbons into the cell (5) separately and apart from refuse; introducing refuse into the chamber (, 3); incinerating said separate chlorinated hydrocarbons in said incineration cell (5) and whereby chlorinated hydrocarbon combustion gases will be generated; combusting the refuse in the chamber (, 3 ) at a combustion temperature below that of the chlorinated hydrocarbon incinerating temperature and generating refuse combustion gases at a temperature below that of the chlorinated hydrocarbon combustion gases; retaining the chlorinated hydrocarbon combustion gases while flowing in said cell (5) for a dwell time period of at least one second, separate from the refuse combustion gases; then mixing the chlorinated hydrocarbon combustion gases and the cooler refuse combustion gases to cool the chlorinated hydrocarbon combustion gases in the mixture; and then purifying the cooled mixture of refuse combustion gases and chlorinated hydrocarbon combustion gases.
Claim 2
Dependent Claim
183 words
Method for simultaneous combustion of refuse and chlorinated hydrocarbons in a single furnace having a refuse combustion chamber (, 3) and a separate incineration cell (5) located within at least a portion of the chamber (, 3) comprising the steps of introducing the chlorinated hydrocarbons into the cell (5) separately and apart from refuse; introducing refuse into the chamber (, 3); incinerating said separate chlorinated hydrocarbons in said incineration cell (5) and whereby chlorinated hydrocarbon combustion gases will be generated; combusting the refuse in the chamber (, 3 ) at a combustion temperature below that of the chlorinated hydrocarbon incinerating temperature and generating refuse combustion gases at a temperature below that of the chlorinated hydrocarbon combustion gases; retaining the chlorinated hydrocarbon combustion gases while flowing in said cell (5) for a dwell time period of at least one second, separate from the refuse combustion gases; then mixing the chlorinated hydrocarbon combustion gases and the cooler refuse combustion gases to cool the chlorinated hydrocarbon combustion gases in the mixture; and then purifying the cooled mixture of refuse combustion gases and chlorinated hydrocarbon combustion gases.
Claim 3
Dependent Claim
13 words
Method according to claim 1, wherein the purifying step comprises washing with water.
Claim 4
Dependent Claim
19 words
Method according to claim 1, wherein the purifying step comprises reacting the mixture with reactants which bind hydrochloric acid.
Claim 5
Dependent Claim
17 words
Method according to claim 1, further comprising the step of conducting the purified gases to free atmosphere.
Claim 6
Dependent Claim
33 words
Method according to claim 1, further comprising the step of introducing a combustion-supporting fuel into said separate, incineration cell (5) at least upon initiation of burning said separated chlorinated hydrocarbons in said cell.
Claim 7
Dependent Claim
27 words
Method according to claim 5, further comprising the step of controlling the introduction of additional fuel in dependence on sensed temperature within said separate incineration cell (5).
Claim 8
Dependent Claim
33 words
Method according to claim 1, further comprising the step of cooling the mixture of chlorinated hydrocarbon combustion gases and refuse combustion gases obtained by said mixing step before carrying out said purifying step.
Claim 9
Dependent Claim
33 words
Method according to claim 1, further comprising the step of introducing secondary air into the furnace in a region where the chlorinated hydrocarbon combustion gases and the refuse combustion gases are being mixed.
Claim 10
Dependent Claim
45 words
Method according to claim 1, wherein the temperature of combustion of the refuse in the chamber (2, 3) is in the order of about 900° C; and the temperature of incineration of said chlorinated hydrocarbons is in the order of at least about 1200° C.