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1. A method for generating current from hydrogen sulphide-containing exhaust gases, particularly from the natural gas and petroleum industry, the hydrogen sulphide-containing exhaust gases being delivered to a current generation device and being combusted there, with air being supplied, the energy released during combustion being employed at least partially for current generation,characterized in thata composition of the hydrogen sulphide-containing exhaust gases is measured before combustion and is compared with a stipulated composition or stipulated co...
1. A method for generating current from hydrogen sulphide-containing exhaust gases, particularly from the natural gas and petroleum industry, the hydrogen sulphide-containing exhaust gases being delivered to a current generation device and being combusted there, with air being supplied, the energy released during combustion being employed at least partially for current generation,characterized in thata composition of the hydrogen sulphide-containing exhaust gases is measured before combustion and is compared with a stipulated composition or stipulated composition bandwidth, and, in the event of a deviation from the stipulated composition or composition bandwidth, an additional fraction of one or more gases, which is required for correction, is determined and is admixed to the hydrogen sulphide-containing exhaust gases before combustion;wherein a sulphur dioxide-containing and sulpher trioxide-containing combustion exhaust gases occurring during the combustion of the hydrogen sulphide-containing exhaust gases are delivered for flue gas desulphurization, the flue gas desulphurization giving rise to gypsum which is delivered to a gypsum mill for the production of gypsum products, in particular gypsum plasterboards and/or ready-prepared a gypsum mixtures. 2. The method according to claim 1, characterized in thata combustion temperature of the hydrogen sulphide-containing exhaust gases is at least about 1,300° C. 3. The method according to claim 1, characterized in thatthe current generation device comprises a steam generator which is part of a thermodynamic circuit of a steam power process, which, in turn, comprises a steam turbine following the steam generator and a condenser following the steam turbine, the combustion of the hydrogen sulphide-containing exhaust gases taking place in the steam generator, and the energy released being employed at least partially for steam generation, and current generation being performed by a generator driven by the steam turbine. 4. The method according to claim 3, characterized in thatthe current generation device comprises a gas turbine and/or a gas engine, current generation being performed by a generator driven by the gas turbine and/or by the gas engine. 5. The method according to claim 1, characterized in thatthe stipulated composition or stipulated composition bandwidth of the hydrogen sulphide-containing exhaust gases provides the following fractions as molar percentages:hydrogen sulphide: 1% to 10%, in particular 3% to 7%, about 6%, and/orcarbon dioxide: 10% to 90%, in particular 60% to 70%, about 65%, and/ornitrogen: 0.0% to 2,0%, in particular 0,2% to 0.6%, about 0.4%, and/ormethane: 0.1% to 65%, in particular 12% to 20%, about 16%, and/orethane: 0,1% to 20%, in particular 2% to 8%, about 5%, and/orhydrocarbons (C4 to C9): 0,01% to 40%, in particular 4% to 10%, about 7%. 6. The method according to claim 1, wherein the one or more gases comprise natural gas. 7. The method according to claim 6, characterized in thatthe flue gas desulphurization is multi-stage flue gas desulphurization, comprising a solid-bed reactor for sulphur trioxide separation and a lime scrub for sulphur dioxide separation. 8. The method according to claim 6, characterized in thatthe gypsum mill satisfies demand of the gypsum mill for electrical energy completely or partially from current generation as a result of the combustion of the hydrogen sulphide-containing exhaust gases, and/or the gypsum mill derives a heat demand completely or partially from the combustion gases occurring during combustion of the hydrogen sulphide-containing exhaust gases and/or from a current generation processes, in particular the thermodynamic circuit of the steam power process. 9. An Apparatus for generating current from hydrogen sulphide-containing exhaust gases, particularly from the natural gas and petroleum industry, comprising: a current generation device in which supplied hydrogen sulphide-containing exhaust gases are combusted with air being supplied, the energy released during combustion being employed at least partially for current generation, the current generation device comprising: a measuring device for determining a composition of the hydrogen sulphide-containing exhaust gases before combustion is provided,an evaluation device for comparing the composition determined with a stipulated composition or with a stipulated composition bandwidth is provided,a control device and a supply device for one or more gases, in the event of a deviation, determined by the evaluation device, from the stipulated composition or composition bandwidth, the control device determining an additional fraction of the one or more gases, which is required for correction, and admixing it to the hydrogen sulphide-containing exhaust gases via the supply device before combustion, anda flue gas desulphurization device which purifies sulphur dioxide-containing and sulphur trioxide-containing combustion gases occurring during the combustion of the hydrogen sulphide-containing exhaust gases, gypsum being obtained, and in that the apparatus comprises a gypsum mill which employs the gypsum occurring during flue gas desulphurization for the production of gypsum products, in particular in the production of gypsum plasterboards and/or ready-prepare gypsum mixtures. 10. The apparatus according to claim 9, characterized in thata combustion temperature of the hydrogen sulphide-containing exhaust gases is at least about 1,300° C. 11. The apparatus according to claim 9, characterized in thatthe current generation device comprises a steam generator which is part of a thermodynamic circuit of a steam power process, which, in turn, comprises a steam turbine following the steam generator and a condenser following the steam turbine, the combustion of the hydrogen sulphide-containing exhaust gases taking place in the steam generator, and the energy released being employed at least partially for steam generation, and a generator driven by the steam turbine being provided for current generation. 12. The apparatus according to claim 11, characterized in thatthe current generation device comprises a gas turbine and/or a gas engine, a generator driven by the gas turbine and/or by the gas engine being provided for current generation. 13. The apparatus according to claim 9, characterized in thatthe stipulated composition or stipulated composition bandwidth of the hydrogen sulphide-containing exhaust gases provides the following fractions as molar percentages:hydrogen sulphide: 1% to 10%, in particular 3% to 7%, about 6%, and/orcarbon dioxide: 10% to 90%, in particular 60% to 70%, about 65%, and/ornitrogen: 0.0% to 2.0%, in particular 0.2% to 0.6%, about 0.4%, and/ormethane: 0.1% to 65%, in particular 12% to 20%, about 16%, and/orethane: 0.1% to 20%, in particular 2% to 8%, about 5%, and/orhydrocarbons (C4 to C9): 0.01% to 40%, in particular 4% to 10%, about 7%. 14. The apparatus according to claim 10, wherein the one or more gases comprise natural gas. 15. The apparatus according to claim 14, characterized in thatthe gypsum mill satisfies demand of the gypsum mill for electrical energy completely or partially from current generation as a result of the combustion of the hydrogen sulphide-containing exhaust gases, and/or the gypsum mill derives a heat demand completely or partially from the combustion gases occurring during the combustion of the hydrogen sulphide-containing exhaust gases and/or from a current generation processes, in particular the thermodynamic circuit of the steam power process.