초록 ▼

A cogeneration method and device by turbine, particularly by gas turbine, uses a compression section, at least one expansion section, and a combustion chamber. A combustion agent including oxygen is compressed in the compression section; in the combustion chamber, one combustion step is carried out

A cogeneration method and device by turbine, particularly by gas turbine, uses a compression section, at least one expansion section, and a combustion chamber. A combustion agent including oxygen is compressed in the compression section; in the combustion chamber, one combustion step is carried out under pressure with a mixture of combustion agent compressed with a fuel; at least some of the hot gases obtained by pressurized combustion are used to effect an exchange with an external facility; and at least one postcombustion step is carried out of a mixture of hot gases coming from combustion with a fuel, prior to the exchange, and at least one other postcombustion step of a mixture of hot gases, coming from the exchange, with a fuel, in order to obtain hot gases that are sent to the expansion section.

대표청구항 ▼

The invention claimed is: 1. A turbine cogeneration method, by a turbine comprising a compression section, at least first and second expansion sections, and a combustion chamber, wherein the following steps are carried out: (a) a combustion agent including oxygen is compressed in the compression se

The invention claimed is: 1. A turbine cogeneration method, by a turbine comprising a compression section, at least first and second expansion sections, and a combustion chamber, wherein the following steps are carried out: (a) a combustion agent including oxygen is compressed in the compression section; (b) in the combustion chamber, a combustion step is carried out under pressure with a mixture of combustion agent compressed with a fuel; (c) at least some of the hot gas obtained by pressurized combustion is introduced in a first expansion section, (d) one postcombustion step comprising combustion in a first postcombustor immediately downstream, with respect to the flow of gases, of the first expansion section is carried out of a mixture of gas coming from the first expansion section with a fuel, prior to an exchange, (e) at least some of the hot gas obtained by the one postcombustion step is used to effect an heat exchanger provided immediately downstream, with respect to the flow of gases, of the first postcombustor with an external facility, (f) at least one other postcombustion step comprising combustion in a second postcombustor is carried out of a mixture of the hot gas coming from the exchange, with a fuel, in order to obtain hot gas, and (g) the hot gas from the at least one other postcombustion step is sent to a second expansion section. 2. The turbine cogeneration method according to claim 1, characterized in that the at least one other postcombustion step is carried out by introducing a quantity of fuel which is adjusted to obtain a hot gas temperature at the inlet of the expansion section that is substantially close to the initial inlet temperature in the absence of an exchange. 3. The turbine cogeneration method according to claim 1, characterized in that the at least one other postcombustion step is carried out by introducing a quantity of hot gases, which is adjusted to obtain a hot gas temperature at the inlet of the expansion section that is substantially close to the initial inlet temperature in the absence of an exchange. 4. The turbine cogeneration method according to claim 1, characterized in that a steam production operation is carried out by exchange with the external heat exchanger. 5. The turbine cogeneration method according to claim 1, characterized in that a feedstock reforming operation is conducted by exchange with the external heat exchanger. 6. A turbine cogeneration device, comprising a compression section in which a combustion agent including oxygen is compressed, a combustion chamber in which a combustion step is carried out under pressure with a mixture of combustion agent compressed with a fuel, a first expansion section in which at least some of the hot gas obtained from the combustion chamber is introduced, a first postcombustion chamber in which a postcombustion step is carried out of a mixture of gas coming from the first expansion section with a fuel, the first postcombustion chamber being provided immediately downstream, with respect to the flow of gases, of the first expansion section, and a heat exchanger provided immediately downstream, with respect to the flow of gas, of the first postcombustion chamber, for exchanging heat between the hot gases coming from the first postcombustion chamber and a fluid to be heated, at least one other postcombustion chamber in which another postcombustion step is carried out of a mixture of the hot gas coming from the heat exchanger with a fuel, and a second expansion section in which hot gas coming from the at least one other postcombustion chamber is expanded. 7. The cogeneration device according to claim 6, characterized in that the cogeneration device includes a short-circuit pipe for adjusting the hot gas temperature at the outlet of the combustion chamber and/or of the postcombustion chamber. 8. The cogeneration device according to claim 6, characterized in that the heat exchanger includes a reactor. 9. The cogeneration device according to, claim 6, characterized in that the cogeneration device includes a hot gas pipe connecting the first expansion section to the second expansion section.