초록 ▼

A method in which an air mass flow supplied to a compressor in a power plant is divided in a flow divider into a small partial flow and into a larger partial flow. The smaller partial flow is supplied to an ejector via an air cooler and a booster. The larger partial flow is supplied to the suction l

A method in which an air mass flow supplied to a compressor in a power plant is divided in a flow divider into a small partial flow and into a larger partial flow. The smaller partial flow is supplied to an ejector via an air cooler and a booster. The larger partial flow is supplied to the suction line of said ejector. Both partial flows are combined in the ejector. The mass flow which is combined at the outlet of the ejector can be used as pressurized air in various components of a power plant.

대표청구항 ▼

1. A method for increasing the pressure of a gas from a compressor with a booster, comprising: subdividing a mass stream of the gas into a relatively smaller part stream and into a relatively larger part stream; cooling the relatively smaller part stream; delivering the relatively smaller part

1. A method for increasing the pressure of a gas from a compressor with a booster, comprising: subdividing a mass stream of the gas into a relatively smaller part stream and into a relatively larger part stream; cooling the relatively smaller part stream; delivering the relatively smaller part stream to an ejector via the booster; and combining the relatively smaller part stream with the relatively larger part stream at the ejector, wherein the relatively larger part stream is supplied to a suction nipple of the ejector and wherein the combined mass stream of the gas is picked up at an outlet of the ejector. 2. The method as claimed in claim 1, wherein the relatively smaller part stream is about 20-40% of the mass stream of the delivered gas. 3. The method as claimed in claim 1, wherein the relatively smaller part stream emerging at the outlet of the booster is smoothed with respect to pressure fluctuations. 4. The method as claimed in claim 1, wherein a pressure difference in the mass stream before subdivision and after combination is about 2 bar. 5. The method as claimed in claim 2, wherein the relatively smaller part stream emerging at the outlet of the booster is smoothed with respect to pressure fluctuations. 6. The method as claimed in claim 2, wherein a pressure difference in the mass stream before subdivision and after combination is about 2 bar. 7. The method as claimed in claim 3, wherein a pressure difference in the mass stream before subdivision and after combination is about 2 bar. 8. The method of claim 1, wherein the gas includes air delivered in a power station. 9. The method as claimed in claim 2, wherein the relatively smaller part stream is about 20% of the mass stream of the delivered gas. 10. A device for increasing pressure of a gas from a compressor with a booster, comprising: a stream divider, via which a mass stream of the gas is adapted to be subdivided into a relatively smaller part stream and a relatively larger part stream; an ejector, to which the relatively smaller part stream is adapted to be delivered by the booster; and a bypass line, via which the relatively larger part stream is adapted to be delivered to a suction nipple of the ejector, wherein the relatively smaller part stream is adapted to be delivered to the booster via an air cooler. 11. The device as claimed in claim 10, wherein the relatively smaller part stream is about 20-40% of the mass stream of the delivered air. 12. The device as claimed in claim 10, wherein the booster is coupled to the ejector via a line, to which a buffer tank is coupled for smoothing of pressure fluctuations. 13. The device as claimed in claim 10, wherein the output of the ejector is coupled to at least one of a device for pressure-type fluidized-bed firing, an after burner and a coal gasifier. 14. A power station, including the device as claimed in claim 10. 15. The device of claim 11, wherein the booster is connected to the ejector via a line to which a buffer tank is connected for smoothing of pressure fluctuations. 16. The device as claimed in claim 11, wherein the relatively smaller part stream is about 20% of the mass stream of the delivered air. 17. The method as claimed in claim 11, wherein the relatively smaller part stream is about 20-40% of the mass stream of the delivered gas. 18. The device as claimed in claim 11, wherein the output of the ejector is coupled to at least one of a device for pressure-type fluidized-bed firing, an after burner and a coal gasifier. 19. The device as claimed in claim 12, wherein the output of the ejector is coupled to at least one of a device for pressure-type fluidized-bed firing, an after burner and a coal gasifier. 20. A power station, including the device as claimed in claim 10, and further including a device for pressure-type fluidized-bed firing and a coal gasifier.