[특허]Method for operating a thermodynamic cycle, and thermodynamic cycle

Kalina Power Limited

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특허 상세정보

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Method for operating a thermodynamic cycle, and thermodynamic cycle

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	F25B-043/00 F01K-025/04 F01K-025/02 F25B-011/02 F01D-015/10 F02C-001/10 F25B-030/02 F01K-025/06
출원번호	US-0865754 (2008-12-03)
등록번호	US-9790815 (2017-10-17)
우선권정보	DE-10 2008 007 249 (2008-02-01); DE-10 2008 045 450 (2008-09-02)
국제출원번호	PCT/EP2008/066673 (2008-12-03)
§371/§102 date	20100802 (20100802)
국제공개번호	WO2009/095127 (2009-08-06)
발명자 / 주소	Lengert, Jörg Lengert, Martina Lutz, Roland
출원인 / 주소	Kalina Power Limited
대리인 / 주소	Sunstone IP
인용정보	피인용 횟수 : 0 인용 특허 : 12

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In a thermodynamic cycle with at least one first heat exchanger for creating a first heated or partially evaporated working medium flow by heating or partially evaporating a liquid working medium flow by heat transmission from an expanded working medium flow; a second heat exchanger for creating a second at least partially evaporated working medium flow; a separator for separating a liquid from a vaporous phase of the second flow; and an expansion device for creating an expanded vaporous phase, pressure pulsations are prevented during the start-up of the cycle in that the vaporous phase separated by the separator is conducted past the expansion device and the first heat exchanger. The liquid phase separated by the separator is cooled in the first heat exchanger by heat transfer to the liquid flow. After the first heat exchanger, the cooled, separated, liquid phase and the separated vaporous phase are brought together.

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1. A method for operating a thermodynamic circuit with at least the following components: a first heat exchanger for producing a first heated or partially vaporized working medium flow by heating or partially vaporizing a pressurized liquid working medium flow received directly from a pump by heat transfer from an expanded working medium flow;a second heat exchanger for producing a second at least partially vaporized working medium flow by at least partially vaporizing or further vaporizing the first working medium flow with heat which is transferred from an external heat source;a third heat exchanger for completely condensing the expanded working medium flow;a first separator for separating a liquid phase from a vapor phase of the second working medium flow;an expansion device for expanding the vapor phase, converting its energy to a usable form, and producing an expanded vapor phase;a first combination point for producing the expanded working medium flow by combining the liquid phase and the expanded vapor phase;a working medium flow homogenizing system arranged between the first heat exchanger and the third heat exchanger, the working medium flow homogenizing system comprising: a second separator configured to separate a liquid phase from a vapor phase of the working medium flow, wherein all of the liquid phase from the second separator enters the third heat exchanger; anda mixer for combining the separated liquid phase and vapor phase output by the second separator in a manner that homogenizes the working medium flow;the method comprising: in order to start the circuit: separating the vapor phase by the first separator, wherein the vapor phase bypasses the expansion device and the first heat exchanger,supplying the liquid phase, which has been separated by the first separator, via the first combination point to the first heat exchanger, where the liquid phase is cooled down by heat transfer to the pressurized liquid working medium flow received directly from the pump, andafter the first heat exchanger, combining the cooled-down separated liquid phase and the separated vapor phase at a second combination point downstream of the first heat exchanger and upstream of working medium flow homogenizing system that is arranged upstream of the third heat exchanger to form a partially-condensed cooled-down working medium flow, such that the working medium flow homogenizing system homogenizes the combined liquid phase and vapor phase of the partially-condensed cooled-down working medium flow, and such that between the first separator and the second combination point, the separated liquid phase passes through the first heat exchanger and the separated vapor phase bypasses both the expansion device and the first heat exchanger; andsupplying the partially-condensed cooled-down working medium flow produced by the working medium flow homogenizing system to the third heat exchanger for completely condensing the working medium flow, and delivering the completely condensed working medium flow to the pump; andafter the circuit has been fully started up, directing the vapor phase to both the first heat exchanger and the expansion device for regular operation without the bypass. 2. The method according to claim 1, wherein a two-substance mixture is used as the working medium. 3. The method according to claim 1, wherein a geothermal liquid is used as the external heat source. 4. The method according to claim 1, wherein the heat source is at a temperature of 100° C. to 200° C. or at a temperature of 100° C. to 140° C. 5. A thermodynamic circuit comprising: a first heat exchanger for producing a first heated or partially vaporized working medium flow by heating or partially vaporizing a pressurized liquid working medium flow received directly from a pump by heat transfer from an expanded working medium flow;a second heat exchanger for producing a second at least partially vaporized working medium flow by at least partially vaporizing or further vaporizing the first working medium flow with heat which is transferred from an external heat source;a third heat exchanger for completely condensing the expanded working medium flow, wherein the completely condensed working medium flow is delivered to the pump;a first separator for separating a liquid phase from a vapor phase of the second working medium flow;an expansion device for expanding the vapor phase, converting its energy to a usable form, and producing an expanded vapor phase;a first combination point for producing the expanded working medium flow by combining the liquid phase and the expanded vapor phase;a working medium flow homogenizing system arranged between the first heat exchanger and the third heat exchanger, the working medium flow homogenizing system comprising: an additional separator configured to separate a liquid phase from a vapor phase of the working medium flow, wherein all of the liquid phase from the additional separator enters the third heat exchanger; anda mixer for combining the separated liquid phase and vapor phase output by the additional separator in a manner that homogenizes the working medium flow; anda valve system configured to be switched between: a first configuration in which the separated liquid phase is routed to bypass the expansion device and pass through the first heat exchanger and the separated vapor phase is routed through the expansion device;a second configuration in which the separated liquid phase is passed through the first heat exchanger, and the separated vapor phase is routed through a bypass line which branches off from a line between the first separator and the expansion device at a branching point, bypasses the expansion device and the first heat exchanger, and opens into a line between the first heat exchanger and the third heat exchanger at a second combination point downstream of the first heat exchanger and upstream of working medium flow homogenizing system to combine with the separated liquid phase heated by the first heat exchanger and form a partially-condensed cooled-down working medium flow, such that downstream of the mixer, the working medium flow homogenizing system homogenizes the combined liquid phase and vapor phase of the partially-condensed cooled-down working medium flow; anda third configuration directing the vapor phase to both the first heat exchanger and the expansion device for regular operation without the bypass after the circuit has been fully started up. 6. The thermodynamic circuit according to claim 5, wherein the working medium consists of a multiple-substance mixture. 7. The thermodynamic circuit according to claim 6, wherein the multiple-substance mixture is a two-substance mixture. 8. The thermodynamic circuit according to claim 5, having a geothermal liquid as the external heat source. 9. The thermodynamic circuit according to claim 5, wherein the external heat source is at a temperature of 100° C. to 200° C. or at a temperature of 100° C. to 140° C. 10. The thermodynamic circuit according to claim 6, wherein the multiple-substance mixture is an ammonia-water mixture. 11. The thermodynamic circuit according to claim 5, having thermal water as the external heat source. 12. The method according to claim 1, wherein an ammonia-water mixture is used as the multiple-substance mixture. 13. The method according to claim 1, wherein thermal water is used as the external heat source. 14. A system for operating a thermodynamic circuit comprising: a first heat exchanger for producing a first heated or partially vaporized working medium flow by heating or partially vaporizing a pressurized liquid working medium flow received directly from a pump by heat transfer from an expanded working medium flow;a second heat exchanger for producing a second at least partially vaporized working medium flow by at least partially vaporizing or further vaporizing the first working medium flow with heat which is transferred from an external heat source;a third heat exchanger for completely condensing the expanded working medium flow, the completely condensed working medium flow being delivered to the pump;a first separator for separating a liquid phase from a vapor phase of the second working medium flow;an expansion device, in particular a turbine, for expanding the vapor phase, converting its energy to a usable form, and producing an expanded vapor phase;a first combination point for producing the expanded working medium flow by combining the liquid phase and the expanded vapor phase;a working medium flow homogenizing system arranged between the first heat exchanger and the third heat exchanger, the working medium flow homogenizing system comprising: an additional separator configured to separate a liquid phase from a vapor phase of the working medium flow, wherein all of the liquid phase from the additional separator enters the third heat exchanger; anda mixer for combining the separated liquid phase and vapor phase output by the additional separator in a manner that homogenizes the working medium flow;wherein the system is configured, in order to start the circuit: to separate the vapor phase by the first separator, wherein the vapor phase bypasses the expansion device and the first heat exchanger,to supply the liquid phase, which has been separated by the first separator, via the first combination point to the first heat exchanger, where the liquid phase is cooled down by heat transfer to the liquid working medium flow, andafter the first heat exchanger, to combine the cooled-down separated liquid phase and the separated vapor phase at a second combination point downstream of the first heat exchanger and upstream of working medium flow homogenizing system that is arranged upstream of the third heat exchanger to form a partially-condensed cooled-down working medium flow, such that the working medium flow homogenizing system homogenizes the combined liquid phase and vapor phase of the partially-condensed cooled-down working medium flow, and such that between the first separator and the second combination point, the separated liquid phase passes through the first heat exchanger and the separated vapor phase bypasses both the expansion device and the first heat exchanger; andwherein the system is configured, after the circuit has been fully started up, to direct the vapor phase to both the first heat exchanger and the expansion device for regular operation without the bypass. 15. The system according to claim 14, wherein a multiple-sub stance mixture is used as the working medium. 16. The method according to claim 14, wherein the heat source is at a temperature of 100° C. to 200° C. or at a temperature of 100° C. to 140° C.

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Method for operating a thermodynamic cycle, and thermodynamic cycle

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Method for operating a thermodynamic cycle, and thermodynamic cycle

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