WO2020248591A1 - Reverse single-working-media steam combined cycle - Google Patents
Reverse single-working-media steam combined cycle Download PDFInfo
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- WO2020248591A1 WO2020248591A1 PCT/CN2020/000135 CN2020000135W WO2020248591A1 WO 2020248591 A1 WO2020248591 A1 WO 2020248591A1 CN 2020000135 W CN2020000135 W CN 2020000135W WO 2020248591 A1 WO2020248591 A1 WO 2020248591A1
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- working fluid
- kilogram
- endothermic
- exothermic
- boosting
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
- F25B1/10—Compression machines, plants or systems with non-reversible cycle with multi-stage compression
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
- F01K11/02—Plants characterised by the engines being structurally combined with boilers or condensers the engines being turbines
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B31/00—Compressor arrangements
- F25B31/006—Cooling of compressor or motor
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/07—Details of compressors or related parts
- F25B2400/075—Details of compressors or related parts with parallel compressors
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B6/00—Compression machines, plants or systems, with several condenser circuits
- F25B6/02—Compression machines, plants or systems, with several condenser circuits arranged in parallel
Definitions
- the invention belongs to the technical fields of thermodynamics, refrigeration and heat pumps.
- Cold demand, heat demand, and power demand are common in human life and production; among them, the use of mechanical energy to convert heat energy is an important way to achieve cooling and efficient heating. Under normal circumstances, the temperature of the cooling medium changes during cooling, and the temperature of the heated medium often changes during heating. When using mechanical energy to heat, the heated medium often has the dual characteristics of variable temperature and high temperature at the same time, which makes the use of a single The thermal cycle theory realizes the unreasonable performance index for cooling or heating; these problems are-unreasonable performance index, low heating parameters, high compression ratio, and too much working pressure.
- the main purpose of the present invention is to provide a reverse single working fluid steam combined cycle.
- the specific content of the invention is described as follows:
- Reverse single working fluid steam combined cycle refers to the working fluid consisting of M 1 kg and M 2 kg, which are carried out separately or together in eight processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Mass pressure boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, (M 1 +M 2 ) kg working fluid exothermic process 56 , M 2 kg working fluid depressurization process 63, M 1 kg working fluid exothermic condensation process 67, M 1 kg working fluid depressurization process 71-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the nine processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Mass pressure boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid Mass depressurization process 63, M 1 kg working fluid boost process 57, M 1 kg working fluid exothermic condensation process 78, M 1 kg working fluid depressurization process 81-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the nine processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Mass pressure boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid 67, M 2 kg working fluid depressurization process 73, M 1 kg working fluid exothermic condensation process 58, M 1 kg working fluid depressurization process 81-a closed process composed of.
- Reverse single working fluid steam combined cycle refers to ten processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 + M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid endothermic process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid exothermic process 67 , M 2 kg working fluid depressurization process 76, M 1 kg working fluid boosting process 48, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid depressurizing process 91-a closed process composed of.
- Reverse single working fluid steam combined cycle refers to ten processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid depressurizing process 63 , M 1 kg working fluid endothermic process 47, M 1 kg working fluid boosting process 78, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid depressurizing process 91-a closed process composed of.
- Reverse single working fluid steam combined cycle refers to the eleven processes that are composed of M 1 kg and M 2 kg, which are carried out separately or jointly or partially-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid boosting process 23, (M 1 +M 2 ) kg working fluid heat absorption process 34, (M 1 +M 2 -X) kg working fluid heat absorption process 45, (M 1 +M 2 -X) Kilogram working fluid boost process 56, (M 1 +M 2 -X) kilogram working fluid heat release process 67, X kilogram working fluid boost process 47, (M 1 +M 2 ) kg working fluid heat release process 78, M 2 kg working fluid depressurization process 83, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid depressurization process 91-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kg and M 2 kg, and ten processes which are carried out separately or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Mass pressure boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, (M 1 +M 2 ) kg working fluid exothermic process 56 , M 2 kg working fluid pressure reduction process 6a, M 2 kg working fluid heat absorption process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid exothermic condensation process 67, M 1 kg working fluid pressure reduction process 71—The closing process of composition.
- Reverse single working fluid steam combined cycle refers to eleven processes composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg Working fluid depressurization process 6a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid depressurizing process b3, M 1 kg working fluid boosting process 57, M 1 kg working fluid exothermic condensation process 78, M 1 Pressure reduction process of kilogram working fluid 81-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to eleven processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid boosting process 56, M 2 kg Working fluid exothermic process 67, M 2 kg working fluid depressurization process 7a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid depressurization process b3, M 1 kg working fluid exothermic condensation process 58, M 1 Pressure reduction process of kilogram working fluid 81-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid endothermic process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid exothermic process 67, M 2 kg working fluid depressurization process 7a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid depressurization process b3, M 1 kg working fluid boosting process 48, M 1 kg working fluid exothermic condensation Process 89, M 1 kg of working fluid pressure reduction process 91-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluids consisting of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid depressurizing process 6a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid heat absorption process 47, M 1 kg working fluid boost process 78, M 1 kg working fluid exothermic condensation Process 89, M 1 kg of working fluid pressure reduction process 91-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to thirteen processes composed of M 1 kg and M 2 kg, which are carried out separately or jointly or partially-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid boosting process 23, (M 1 +M 2 ) kg working fluid heat absorption process 34, (M 1 +M 2 -X) kg working fluid heat absorption process 45, (M 1 +M 2 -X) Kilogram working fluid boost process 56, (M 1 +M 2 -X) kilogram working fluid heat release process 67, X kilogram working fluid boost process 47, (M 1 +M 2 ) kg working fluid heat release process 78, M 2 kg working fluid pressure reduction process 8a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid pressure reduction process 91— -The closing process of the composition.
- Reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, (M 1 +M 2 ) kg working fluid exothermic process 56, (M 2 -M) kg working fluid pressure reduction process 6t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid exothermic condensation process 6r, M kg working fluid pressure reduction process rs, M kg working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r7, M 1 kg working fluid depressurization process 71-a closed process composed of.
- Reverse single working fluid steam combined cycle refers to 13 processes consisting of M 1 kg and M 2 kg, respectively or together-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boost process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boost process 45, (M 2 -M) kilogram working fluid heat release process 56 , (M 2 -M) kg working fluid pressure reduction process 6t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid pressure increase process 57, (M 1 +M) kg working fluid heat release Condensation process 7r, M kg working fluid depressurization process rs, M kg working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r8, M 1 kg working fluid depressurization process 81-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to 13 processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boost process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boost process 45, (M 2 -M) kilogram working fluid boost process 56 , (M 2 -M) kg working fluid heat release process 67, (M 2 -M) kg working fluid pressure reduction process 7t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid heat release Condensation process 5r, M kilogram working fluid depressurization process rs, M kilogram working fluid endothermic vaporization process st, M 1 kilogram working fluid exothermic process r8, M 1 kilogram working fluid depressurization process 81-a closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or together in 14 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boost process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 2 -M) kilogram working fluid endothermic process 45, (M 2 -M) kilogram working fluid boost process 56, (M 2 -M) Kilogram working fluid exothermic process 67, (M 2 -M) Kilogram working fluid pressure reduction process 7t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) Kilogram working fluid pressure increase process 48, (M 1 +M) kg working fluid exothermic condensation process 8r, M kg working fluid pressure reduction process rs, M kg working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r9, M 1 kg working fluid Quality reduction process 91-the closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kg and M 2 kg, which are carried out separately or together in 14 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 2 -M) kilogram working fluid boosting process 45, (M 2 -M) kilogram working fluid exothermic process 56, (M 2 -M) kg working fluid pressure reduction process 6t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid heat absorption process 47, (M 1 +M) kg working fluid pressure increase process 78, (M 1 +M) kg working fluid exothermic condensation process 8r, M kg working fluid pressure reduction process rs, M kg working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r9, M 1 kg working fluid Quality reduction process 91-the closed process of composition.
- Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kilogram and M 2 kilograms, and fifteen processes that are carried out separately or jointly or partially-M 1 kilogram of working fluid endothermic vaporization process 12, M 1 kg working fluid boosting process 23, (M 1 +M 2 ) kg working fluid heat absorption process 34, (M 1 +M 2 -X) kg working fluid heat absorption process 45, (M 1 +M 2 -X) Kilogram working fluid boost process 56, (M 1 +M 2 -X) kilogram working fluid heat release process 67, X kilogram working fluid boost process 47, (M 1 +M 2 ) kg working fluid heat release process 78, ( M 2 -M) kg working fluid pressure reduction process 8t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid exothermic condensation process 8r, M kg working fluid pressure reduction process rs, M kg working fluid mass endothermic vaporization st, M 1 kilogram refrigerant exothermic process r9, M 1 kilogram working medium composed of depress
- a reverse single working fluid steam combined cycle is a reverse single working fluid steam combined cycle of any one of claims 1-18, in which the "M 1 kg working fluid boost process 23" is changed to " The pressure increase process of M 1 kg of working fluid is 2z, and the heat absorption process of M 1 kg of working fluid is z3", and the reverse single working fluid steam combined cycle is obtained.
- Fig. 1/19 is an example diagram of the first principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 2/19 is an example diagram of the second principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 3/19 is an example diagram of the third principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 4/19 is an example diagram of the fourth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 5/19 is an example diagram of the fifth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Fig. 6/19 is an example diagram of the sixth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 7/19 is an example diagram of the seventh principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 8/19 is an example diagram of the eighth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 9/19 is an example diagram of the ninth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 10/19 is an example diagram of the tenth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 11/19 is an example diagram of the eleventh principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 12/19 is an example diagram of the twelfth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 13/19 is an example diagram of the thirteenth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Fig. 14/19 is an example diagram of the 14th principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 15/19 is an example diagram of the 15th principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 16/19 is an example diagram of the sixteenth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Fig. 17/19 is an example diagram of the 17th principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 18/19 is an example diagram of the eighteenth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Figure 19/19 is an example diagram of the nineteenth principle flow chart of the reverse single working fluid steam combined cycle provided by the present invention.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Kilogram working fluid pressure rise process 45, (M 1 +M 2 ) kilogram working fluid exothermic cooling process 56, M 2 kilogram working fluid depressurization expansion process 63, M 1 kg working fluid exothermic cooling, liquefaction and condensate release Thermal cooling process 67, M 1 kg working fluid condensate pressure reduction process 71-a total of 8 processes.
- (M 1 +M 2 ) kilogram of working fluid is used for 56 process heat release for the heated medium, or at the same time for the heated medium and (M 1 +M 2 ) kilogram of working fluid.
- 34 process heat demand (regeneration) M 1 kg of working fluid for 67 process heat is mainly used for (M 1 +M 2 ) kg of working fluid to complete 34 process heat demand, or at the same time for the heated medium and (M 1 + M 2 ) Kilogram of working fluid completes 34 process heat requirements.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source; (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is met by reheating, or all of it is met by reheating.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Pressure increasing process of kilogram working fluid 45, M 2 kilogram working fluid exothermic cooling process 56, M 2 kilogram working fluid depressurizing expansion process 63, M 1 kilogram working fluid increasing pressure and heating process 57, M 1 kilogram working fluid exothermic cooling process , Liquefaction and condensate exothermic cooling process 78, M 1 kg working fluid condensate pressure reduction process 81-a total of 9 processes.
- M 2 kg of working fluid carries out the heat release of 56 process
- M 1 kilogram of working fluid carries out the heat release of 78 process.
- the high temperature part is generally used for the heated medium
- the low temperature part is generally used for (M 1 +M 2 )
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source; (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is met by reheating, or all of it is met by reheating.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, (M 1 + M 2 ) kg of working fluid for 45 processes and M 1 kg of working fluid for 57 processes are generally completed by compressors and require mechanical energy; M 2 kg
- the process of 63 working fluid is completed by an expander and provides mechanical energy.
- the pressure reduction process of M 1 kg working fluid 81 can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (cycle net work ) Provided from the outside to form a reverse single working substance steam combined cycle.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Kilogram working fluid pressure rise process 45, M 2 kilogram working fluid pressure rise process 56, M 2 kilogram working fluid heat release process 67, M 2 kilogram working fluid pressure drop expansion process 73, M 1 kg working fluid heat release and cooling process , Liquefaction and condensate exothermic cooling process 58, M 1 kg working fluid condensate pressure reduction process 81-a total of 9 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source; (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is met by reheating, or all of it is met by reheating.
- 3Energy conversion process-M 1 kg working fluid for 23 processes, (M 1 + M 2 ) kg working fluid for 45 processes and M 2 kg working fluid for 56 processes are generally completed by compressors, requiring mechanical energy; M 2 kg
- the process of working fluid 73 is completed by an expander and provides mechanical energy.
- the pressure reduction process of M 1 kg of working fluid 81 can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (net cycle net work) ) Provided from the outside to form a reverse single working substance steam combined cycle.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, M 2 kg working fluid endothermic process Heating process 45, M 2 kg working fluid boosting and heating process 56, M 2 kg working fluid exothermic cooling process 67, M 2 kg working fluid depressurizing expansion process 73, M 1 kg working fluid boosting and heating process 48, M 1 Kilogram working fluid exothermic cooling, liquefaction and condensate cooling process 89, M 1 kg working fluid condensate pressure reduction process 91-a total of 10 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low-temperature heat load and part of it is met by regenerative heating, or all is met by regenerative heating; the heat demand of 45 process with M 2 kg working fluid can be met by regenerative heating.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, M 1 kg of working fluid for 48 processes and M 2 kg of working fluid for 56 processes are generally completed by compressors and require mechanical energy; M 2 kg of working fluid for 73 processes
- the expander completes and provides mechanical energy.
- the pressure reduction process 91 of M 1 kg of working fluid can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure-boosting work, and the insufficient part (the net cycle power) is provided by the outside. Form a reverse single working substance steam combined cycle.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, M 2 kg working fluid boosting process Heating process 45, M 2 kg working fluid exothermic cooling process 56, M 2 kg working fluid depressurizing expansion process 63, M 1 kg working fluid endothermic heating process 47, M 1 kg working fluid pressure increasing process 78, M 1 Kilogram working fluid exothermic cooling, liquefaction and condensate cooling process 89, M 1 kg working fluid condensate pressure reduction process 91-a total of 10 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source; (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be portion for obtaining low heat load portion to meet the recuperator or regenerator is satisfied by all; M 1 kilogram working fluid 47 needs heat process, the regenerator can be met.
- 3Energy conversion process-M 1 kg working fluid for 23 processes, M 1 kg working fluid for 78 processes and M 2 kg working fluid for 45 processes are generally completed by compressors and require mechanical energy; M 2 kg working fluid for 63 processes
- the expander completes and provides mechanical energy.
- the pressure reduction process 91 of M 1 kg of working fluid can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure-boosting work, and the insufficient part (the net cycle power) is provided by the outside. Form a reverse single working substance steam combined cycle.
- the working medium is carried out-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure increasing process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, (M 1 +M 2- X) Kilogram working fluid endothermic heating process 45, (M 1 +M 2 -X) kilogram working fluid boosting and heating process 56, (M 1 +M 2 -X) kilogram working fluid exothermic and cooling process 67, X kg working fluid Pressure increasing process 47, (M 1 + M 2 ) kg working fluid exothermic cooling process 78, M 2 kg working fluid depressurization expansion process 83, M 1 kg working fluid exothermic cooling, liquefaction and condensate cooling Process 89, M 1 kg of working fluid condensate pressure reduction process 91-a total of 11 processes.
- M 1 kg of working fluid is used for 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid is used for 34 processes of heat absorption.
- (M 1 +M 2 -X) kg of working fluid undergoes 45 process heat absorption, which can be partly used to obtain low-temperature heat load. Part of it is met by reheating, or all of it is met by reheating.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Pressure rise process of kilogram working fluid 45, (M 1 +M 2 ) kilogram working fluid exothermic cooling process 56, M 2 kilogram working fluid depressurization expansion process 6a, M 2 kilogram working fluid endothermic heating up ab, M 2 kilogram working fluid Mass depressurization expansion process b3, M 1 kg working fluid exothermic cooling, liquefaction and condensate exothermic cooling process 67, M 1 kg working fluid condensate depressurization process 71-a total of 10 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the ab process of the M 2 kg working fluid can be satisfied by the regenerative heat or an external heat source.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Pressure increasing process of kilogram working fluid 45, M 2 kilogram working fluid exothermic cooling process 56, M 2 kilogram working fluid depressurizing expansion process 6a, M 2 kilogram working fluid endothermic heating up ab, M 2 kilogram working fluid depressurizing expansion process b3, M 1 kg working fluid pressure increasing process 57, M 1 kg working fluid exothermic cooling, liquefaction and condensate exothermic cooling process 78, M 1 kg working fluid condensate depressurizing process 81-a total of 11 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the ab process of the M 2 kg working fluid can be satisfied by the regenerative heat or an external heat source.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, (M 1 + M 2 ) kg of working fluid for 45 processes and M 1 kg of working fluid for 57 processes are generally completed by compressors and require mechanical energy; M 2 kg for working medium 6a, b3 to complete the process by the expander and provides mechanical energy, M 1 kilogram depressurisation of the working fluid 81 may be a turbine or a throttle valve is completed; buck boost expansion work is smaller than power consumption, the shortage (cycle Net work) is provided by the outside, forming a reverse single working fluid steam combined cycle.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Kilogram working fluid pressure rise process 45, M 2 kilogram working fluid pressure rise process 56, M 2 kilogram working fluid exothermic cooling process 67, M 2 kilogram working fluid depressurization expansion process 7a, M 2 kilogram working fluid endothermic and warm up ab, M 2 kg of working fluid depressurization and expansion process b3, M 1 kg of working fluid exothermic cooling, liquefaction and condensate exothermic cooling process 58, M 1 kg of working fluid condensate depressurization process 81-a total of 11 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the ab process of the M 2 kg working fluid can be satisfied by the regenerative heat or an external heat source.
- 3Energy conversion process-M 1 kg working fluid for 23 processes, (M 1 + M 2 ) kg working fluid for 45 processes and M 2 kg working fluid for 56 processes are generally completed by compressors, requiring mechanical energy; M 2 kg
- the process 7a, b3 of the working fluid is completed by the expander and provides mechanical energy.
- the pressure reduction process 81 of the M 1 kg working fluid can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (cycle Net work) is provided by the outside, forming a reverse single working fluid steam combined cycle.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, M 2 kg working fluid endothermic process Heating process 45, M 2 kg working fluid boosting and heating process 56, M 2 kg working fluid exothermic cooling process 67, M 2 kg working fluid depressurizing expansion process 7a, M 2 kg working fluid endothermic heating up ab, M 2 kg Working fluid depressurization and expansion process b3, M 1 kg working fluid pressure increase and temperature rise process 48, M 1 kg working fluid heat release and cooling, liquefaction and condensate heat release and cooling process 89, M 1 kg working fluid condensate depressurization process 91— -A total of 12 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low-temperature heat load and part of it is met by regenerative heat, or all is met by regenerative heat; the heat demand of M 2 kg of working fluid for 45 process can be met by regenerative heat;
- M 2 kg of working fluid is used for ab process Heat absorption is generally satisfied by heat recovery or by an external heat source.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, M 1 kg of working fluid for 48 processes, and M 2 kg of working fluid for 56 processes are generally completed by compressors and require mechanical energy; M 2 kilograms of working fluid for 7a,
- the b3 process is completed by an expander and provides mechanical energy.
- the pressure reduction process 91 of M 1 kg of working fluid can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure-boosting work, and the shortfall (net cycle power) is external Provided to form a reverse single working substance steam combined cycle.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, M 2 kg working fluid boosting process Heating process 45, M 2 kg working fluid exothermic cooling process 56, M 2 kg working fluid depressurizing expansion process 6a, M 2 kg working fluid endothermic heating up ab, M 2 kg working fluid depressurizing expansion process b3, M 1 kg Working fluid endothermic heating process 47, M 1 kg working fluid pressure increasing process 78, M 1 kg working fluid exothermic cooling, liquefaction, and condensate cooling process 89, M 1 kg working fluid condensate pressure reduction process 91— -A total of 12 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low-temperature heat load and part of it is met by regenerative heat, or all is met by regenerative heat; the heat demand of M 1 kg of working fluid for 47 process can be met by regenerative heat;
- M 2 kg of working fluid is used for ab process Heat absorption is generally satisfied by heat recovery or by an external heat source.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, M 1 kg of working fluid for 78 processes, and M 2 kg of working fluid for 45 processes are generally completed by compressors and require mechanical energy; M 2 kg of working fluid is performed for 6a,
- the b3 process is completed by an expander and provides mechanical energy.
- the pressure reduction process 91 of M 1 kg of working fluid can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure-boosting work, and the shortfall (net cycle power) is external Provided to form a reverse single working substance steam combined cycle.
- the working medium is carried out-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure increasing process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, (M 1 +M 2- X) Kilogram working fluid endothermic heating process 45, (M 1 +M 2 -X) kilogram working fluid boosting and heating process 56, (M 1 +M 2 -X) kilogram working fluid exothermic and cooling process 67, X kg working fluid
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- M 1 +M 2 kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low temperature heat load and part of it is satisfied by regenerative heat, or all is satisfied by regenerative heat;
- M 1 +M 2 -X kilogram of working fluid undergoes 45 process heat absorption, which can be partially used to obtain low temperature heat load And part of it is satisfied by the regenerative heat, or all of it is satisfied by the regenerative heat; the heat absorption of the ab process by the M 2 kg working fluid can be satisfied by the regenerative heat or an external heat source.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Pressure increasing process of kilogram working fluid 45, (M 1 +M 2 ) kilogram working fluid exothermic cooling process 56, (M 2 -M) kilogram working fluid depressurizing expansion process 6t, M 2 kilogram working fluid pressure reducing expansion process t3 , (M 1 +M) kg working fluid exothermic cooling, liquefaction and condensate cooling process 6r, M kg working fluid pressure reduction process rs, M kg working fluid endothermic, vaporization and overheating process st, M 1 kg working fluid
- the heat release and temperature reduction process of the medium condensate is r7, and the pressure reduction process of M 1 kg of the working fluid condensate is 71-a total of 12 processes.
- (M 1 +M 2 ) kilogram of working fluid is used for 56 process heat release for the heated medium, or at the same time for the heated medium and (M 1 +M 2 ) kilogram of working fluid.
- 34 process M kilogram of working fluid for the heat demand (regeneration) of the st process; (M 1 +M) kilogram of working fluid for the 6r process is mainly used for (M 1 +M 2 ) kilogram of working fluid for 34 process, The heat demand of the M kg working fluid for the st process (regeneration), or the heat demand for the heated medium and (M 1 +M 2 ) kg working fluid for the 34 process and the M kg working fluid for the st process (regeneration ); M 1 kg of working fluid condensate is used to heat the r7 process, generally used for (M 1 +M 2 ) kg of working fluid to heat the low temperature section of the 34 process.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the M kg working fluid in the st process is generally satisfied by the regenerative heat.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, (M 1 + M 2 ) kg of working fluid for 45 processes are generally completed by a compressor, requiring mechanical energy;
- (M 2 -M) kg of working fluid is depressurized and expanded process 6t and M 2 kg working fluid down the expansion process carried out by the expander t3 and mechanical energy,
- M rs kg working fluid for the process and the working medium M 1 kg for 71 process may be a turbine or a throttle valve to complete; buck expansion
- the work is less than the power consumption for boosting, and the insufficient part (circulation net work) is provided by the outside, forming a reverse single working substance steam combined cycle.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Kilogram working fluid pressure rise process 45, (M 2 -M) kilogram working fluid exothermic cooling process 56, (M 2 -M) kilogram working fluid depressurization expansion process 6t, M 2 kg working fluid depressurization expansion process t3, (M 1 +M) Kilogram working fluid boosting and heating process 57, (M 1 +M) Kilogram working fluid exothermic cooling, liquefaction and condensate cooling process 7r, M kg working fluid pressure reduction process rs, M kg working fluid mass endothermic vaporization and superheating process st, M 1 kilogram condensed liquid refrigerant to cool the exothermic process r8, M 1 kilogram refrigerant condensate of 13 81-- depressurization process.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the M kg working fluid in the st process is generally satisfied by the regenerative heat.
- 3Energy conversion process-M 1 kg working medium for 23 processes, (M 1 +M 2 ) kg working medium for 45 processes and (M 1 +M) kg working medium for 57 processes are generally completed by compressors, which require mechanical energy ;
- (M 2 -M) the pressure-reducing expansion process of the kilogram working fluid 6t and the pressure-reducing expansion process t3 of the M 2 kilogram working fluid are completed by the expander and provide mechanical energy, and the M kilogram working fluid performs the rs process and the M 1 kilogram working fluid
- the pressure process 81 can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (net cycle power) is provided by the outside, forming a reverse single-working-substance steam combined cycle.
- Working medium M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid pressure increasing process 23, (M 1 +M 2 ) kg of working fluid endothermic heating process 34, (M 1 +M 2 ) Pressure increasing process of kilogram working fluid 45, (M 2 -M) pressure increasing process of kilogram working fluid 56, (M 2 -M) kilogram working fluid exothermic and cooling process 67, (M 2 -M) pressure reduction of kilogram working fluid Expansion process 7t, M 2 kg working fluid depressurization expansion process t3, (M 1 +M) kg working fluid exothermic cooling, liquefaction and condensate cooling process 5r, M kg working fluid depressurization process rs, M kg working fluid mass endothermic vaporization and superheating process st, M 1 kilogram condensed liquid refrigerant to cool the exothermic process r8, M 1 kilogram refrigerant condensate of 13 81-- depressurization process.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- (M 1 +M 2 ) kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain the low-temperature heat load and part of it is satisfied by the regenerative heat, or all is satisfied by the regenerative heat; the heat absorption of the M kg working fluid in the st process is generally satisfied by the regenerative heat.
- 3Energy conversion process-M 1 kg of working fluid for 23 processes, (M 1 +M 2 ) kg of working fluid for 45 processes and (M 2 -M) kg of working fluid for 56 processes are generally completed by compressors, requiring mechanical energy ;
- (M 2 -M) kg working fluid depressurization expansion process 7t and M 2 kg working fluid depressurization expansion process t3 are completed by the expander and provide mechanical energy, M kg working fluid undergoes the rs process and M 1 kg working fluid reduction
- the pressure process 81 can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (net cycle power) is provided by the outside, forming a reverse single-working-substance steam combined cycle.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, (M 2 -M) kg Working fluid endothermic heating process 45, (M 2 -M) kg working fluid pressure increasing process 56, (M 2 -M) kg working fluid exothermic cooling process 67, (M 2 -M) kg working fluid depressurization and expansion Process 7t, M 2 kg working fluid depressurization and expansion process t3, (M 1 +M) kg working fluid boosting and heating process 48, (M 1 +M) kg working fluid exothermic cooling, liquefaction and condensate cooling process 8r, M kg working fluid depressurization process rs, M kg working fluid endothermic, vaporization and overheating process st, M 1 kg working fluid condensate exothermic cooling process r9, M 1 kg working fluid condensate depressurization process 91—— A total of 14 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- M 1 +M 2 kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low-temperature heat load and part of it is met by regenerative heat, or all of it is met by regenerative heat;
- M 2 -M the heat demand of 45 kilograms of working fluid is generally met by regenerative heat;
- M kg of working fluid The heat absorption of the st process is generally satisfied by heat recovery.
- Working medium M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure rising process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, (M 2 -M) kg Working fluid pressure rising process 45, (M 2 -M) kilogram working fluid exothermic cooling process 56, (M 2 -M) kilogram working fluid depressurizing expansion process 6t, M 2 kg working fluid depressurizing expansion process t3, ( M 1 +M) Kilogram working fluid endothermic heating process 47, (M 1 +M) Kilogram working fluid pressure increasing process 78, (M 1 +M) Kilogram working fluid exothermic cooling, liquefaction and condensate cooling process 8r, M kg working fluid depressurization process rs, M kg working fluid endothermic, vaporization and overheating process st, M 1 kg working fluid condensate exothermic cooling process r9, M 1 kg working fluid condensate depressurization process 91—— A total of 14 processes.
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- M 1 +M 2 kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low-temperature heat load and part is met by regenerative heat, or all is met by regenerative heat;
- M 1 +M kilogram of working fluid for 47 process heat demand can be met by regenerative heat;
- M kg of working fluid The heat absorption of the st process is generally satisfied by the heat recovery.
- 3Energy conversion process-M 1 kg working fluid for 23 processes, (M 1 +M) kg working fluid for 78 processes, and (M 2 -M) kg working fluid for 45 processes are generally completed by compressors, which require mechanical energy;
- M 2 -M The pressure-reducing expansion process of the kilogram working fluid 6t and the pressure-reducing expansion process t3 of the M 2 kilogram working fluid are completed by the expander and provide mechanical energy.
- the M kilogram working fluid is used for the rs process and the pressure reduction of the M 1 kilogram working fluid.
- the process 91 can be completed by a turbine or a throttle valve; the pressure-reducing expansion work is less than the pressure boosting work, and the insufficient part (net cycle power) is provided by the outside, forming a reverse single-working-substance steam combined cycle.
- the working medium is carried out-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid pressure increasing process 23, (M 1 +M 2 ) kg working fluid endothermic heating process 34, (M 1 +M 2- X) Kilogram working fluid endothermic heating process 45, (M 1 +M 2 -X) kilogram working fluid boosting and heating process 56, (M 1 +M 2 -X) kilogram working fluid exothermic and cooling process 67, X kg working fluid Pressure increasing process 47, (M 1 +M 2 ) kg working fluid exothermic cooling process 78, (M 2 -M) kg working fluid depressurizing expansion process 8t, M 2 kg working fluid depressurizing expansion process t3, ( M 1 +M) Kilogram working fluid exothermic cooling, liquefaction and condensate cooling process 8r, M kg working fluid pressure reduction process rs, M kg working fluid heat absorption, vaporization and superheating process st, M 1 kg working fluid condensation Liquid exothermic cooling process r9, M 1 kg working fluid
- M 1 kg of working fluid undergoes 12 processes to obtain low temperature heat load, which is provided by the refrigerated medium or low temperature heat source;
- M 1 +M 2 kg of working fluid undergoes 34 processes of heat absorption, which can be Part of it is used to obtain low temperature heat load and part of it is satisfied by regenerative heat, or all is satisfied by regenerative heat;
- M 1 +M 2 -X kilogram of working fluid undergoes 45 process heat absorption, which can be partially used to obtain low temperature heat load And part of it is satisfied by the regenerative heat, or the whole is satisfied by the regenerative heat; the heat absorption of the M kg working fluid in the st process can be satisfied by the regenerative heat.
- a single working fluid is conducive to production and storage; reduces operating costs and improves the flexibility of cycle adjustment
- the working fluid has a wide application range, can well adapt to the energy supply demand, and the working fluid and working parameters can be matched flexibly.
Abstract
Description
Claims (19)
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的八个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,(M 1+M 2)千克工质放热过程56,M 2千克工质降压过程63,M 1千克工质放热冷凝过程67,M 1千克工质降压过程71——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kg and M 2 kg, which are carried out separately or together in eight processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid rises Pressure process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, (M 1 +M 2 ) kg working fluid exothermic process 56, M 2 kg working fluid depressurization process 63, M 1 kg working fluid exothermic condensation process 67, M 1 kg working fluid depressurization process 71-a closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的九个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,M 2千克工质放热过程56,M 2千克工质降压过程63,M 1千克工质升压过程57,M 1千克工质放热冷凝过程78,M 1千克工质降压过程81——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the nine processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid rises Pressure process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid decreasing Pressure process 63, M 1 kg working fluid boosting process 57, M 1 kg working fluid exothermic condensation process 78, M 1 kg working fluid depressurizing process 81-a closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的九个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,M 2千克工质升压过程56,M 2千克工质放热过程67,M 2千克工质降压过程73,M 1千克工质放热冷凝过程58,M 1千克工质降压过程81——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the nine processes that are composed of M 1 kg and M 2 kg, respectively or jointly-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid rises Pressure process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boost process 45, M 2 kilogram working fluid boost process 56, M 2 kilogram working fluid release Thermal process 67, M 2 kg working fluid depressurization process 73, M 1 kg working fluid exothermic condensation process 58, M 1 kg working fluid depressurization process 81-a closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,M 2千克工质吸热过程45,M 2千克工质升压过程56,M 2千克工质放热过程67,M 2千克工质降压过程76,M 1千克工质升压过程48,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, and ten processes carried out separately or together-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid rises Pressure process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid endothermic process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid exothermic process 67, M 2 kg working fluid depressurisation 76, M 1 kilogram bootstrapping working fluid 48, M 1 kilogram refrigerant radiates heat and condenses process 89, M 1 kilogram working medium composed of depressurization 91-- closing process.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,M 2千克工质升压过程45,M 2千克工质放热过程56,M 2千克工质降压过程63,M 1千克工质吸热过程47,M 1千克工质升压过程78,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, and ten processes carried out separately or together-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid rises Pressure process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid depressurizing process 63, M 1 kg working fluid endothermic process 47, M 1 kg working fluid boosting process 78, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid depressurizing process 91-a closed process composed of.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同或部分进行的十一个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2-X)千克工质吸热过程45,(M 1+M 2-X)千克工质升压过程56,(M 1+M 2-X)千克工质放热过程67,X千克工质升压过程47,(M 1+M 2)千克工质放热过程78,M 2千克工质降压过程83,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to eleven processes that are composed of M 1 kg and M 2 kg, which are carried out separately or jointly or partially-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 -X) kg working fluid endothermic process 45, (M 1 +M 2 -X) kg working fluid Mass pressure increase process 56, (M 1 +M 2 -X) kg working fluid heat release process 67, X kg working fluid pressure boost process 47, (M 1 +M 2 ) kg working fluid heat release process 78, M 2 kg Working fluid depressurization process 83, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid depressurization process 91-a closed process composed of.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,(M 1+M 2)千克工质放热过程56,M 2千克工质降压过程6a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质放热冷凝过程67,M 1千克工质降压过程71——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, and ten processes carried out separately or together-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid rises Pressure process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, (M 1 +M 2 ) kg working fluid exothermic process 56, M 2 kg working fluid depressurisation 6a, M 2 kilogram refrigerant endothermic process ab, M 2 kilogram working fluid depressurisation b3, M 1 kilogram refrigerant radiates heat and condenses process 67, M 1 kilogram refrigerant depressurization 71- -The closing process of the composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行 的十一个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,M 2千克工质放热过程56,M 2千克工质降压过程6a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质升压过程57,M 1千克工质放热冷凝过程78,M 1千克工质降压过程81——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to eleven processes consisting of M 1 kg and M 2 kg, respectively or jointly-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid Boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid Pressure reduction process 6a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid boosting process 57, M 1 kg working fluid exothermic condensation process 78, M 1 kg working fluid Quality reduction process 81-the closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十一个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,M 2千克工质升压过程56,M 2千克工质放热过程67,M 2千克工质降压过程7a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质放热冷凝过程58,M 1千克工质降压过程81——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to eleven processes consisting of M 1 kg and M 2 kg, respectively or jointly-M 1 kg of working fluid endothermic vaporization process 12, M 1 kg of working fluid Boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 ) kg working fluid boosting process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid Exothermic process 67, M 2 kg working fluid depressurization process 7a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid depressurization process b3, M 1 kg working fluid exothermic condensation process 58, M 1 kg working fluid Quality reduction process 81-the closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十二个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,M 2千克工质吸热过程45,M 2千克工质升压过程56,M 2千克工质放热过程67,M 2千克工质降压过程7a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质升压过程48,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid endothermic process 45, M 2 kg working fluid boosting process 56, M 2 kg working fluid exothermic process 67, M 2 kg working fluid depressurization process 7a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid depressurization process b3, M 1 kg working fluid boosting process 48, M 1 kg working fluid exothermic condensation process 89 , M 1 kg of working fluid pressure reduction process 91-a closed process composed of.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十二个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,M 2千克工质升压过程45,M 2千克工质放热过程56,M 2千克工质降压过程6a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质吸热过程47,M 1千克工质升压过程78,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, M 2 kg working fluid boosting process 45, M 2 kg working fluid exothermic process 56, M 2 kg working fluid depressurizing process 6a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid heat absorption process 47, M 1 kg working fluid boosting process 78, M 1 kg working fluid exothermic condensation process 89 , M 1 kg of working fluid pressure reduction process 91-a closed process composed of.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同或部分进行的十三个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2-X)千克工质吸热过程45,(M 1+M 2-X)千克工质升压过程56,(M 1+M 2-X)千克工质放热过程67,X千克工质升压过程47,(M 1+M 2)千克工质放热过程78,M 2千克工质降压过程8a,M 2千克工质吸热过程ab,M 2千克工质降压过程b3,M 1千克工质放热冷凝过程89,M 1千克工质降压过程91——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to 13 processes that are composed of M 1 kg and M 2 kg, which are carried out separately or jointly or partially-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 -X) kg working fluid endothermic process 45, (M 1 +M 2 -X) kg working fluid Mass pressure increase process 56, (M 1 +M 2 -X) kg working fluid heat release process 67, X kg working fluid pressure boost process 47, (M 1 +M 2 ) kg working fluid heat release process 78, M 2 kg Working fluid pressure reduction process 8a, M 2 kg working fluid endothermic process ab, M 2 kg working fluid pressure reduction process b3, M 1 kg working fluid exothermic condensation process 89, M 1 kg working fluid pressure reduction process 91-composition The closing process.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十二个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,(M 1+M 2)千克工质放热过程56,(M 2-M)千克工质降压过程6t,M 2千克工质降压过程t3,(M 1+M)千克工质放热冷凝过程6r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r7,M 1千克工质降压过程71——组成的闭合过程。 The reverse single working fluid steam combined cycle refers to the working fluids composed of M 1 kg and M 2 kg, which are carried out separately or jointly in twelve processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boosting process 45, (M 1 +M 2 ) kilogram working fluid exothermic process 56, (M 2 -M) kg working fluid pressure reduction process 6t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid exothermic condensation process 6r, M kg working fluid pressure reduction process rs, M kg Working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r7, M 1 kg working fluid depressurization process 71-a closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十三个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,(M 2-M)千克工质放热过程56, (M 2-M)千克工质降压过程6t,M 2千克工质降压过程t3,(M 1+M)千克工质升压过程57,(M 1+M)千克工质放热冷凝过程7r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r8,M 1千克工质降压过程81——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kg and M 2 kg, which are carried out separately or together 13 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boosting process 45, (M 2 -M) kilogram working fluid exothermic process 56, ( M 2 -M) kg working fluid depressurization process 6t, M 2 kg working fluid depressurization process t3, (M 1 +M) kg working fluid boosting process 57, (M 1 +M) kg working fluid exothermic condensation process 7r, M kg working fluid depressurization process rs, M kg working fluid endothermic vaporization process st, M 1 kg working fluid exothermic process r8, M 1 kg working fluid depressurization process 81-a closed process composed of.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十三个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2)千克工质升压过程45,(M 2-M)千克工质升压过程56,(M 2-M)千克工质放热过程67,(M 2-M)千克工质降压过程7t,M 2千克工质降压过程t3,(M 1+M)千克工质放热冷凝过程5r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r8,M 1千克工质降压过程81——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid composed of M 1 kg and M 2 kg, which are carried out separately or together 13 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 1 +M 2 ) kilogram working fluid boosting process 45, (M 2 -M) kilogram working fluid boosting process 56, ( M 2 -M) kg working fluid exothermic process 67, (M 2 -M) kg working fluid pressure reduction process 7t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid exothermic condensation process 5r, M kilogram working fluid depressurization process rs, M kilogram working fluid endothermic vaporization process st, M 1 kilogram working fluid exothermic process r8, M 1 kilogram working fluid depressurization process 81-a closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十四个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 2-M)千克工质吸热过程45,(M 2-M)千克工质升压过程56,(M 2-M)千克工质放热过程67,(M 2-M)千克工质降压过程7t,M 2千克工质降压过程t3,(M 1+M)千克工质升压过程48,(M 1+M)千克工质放热冷凝过程8r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r9,M 1千克工质降压过程91——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid consisting of M 1 kg and M 2 kg, which are carried out separately or together in 14 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Pressure boosting process 23, (M 1 +M 2 ) kilogram working fluid endothermic process 34, (M 2 -M) kilogram working fluid heat absorption process 45, (M 2 -M) kilogram working fluid boosting process 56, (M 2 -M) kilogram working fluid heat release process 67, (M 2 -M) kilogram working fluid pressure reduction process 7t, M 2 kilogram working fluid pressure reduction process t3, (M 1 +M) kilogram working fluid pressure increase process 48, (M 1 + M) kg refrigerant radiates heat and condenses process 8r, M kg working fluid depressurisation rs, M kg refrigerant absorbs heat of vaporization process st, M 1 kg refrigerant exothermic process r9, M 1 kg working fluid drop Compression process 91-the closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同进行的十四个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 2-M)千克工质升压过程45,(M 2-M)千克工质放热过程56,(M 2-M)千克工质降压过程6t,M 2千克工质降压过程t3,(M 1+M)千克工质吸热过程47,(M 1+M)千克工质升压过程78,(M 1+M)千克工质放热冷凝过程8r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r9,M 1千克工质降压过程91——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid consisting of M 1 kg and M 2 kg, which are carried out separately or together in 14 processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg working fluid Boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 2 -M) kg working fluid boosting process 45, (M 2 -M) kg working fluid exothermic process 56, (M 2 -M) kg working fluid pressure reduction process 6t, M 2 kg working fluid pressure reduction process t3, (M 1 +M) kg working fluid heat absorption process 47, (M 1 +M) kg working fluid pressure increase process 78, (M 1 + M) kg refrigerant radiates heat and condenses process 8r, M kg working fluid depressurisation rs, M kg refrigerant absorbs heat of vaporization process st, M 1 kg refrigerant exothermic process r9, M 1 kg working fluid drop Compression process 91-the closed process of composition.
- 逆向单工质蒸汽联合循环,是指由M 1千克和M 2千克组成的工质,分别或共同或部分进行的十五个过程——M 1千克工质吸热汽化过程12,M 1千克工质升压过程23,(M 1+M 2)千克工质吸热过程34,(M 1+M 2-X)千克工质吸热过程45,(M 1+M 2-X)千克工质升压过程56,(M 1+M 2-X)千克工质放热过程67,X千克工质升压过程47,(M 1+M 2)千克工质放热过程78,(M 2-M)千克工质降压过程8t,M 2千克工质降压过程t3,(M 1+M)千克工质放热冷凝过程8r,M千克工质降压过程rs,M千克工质吸热汽化过程st,M 1千克工质放热过程r9,M 1千克工质降压过程91——组成的闭合过程。 Reverse single working fluid steam combined cycle refers to the working fluid consisting of M 1 kg and M 2 kg, which are carried out separately or jointly or partially in fifteen processes-M 1 kg working fluid endothermic vaporization process 12, M 1 kg Working fluid boosting process 23, (M 1 +M 2 ) kg working fluid endothermic process 34, (M 1 +M 2 -X) kg working fluid endothermic process 45, (M 1 +M 2 -X) kg working fluid Process 56 of (M 1 +M 2 -X) kilogram of working fluid exothermic process 67, X kilogram of working fluid boost process 47, (M 1 +M 2 ) kilogram of working fluid exothermic process 78, (M 2 -M) The pressure reduction process of kilogram working fluid 8t, the pressure reduction process of M 2 kilogram working fluid t3, the exothermic condensation process of (M 1 +M) kilogram working fluid 8r, the pressure reduction process of M kilogram working fluid rs, the absorption of M kilogram working fluid Thermal vaporization process st, M 1 kg working fluid exothermic process r9, M 1 kg working fluid depressurization process 91-a closed process composed of.
- 逆向单工质蒸汽联合循环,是在权利要求1-18所述的任一一款逆向单工质蒸汽联合循环中,将其中的“M 1千克工质升压过程23”变更为“M 1千克工质升压过程2z,M 1千克工质吸热过程z3”,得到逆向单工质蒸汽联合循环。 The reverse single working fluid steam combined cycle is in any one of the reverse single working fluid steam combined cycles described in claims 1-18, in which the "M 1 kg working fluid boost process 23" is changed to "M 1 The pressure increase process of kilogram working fluid is 2z, and the heat absorption process of M 1 kilogram working fluid is z3", and the reverse single working fluid steam combined cycle is obtained.
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2020
- 2020-06-10 US US17/618,784 patent/US20220260285A1/en not_active Abandoned
- 2020-06-10 WO PCT/CN2020/000135 patent/WO2020248591A1/en active Application Filing
- 2020-06-10 GB GB2200342.0A patent/GB2599865B/en active Active
- 2020-06-10 CN CN202010557970.7A patent/CN115478918A/en active Pending
Patent Citations (6)
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JPH03125863A (en) * | 1989-10-06 | 1991-05-29 | Matsushita Electric Ind Co Ltd | Refrigerating cycle unit with two stage compression |
JPH09126115A (en) * | 1995-11-08 | 1997-05-13 | Wakabayashi Hiroo | Method for transforming one thermal source into work |
CN101906998A (en) * | 2009-07-31 | 2010-12-08 | 王世英 | Multi-cycle electricity-generation thermodynamic system and implementing method thereof |
WO2016117946A1 (en) * | 2015-01-23 | 2016-07-28 | Lg Electronics Inc. | Cooling cycle apparatus for refrigerator |
CN107893685A (en) * | 2016-10-12 | 2018-04-10 | 李华玉 | Either simplex matter Steam Combined Cycle and combined cycle Steam Power Equipment |
CN108662809A (en) * | 2017-03-30 | 2018-10-16 | 李华玉 | Double-work medium combined cycle compression heat pump |
Also Published As
Publication number | Publication date |
---|---|
CN115478918A (en) | 2022-12-16 |
GB2599865B (en) | 2023-03-29 |
GB2599865A (en) | 2022-04-13 |
US20220260285A1 (en) | 2022-08-18 |
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