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US20220195895A1 - Single-working-medium vapor combined cycle - Google Patents

Single-working-medium vapor combined cycle Download PDF

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Publication number
US20220195895A1
US20220195895A1 US17/606,446 US202017606446A US2022195895A1 US 20220195895 A1 US20220195895 A1 US 20220195895A1 US 202017606446 A US202017606446 A US 202017606446A US 2022195895 A1 US2022195895 A1 US 2022195895A1
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working medium
state
heat
absorption
depressurization
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US17/606,446
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Huayu Li
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K7/00Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/06Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using mixtures of different fluids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K27/00Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00Methods of steam generation characterised by form of heating method
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B9/00Auxiliary systems, arrangements, or devices
    • F28B9/08Auxiliary systems, arrangements, or devices for collecting and removing condensate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K13/00General layout or general methods of operation of complete plants
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K7/00Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • F01K7/02Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of multiple-expansion type

Definitions

  • the present invention belongs to the field of energy and power technology.
  • the vapor power device with external combustion for example, its heat source has the dual characteristics of high temperature and variable temperature.
  • the material's temperature resistance and pressure resistance abilities and safety concerns limit the parameters of the cycle's working medium. Therefore, there is a big temperature difference between the working medium and the heat source, which leads to big irreversible loss and low efficiency.
  • thermodynamic cycles are the theoretical basis of thermal energy utilization devices, and the core of energy utilization systems. The establishment, development and application of thermodynamic cycles will play an important role in the rapid development of energy utilization and will promote actively for social progress and productivity development.
  • the present invention proposes a single-working-medium vapor combined cycle.
  • the single working-medium vapor combined cycle and the vapor power device for combined cycle are mainly provided in the present invention, and the specific content of the present invention is as follows:
  • a single-working-medium vapor combined cycle method consisting of twelve processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M 1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (5) of the M 2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M 1 +M 2
  • a single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M 1 kg of working medium, performing a depressurization process to set the state (5) to (7) of the M 1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (6) of the M 2 kg of working medium, performing
  • a single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the M 1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (5) of the M 2 kg of working medium, performing a heat-absorption process to set the state (5) to (6) of the M 2 kg of working medium,
  • a single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M 1 kg of working medium, performing a depressurization process to set the state (5) to (9) of the M 1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (6) of the M 2 kg of working medium
  • a single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M 1 kg of working medium, performing a depressurization process to set the state (5) to (6) of the M 1 kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the M 1 kg of working medium and the H kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c)
  • a single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M 1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M 1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M 1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (5) of the M 2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M 1 +
  • a single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M 1 +M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a
  • a single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (5) to (7) of the (M 1 +M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption
  • a single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the (M 1 +M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a
  • a single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (5) to (9) of the (M 1 +M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption
  • a single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (5) to (6) of the (M 1 +M) kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the (M 1 +M) kg of working medium and the H
  • a single-working-medium vapor combined cycle method consisting of eighteen processes which are conducted with M 1 kg of working medium, M 2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M 1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M 1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M 1 +M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M 1 +M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M 1 +M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to
  • FIG. 1 is a type 1 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 2 is a type 2 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 3 is a type 3 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 4 is a type 4 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 5 is a type 5 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 6 is a type 6 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 7 is a type 7 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 8 is a type 8 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 9 is a type 9 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 10 is a type 10 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 11 is a type 11 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 12 is a type 12 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 1 works as follows:
  • the working medium conducts twelve processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 5 of the M 1 kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 8 of the H kg of working medium, a pressurization process 8 - 5 of the M 2 kg of working medium, a heat-absorption process 5 - 6 of the (M 1 +M 2 ) kg of working medium, a depressurization process 6 - 7 of the (M 1 +M 2 ) kg of working medium, a mixed heat-releasing process 7 - 8 of the (M 1 +M 2 ) kg of working medium and the H kg of working medium, a depressurization process
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 8 - 5 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization (and expansion) process 3 - 4 of the M 1 kg of working medium, the depressurization (and expansion) process 6 - 7 of the (M 1 +M 2 ) kg of working medium and the depressurization (and expansion) process 8 - 9 of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 2 works as follows:
  • the working medium conducts thirteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 5 of the M 1 kg of working medium, a depressurization process 5 - 7 of the M 1 kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 9 of the H kg of working medium, a pressurization process 9 - 6 of the M 2 kg of working medium, a heat-absorption process 6 - 7 of the M 2 kg of working medium, a depressurization process 7 - 8 of the (M 1 +M 2 ) kg of working medium, a mixed heat-releasing process 8 - 9 of the (M 1 +M 2 ) kg of working medium and
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 9 - 6 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization (and expansion) process 3 - 4 of the M 1 kg of working medium, the depressurization (and expansion) process 5 - 7 of the M 1 kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ) kg of working medium and the depressurization (and expansion) process 9 - c of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 3 works as follows:
  • the working medium conducts thirteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 7 of the M 1 kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 9 of the H kg of working medium, a pressurization process 9 - 5 of the M 2 kg of working medium, a heat-absorption process 5 - 6 of the M 2 kg of working medium, a depressurization process 6 - 7 of the M 2 kg of working medium, a depressurization process 7 - 8 of the (M 1 +M 2 ) kg of working medium, a mixed heat-releasing process 8 - 9 of the (M 1 +M 2 ) kg of working medium and
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 9 - 5 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization (and expansion) process 3 - 4 of the M 1 kg of working medium, the depressurization (and expansion) process 6 - 7 of the M 2 kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ) kg of working medium and the depressurization (and expansion) process 9 - c of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 4 works as follows:
  • the working medium conducts fourteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 5 of the M 1 kg of working medium, a depressurization process 5 - 9 of the M 1 kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c- 6 of the M 2 kg of working medium, a heat-absorption process 6 - 7 of the M 2 kg of working medium, a depressurization process 7 - 8 of the M 2 kg of working medium, a mixed heat-releasing process 8 - 9 of the M 2 kg of working medium and the H kg of working medium, a mixed heat-
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c- 6 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization process 3 - 4 of the M 1 kg of working medium, the depressurization process 5 - 9 of the M 1 kg of working medium, the depressurization process 7 - 8 of the M 2 kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 5 works as follows:
  • the working medium conducts fourteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 5 of the M 1 kg of working medium, a depressurization process 5 - 6 of the M 1 kg of working medium, a mixed heat-releasing process 6 - 9 of the M 1 kg of working medium and the H kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c- 7 of the M 2 kg of working medium, a heat-absorption process 7 - 8 of the M 2 kg of working medium, a depressurization process 8 - 9 of the M 2 kg of working medium, a mixed heat-
  • the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 6 - 9 of the M 1 kg of working medium and the process 9 - c of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the process 2 - 3 of the M 1 kg of working medium the process 4 - 5 of the M 1 kg of working medium and the process 5 - 6 of the M 2 kg of working medium, the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c- 7 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization (and expansion) process 3 - 4 of the M 1 kg of working medium, the depressurization (and expansion) process 5 - 6 of the M 1 kg of working medium, the depressurization (and expansion) process 8 - 9 of the M 2 kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 6 works as follows:
  • the working medium conducts fifteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption vaporization and superheating process 2 - 3 of the M 1 kg of working medium, a depressurization process 3 - 4 of the M 1 kg of working medium, a heat-absorption process 4 - 5 of the M 1 kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c- 5 of the M 2 kg of working medium, a heat-absorption process 5 - 6 of the (M 1 +M 2 ) kg of working medium, a depressurization process 6 - 9 of the X kg of working medium, a heat-absorption process 6 - 7 of the (M 1 +M 2 ⁇ X) kg of working medium, a depressurization process 7 - 8 of the (M 1 +
  • the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8 - 9 of the (M 1 +M 2 ⁇ X) kg of working medium and the process 9 - c of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the process 2 - 3 of the M 1 kg of working medium the process 4 - 5 of the M 1 kg of working medium, the process 5 - 6 of the (M 1 +M 2 ) kg of working medium and the process 6 - 7 of the (M 1 +M 2 ⁇ X) kg of working medium, the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c- 5 of the M 2 kg of working medium is usually achieved by a compressor.
  • the depressurization (and expansion) process 3 - 4 of the M 1 kg of working medium, the depressurization (and expansion) process 6 - 9 of the X kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ⁇ X) kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 7 works as follows:
  • the working medium conducts twelve processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 5 of the (M 1 +M) kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 8 of the H kg of working medium, a pressurization process 8 - a of the M 2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M 1 kg of working medium, a pressurization process a- 5 of the (M 2 ⁇ M) kg of working medium, a heat-absorption
  • the absorbed heat in the process e- 8 of the H kg of working medium is provided by the heat-releasing in the process 7 - 8 of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the process 4 - 5 of the (M 1 +M) kg of working medium and the process 5 - 6 of the (M 1 +M 2 ) kg of working medium the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 8 - a of the M 2 kg of working medium and the pressurization process a- 5 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 6 - 7 of the (M 1 +M) kg of working medium and the depressurization (and expansion) process 8 - 9 of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 8 works as follows:
  • the working medium conducts sixteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 5 of the (M 1 +M) kg of working medium, a depressurization process 5 - 7 of the (M 1 +M) kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 9 of the H kg of working medium, a pressurization process 9 - a of the M 2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M 1 kg of
  • the absorbed heat in the process e- 9 of the H kg of working medium is provided by the heat-releasing in the process 8 - 9 of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the process 4 - 5 of the (M 1 +M) kg of working medium and the process 6 - 7 of the (M 2 ⁇ M) kg of working medium the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 9 - a of the M 2 kg of working medium and the pressurization process a- 6 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 5 - 7 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ) kg of working medium and the depressurization (and expansion) process 9 - c of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 9 works as follows:
  • the working medium conducts sixteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 7 of the (M 1 +M) kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e- 9 of the H kg of working medium, a pressurization process 9 - a of the M 2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M 1 kg of working medium, a pressurization process a- 5 of the (M 2 ⁇ M) kg of
  • the absorbed heat in the process e- 9 of the H kg of working medium is provided by the heat-releasing in the process 8 - 9 of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the process 4 - 7 of the (M 1 +M) kg of working medium and the process 5 - 6 of the (M 2 ⁇ M) kg of working medium the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process 9 - a of the M 2 kg of working medium and the pressurization process a- 5 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 6 - 7 of the (M 2 ⁇ M) kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ) kg of working medium and the depressurization (and expansion) process 9 - c of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 10 works as follows:
  • the working medium conducts seventeen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 5 of the (M 1 +M) kg of working medium, a depressurization process 5 - 9 of the (M 1 +M) kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M 2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M 1 kg of working medium
  • the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8 - 9 of the (M 2 ⁇ M) kg of working medium and the process 9 - c of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c-a of the M 2 kg of working medium and the pressurization process a- 6 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 5 - 9 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 2 ⁇ M) kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 11 works as follows:
  • the working medium conducts seventeen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 5 of the (M 1 +M) kg of working medium, a depressurization process 5 - 6 of the (M 1 +M) kg of working medium, a mixed heat-releasing process 6 - 9 of the (M 1 +M) kg of working medium and the H kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M
  • the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 6 - 9 of the (M 1 +M) kg of working medium and the process 9 - c of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c-a of the M 2 kg of working medium and the pressurization process a- 7 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 5 - 6 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 8 - 9 of the (M 2 ⁇ M) kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the T-s diagram of the single-working-medium vapor combined cycle in FIG. 12 works as follows:
  • the working medium conducts eighteen processes: a pressurization process 1 - 2 of the M 1 kg of working medium, a heat-absorption process 2 - b of the M 1 kg of working medium, a heat-absorption vaporization and superheating process b- 3 of the (M 1 +M) kg of working medium, a depressurization process 3 - 4 of the (M 1 +M) kg of working medium, a heat-absorption process 4 - 5 of the (M 1 +M) kg of working medium, a pressurization process 1 - e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M 2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M 1 kg of working medium, a pressurization process a- 5 of the (M 2 ⁇ M) kg
  • the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8 - 9 of the (M 1 +M 2 ⁇ X) kg of working medium and the process 9 - c of the (M 1 +M 2 ) kg of working medium, or by an external heat source at the same time.
  • the absorbed heat in the process 2 - b of the M 1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time.
  • the absorbed heat is provided by an external heat source.
  • the pressurization process 1 - 2 of the M 1 kg of working medium and the pressurization process 1 - e of H kg of working medium are usually achieved by pumps.
  • the pressurization process c-a of the M 2 kg of working medium and the pressurization process a- 5 of the (M 2 ⁇ M) kg of working medium are usually achieved by compressors.
  • the depressurization (and expansion) process 3 - 4 of the (M 1 +M) kg of working medium, the depressurization (and expansion) process 6 - 9 of the X kg of working medium, the depressurization (and expansion) process 7 - 8 of the (M 1 +M 2 ⁇ X) kg of working medium and the depressurization (and expansion) process c-d of the (M 1 +H) kg of working medium are usually achieved by expanders.
  • the total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • the technical effects of the present invention invention The single-working-medium vapor combined cycle proposed by the present invention has the following effects and advantages:
  • the present invention greatly reduces the amount of heat absorbed in the phase-change region, and correspondingly increases the amount of heat absorbed in the high-temperature region or the variable temperature region. Therefore, the single-working-medium vapor combined cycle can achieve high efficiency.
  • the present invention possesses simple methods, reasonable processes and good applicability. It is a common technology to realize the effective utilization of temperature differences.
  • the present invention only uses a single working medium, which is easy to produce and store.
  • the present invention can also reduce the operation cost and improve the flexibility of cycle regulation.
  • both the cycle's working medium and the heat source medium conduct variable-temperature processes; therefore, the temperature difference loss is reduced and the efficiency is improved.
  • the present invention adopts the low-pressure and high-temperature operation mode in the high-temperature region; therefore, the contradiction among thermal efficiency, the working medium's parameters and the material's temperature resistance and pressure resistance abilities, which is common in traditional vapor power devices, can be resolved.
  • the vapor power device provided in the present invention can operate at a low pressure.
  • the present invention provides theoretical support for improving the safety of device operation.
  • the present invention possesses a wide range of applicable working media.
  • the present invention can match energy supply with demand well. It is flexible to match the working medium and the working parameters.
  • the present invention expands the range of thermodynamic cycles for temperature difference utilization, and contributes to a higher-efficiency power generation of high-temperature heat sources and variable-temperature heat sources.

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Abstract

The single-working-medium vapor combined cycle is provided in this invitation and belongs to the field of energy and power technology. A single-working-medium vapor combined cycle consists of nine processes which are conducted with M1 kg of working medium and M2 kg of working medium separately or jointly: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a pressurization process 7-4 of M2 kg of working medium, a heat-absorption process 4-5 of the M3 kg of working medium, a depressurization process 5-6 of the M3 kg of working medium, a heat-releasing process 6-7 of the M3 kg of working medium, a heat-releasing and condensation process 7-1 of the M1 kg of working medium; M3 is the sum of M1 and M2.

Description

    FIELD
  • The present invention belongs to the field of energy and power technology.
  • BACKGROUD
  • Cold demand, heat demand and power demand are common in human life and production. It is an important way to obtain and provide power by the conversion of thermal energy into mechanical energy. In general, the temperature of heat source reduces and varies with the release of heat. When fossil fuels are used as the primary energy, the heat source has the dual characteristics of both high temperature and variable temperature. Therefore, only one single thermodynamic cycle cannot achieve an ideal efficiency for refrigeration, heating or power generation.
  • Take the vapor power device with external combustion for example, its heat source has the dual characteristics of high temperature and variable temperature. For those vapor power devices based on the Rankine cycle, the material's temperature resistance and pressure resistance abilities and safety concerns limit the parameters of the cycle's working medium. Therefore, there is a big temperature difference between the working medium and the heat source, which leads to big irreversible loss and low efficiency.
  • Humans need new basic theory of thermal science to use fuel or other high temperature thermal energy simply, actively, efficiently for achieving refrigeration, heating or power. In the basic theory system of thermal science, thermodynamic cycles are the theoretical basis of thermal energy utilization devices, and the core of energy utilization systems. The establishment, development and application of thermodynamic cycles will play an important role in the rapid development of energy utilization and will promote actively for social progress and productivity development.
  • Based on the principles of simple, active and efficient utilization of temperature difference, aiming at the power generation application of high temperature heat sources or variable temperature heat sources, and striving to provide theoretical support for the simplification and high efficiency of thermo-power systems, the present invention proposes a single-working-medium vapor combined cycle.
  • THE CONTENTS OF THE PRESENT INVENTION
  • The single working-medium vapor combined cycle and the vapor power device for combined cycle are mainly provided in the present invention, and the specific content of the present invention is as follows:
  • 1. A single-working-medium vapor combined cycle method consisting of twelve processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (5) of the M2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set the state (6) to (7) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (7) to (8) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (9) to (1) of the (M1+H) kg of working medium.
  • 2. A single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (7) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (6) of the M2 kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
  • 3. A single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (5) of the M2 kg of working medium, performing a heat-absorption process to set the state (5) to (6) of the M2 kg of working medium, performing a depressurization process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
  • 4. A single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (9) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (6) of the M2 kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set the state (7) to (8) of the M2 kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the M2 kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • 5. A single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (6) of the M1 kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the M1 kg of working medium and the H kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (7) of the M2 kg of working medium, performing a heat-absorption process to set the state (7) to (8) of the M2 kg of working medium, performing a depressurization process to set the state (8) to (9) of the M2 kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • 6. A single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (5) of the M2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set a state (6) to (9) of the X kg of working medium, performing a heat-absorption process to set a state (6) to (7) of the (M1+M2−X) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2−X) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2−X) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • 7. A single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set the state (6) to (7) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (7) to (8) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (9) to (1) of the (M1+H) kg of working medium.
  • 8. A single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (7) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (6) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
  • 9. A single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (5) to (6) of the (M2−M) kg of working medium, performing a depressurization process to set a state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
  • 10. A single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (9) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (6) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M2−M) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M2−M) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • 11. A single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (6) of the (M1+M) kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the (M1+M) kg of working medium and the H kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (7) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (7) to (8) of the (M2−M) kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M2−M) kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • 12. A single-working-medium vapor combined cycle method consisting of eighteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set a state (6) to (9) of the X kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M1+M2−X) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2−X) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2−X) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
  • BRIEF DESCRIPTION OF THE FIGURES
  • FIG. 1 is a type 1 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 2 is a type 2 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 3 is a type 3 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 4 is a type 4 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 5 is a type 5 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 6 is a type 6 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 7 is a type 7 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 8 is a type 8 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 9 is a type 9 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 10 is a type 10 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 11 is a type 11 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • FIG. 12 is a type 12 example general flow chart of a single-working-medium vapor combined cycle provided in the present invention.
  • DETAILED DESCRIPTION
  • The first thing to note is that, when describing the cycle's structures and processes, the processes will not be repeatedly described if not necessary, and the obvious processes will not be described. The detailed description of the present invention is as follows:
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 1 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts twelve processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-5 of the M1 kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-8 of the H kg of working medium, a pressurization process 8-5 of the M2 kg of working medium, a heat-absorption process 5-6 of the (M1+M2) kg of working medium, a depressurization process 6-7 of the (M1+M2) kg of working medium, a mixed heat-releasing process 7-8 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 8-9 of the (M1+H) kg of working medium, a heat-releasing and condensation process 9-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-8 of the H kg of working medium is provided by the heat-releasing in the process 7-8 of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-5 of the M1 kg of working medium and the process 5-6 of the (M1+M2) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 7-8, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 8. The heat released by the (M1+H) kg of working medium in process 9-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 8-5 of the M2 kg of working medium is usually achieved by a compressor. The depressurization (and expansion) process 3-4 of the M1 kg of working medium, the depressurization (and expansion) process 6-7 of the (M1+M2) kg of working medium and the depressurization (and expansion) process 8-9 of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 2 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts thirteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-5 of the M1 kg of working medium, a depressurization process 5-7 of the M1 kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-9 of the H kg of working medium, a pressurization process 9-6 of the M2 kg of working medium, a heat-absorption process 6-7 of the M2 kg of working medium, a depressurization process 7-8 of the (M1+M2) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 9-c of the (M1+H) kg of working medium, a heat-releasing and condensation process c-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-9 of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-5 of the M1 kg of working medium and the process 6-7 of the M2 kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 9. The heat released by the (M1+H) kg of working medium in process c-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 9-6 of the M2 kg of working medium is usually achieved by a compressor. The depressurization (and expansion) process 3-4 of the M1 kg of working medium, the depressurization (and expansion) process 5-7 of the M1 kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2) kg of working medium and the depressurization (and expansion) process 9-c of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 3 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts thirteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-7 of the M1 kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-9 of the H kg of working medium, a pressurization process 9-5 of the M2 kg of working medium, a heat-absorption process 5-6 of the M2 kg of working medium, a depressurization process 6-7 of the M2 kg of working medium, a depressurization process 7-8 of the (M1+M2) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 9-c of the (M1+H) kg of working medium, a heat-releasing and condensation process c-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-9 of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-7 of the M1 kg of working medium and the process 5-6 of the M2 kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 9. The heat released by the (M1+H) kg of working medium in process c-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 9-5 of the M2 kg of working medium is usually achieved by a compressor. The depressurization (and expansion) process 3-4 of the M1 kg of working medium, the depressurization (and expansion) process 6-7 of the M2 kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2) kg of working medium and the depressurization (and expansion) process 9-c of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 4 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts fourteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-5 of the M1 kg of working medium, a depressurization process 5-9 of the M1 kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-6 of the M2 kg of working medium, a heat-absorption process 6-7 of the M2 kg of working medium, a depressurization process 7-8 of the M2 kg of working medium, a mixed heat-releasing process 8-9 of the M2 kg of working medium and the H kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2−X) kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-5 of the M1 kg of working medium and the process 6-7 of the M2 kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the M2 kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the M2 kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-6 of the M2 kg of working medium is usually achieved by a compressor. The depressurization process 3-4 of the M1 kg of working medium, the depressurization process 5-9 of the M1 kg of working medium, the depressurization process 7-8 of the M2 kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 5 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts fourteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-5 of the M1 kg of working medium, a depressurization process 5-6 of the M1 kg of working medium, a mixed heat-releasing process 6-9 of the M1 kg of working medium and the H kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-7 of the M2 kg of working medium, a heat-absorption process 7-8 of the M2 kg of working medium, a depressurization process 8-9 of the M2 kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 6-9 of the M1 kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-5 of the M1 kg of working medium and the process 5-6 of the M2 kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 6-9, the M1 kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the M2 kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-7 of the M2 kg of working medium is usually achieved by a compressor. The depressurization (and expansion) process 3-4 of the M1 kg of working medium, the depressurization (and expansion) process 5-6 of the M1 kg of working medium, the depressurization (and expansion) process 8-9 of the M2 kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 6 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts fifteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption vaporization and superheating process 2-3 of the M1 kg of working medium, a depressurization process 3-4 of the M1 kg of working medium, a heat-absorption process 4-5 of the M1 kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-5 of the M2 kg of working medium, a heat-absorption process 5-6 of the (M1+M2) kg of working medium, a depressurization process 6-9 of the X kg of working medium, a heat-absorption process 6-7 of the (M1+M2−X) kg of working medium, a depressurization process 7-8 of the (M1+M2−X) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2−X) kg of working medium and the H kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2−X) kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. In the process 2-3 of the M1 kg of working medium, the process 4-5 of the M1 kg of working medium, the process 5-6 of the (M1+M2) kg of working medium and the process 6-7 of the (M1+M2−X) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2−X) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2−X) kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-5 of the M2 kg of working medium is usually achieved by a compressor. The depressurization (and expansion) process 3-4 of the M1 kg of working medium, the depressurization (and expansion) process 6-9 of the X kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2−X) kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 7 works as follows:
  • (1) From the Perspective of the Cycle's Processes.
  • The working medium conducts twelve processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-5 of the (M1+M) kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-8 of the H kg of working medium, a pressurization process 8-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-5 of the (M2−M) kg of working medium, a heat-absorption process 5-6 of the (M1+M2) kg of working medium, a depressurization process 6-7 of the (M1+M2) kg of working medium, a mixed heat-releasing process 7-8 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 8-9 of the (M1+H) kg of working medium, a heat-releasing and condensation process 9-1 of the (M1+H) kg of working medium.
  • (2) From the perspective of energy conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-8 of the H kg of working medium is provided by the heat-releasing in the process 7-8 of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-5 of the (M1+M) kg of working medium and the process 5-6 of the (M1+M2) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 7-8, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 8. The heat released by the (M1+H) kg of working medium in process 9-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 8-a of the M2 kg of working medium and the pressurization process a-5 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 6-7 of the (M1+M) kg of working medium and the depressurization (and expansion) process 8-9 of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 8 works as follows:
  • (1) From the perspective of the cycle's processes. The working medium conducts sixteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-5 of the (M1+M) kg of working medium, a depressurization process 5-7 of the (M1+M) kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-9 of the H kg of working medium, a pressurization process 9-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-6 of the (M2−M) kg of working medium, a heat-absorption process 6-7 of the (M2−M) kg of working medium, a depressurization process 7-8 of the (M1+M2) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 9-c of the (M1+H) kg of working medium, a heat-releasing and condensation process c-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-9 of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-5 of the (M1+M) kg of working medium and the process 6-7 of the (M2−M) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 9. The heat released by the (M1+H) kg of working medium in process c-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 9-a of the M2 kg of working medium and the pressurization process a-6 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 5-7 of the (M1+M) kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2) kg of working medium and the depressurization (and expansion) process 9-c of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 9 works as follows:
  • (1) From the perspective of the cycle's processes. The working medium conducts sixteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-7 of the (M1+M) kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-9 of the H kg of working medium, a pressurization process 9-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-5 of the (M2−M) kg of working medium, a heat-absorption process 5-6 of the (M2−M) kg of working medium, a depressurization process 6-7 of the (M2−M) kg of working medium, a depressurization process 7-8 of the (M1+M2) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process 9-c of the (M1+H) kg of working medium, a heat-releasing and condensation process c-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-9 of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-7 of the (M1+M) kg of working medium and the process 5-6 of the (M2−M) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state 9. The heat released by the (M1+H) kg of working medium in process c-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process 9-a of the M2 kg of working medium and the pressurization process a-5 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 6-7 of the (M2−M) kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2) kg of working medium and the depressurization (and expansion) process 9-c of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 10 works as follows:
  • (1) From the perspective of the cycle's processes. The working medium conducts seventeen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-5 of the (M1+M) kg of working medium, a depressurization process 5-9 of the (M1+M) kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-6 of the (M2−M) kg of working medium, a heat-absorption process 6-7 of the (M2−M) kg of working medium, a depressurization process 7-8 of the (M2−M) kg of working medium, a mixed heat-releasing process 8-9 of the (M2−M) kg of working medium and the H kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M2−M) kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-5 of the (M1+M) kg of working medium and the process 6-7 of the (M2−M) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M2−M) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M2−M) kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-a of the M2 kg of working medium and the pressurization process a-6 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 5-9 of the (M1+M) kg of working medium, the depressurization (and expansion) process 7-8 of the (M2−M) kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 11 works as follows:
  • (1) From the perspective of the cycle's processes. The working medium conducts seventeen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-5 of the (M1+M) kg of working medium, a depressurization process 5-6 of the (M1+M) kg of working medium, a mixed heat-releasing process 6-9 of the (M1+M) kg of working medium and the H kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-7 of the (M2−M) kg of working medium, a heat-absorption process 7-8 of the (M2−M) kg of working medium, a depressurization process 8-9 of the (M2−M) kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 6-9 of the (M1+M) kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-5 of the (M1+M) kg of working medium and the process 7-8 of the (M2−M) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 6-9, the (M1+M) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M2−M) kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-a of the M2 kg of working medium and the pressurization process a-7 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 5-6 of the (M1+M) kg of working medium, the depressurization (and expansion) process 8-9 of the (M2−M) kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The T-s diagram of the single-working-medium vapor combined cycle in FIG. 12 works as follows:
  • (1) From the perspective of the cycle's processes. The working medium conducts eighteen processes: a pressurization process 1-2 of the M1 kg of working medium, a heat-absorption process 2-b of the M1 kg of working medium, a heat-absorption vaporization and superheating process b-3 of the (M1+M) kg of working medium, a depressurization process 3-4 of the (M1+M) kg of working medium, a heat-absorption process 4-5 of the (M1+M) kg of working medium, a pressurization process 1-e of the H kg of working medium, a heat-absorption vaporization and superheating process e-c of the H kg of working medium, a pressurization process c-a of the M2 kg of working medium, a mixed heat-releasing process a-b of the M kg of working medium and the M1 kg of working medium, a pressurization process a-5 of the (M2−M) kg of working medium, a heat-absorption process 5-6 of the (M1+M2) kg of working medium, a depressurization process 6-9 of the X kg of working medium, a heat-absorption process 6-7 of the (M1+M2−X) kg of working medium, a depressurization process 7-8 of the (M1+M2−X) kg of working medium, a mixed heat-releasing process 8-9 of the (M1+M2−X) kg of working medium and the H kg of working medium, a mixed heat-releasing process 9-c of the (M1+M2) kg of working medium and the H kg of working medium, a depressurization process c-d of the (M1+H) kg of working medium, a heat-releasing and condensation process d-1 of the (M1+H) kg of working medium.
  • (2) From the Perspective of Energy Conversion.
  • {circle around (1)} Heat absorption processes: the absorbed heat in the process e-c of the H kg of working medium is provided by the heat-releasing in the process 8-9 of the (M1+M2−X) kg of working medium and the process 9-c of the (M1+M2) kg of working medium, or by an external heat source at the same time. The absorbed heat in the process 2-b of the M1 kg of working medium is provided by the mixed heat-releasing of the M kg of working medium, or by an external heat source at the same time. In the process b-3 of the (M1+M) kg of working medium, the process 4-5 of the (M1+M) kg of working medium, the process 5-6 of the (M1+M2) kg of working medium and the process 6-7 of the (M1+M2−X) kg of working medium, the absorbed heat is provided by an external heat source.
  • {circle around (2)} Heat-releasing processes. In the process 8-9, the (M1+M2−X) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M2−M) kg of working medium is lowered to state 9. In the process 9-c, the (M1+M2) kg of working medium mixes with and releases heat to the H kg of working medium, and the temperature of the (M1+M2) kg of working medium is lowered to state c. The heat released by the (M1+H) kg of working medium in process d-1 is usually released to the low-temperature heat sink, or be supplied to the heat user when cogeneration is applicable.
  • {circle around (3)} Energy conversion processes. The pressurization process 1-2 of the M1 kg of working medium and the pressurization process 1-e of H kg of working medium are usually achieved by pumps. The pressurization process c-a of the M2 kg of working medium and the pressurization process a-5 of the (M2−M) kg of working medium are usually achieved by compressors. The depressurization (and expansion) process 3-4 of the (M1+M) kg of working medium, the depressurization (and expansion) process 6-9 of the X kg of working medium, the depressurization (and expansion) process 7-8 of the (M1+M2−X) kg of working medium and the depressurization (and expansion) process c-d of the (M1+H) kg of working medium are usually achieved by expanders. The total expansion work output is greater than the total pressurization work input; therefore, thermal energy is converted into power (the cycle's net work), and the single-working-medium vapor combined cycle is completed.
  • The technical effects of the present invention invention: The single-working-medium vapor combined cycle proposed by the present invention has the following effects and advantages:
  • (1) A basic theory of thermal energy (temperature difference) utilization has been created.
  • (2) The present invention greatly reduces the amount of heat absorbed in the phase-change region, and correspondingly increases the amount of heat absorbed in the high-temperature region or the variable temperature region. Therefore, the single-working-medium vapor combined cycle can achieve high efficiency.
  • (3) The present invention possesses simple methods, reasonable processes and good applicability. It is a common technology to realize the effective utilization of temperature differences.
  • (4) The present invention only uses a single working medium, which is easy to produce and store. The present invention can also reduce the operation cost and improve the flexibility of cycle regulation.
  • (5) The processes in the present invention are shared and reduced, which provides a theoretical basis for reducing equipment investment.
  • (6) In the high temperature region or the variable temperature region, both the cycle's working medium and the heat source medium conduct variable-temperature processes; therefore, the temperature difference loss is reduced and the efficiency is improved.
  • (7) The present invention adopts the low-pressure and high-temperature operation mode in the high-temperature region; therefore, the contradiction among thermal efficiency, the working medium's parameters and the material's temperature resistance and pressure resistance abilities, which is common in traditional vapor power devices, can be resolved.
  • (8) Under the precondition of achieving a high thermal efficiency, the vapor power device provided in the present invention can operate at a low pressure. The present invention provides theoretical support for improving the safety of device operation.
  • (9) The present invention possesses a wide range of applicable working media. The present invention can match energy supply with demand well. It is flexible to match the working medium and the working parameters.
  • (10) The present invention expands the range of thermodynamic cycles for temperature difference utilization, and contributes to a higher-efficiency power generation of high-temperature heat sources and variable-temperature heat sources.

Claims (12)

What is claimed is:
1. A single-working-medium vapor combined cycle method consisting of twelve processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (5) of the M2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set the state (6) to (7) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (7) to (8) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (9) to (1) of the (M1+H) kg of working medium.
2. A single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (7) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (6) of the M2 kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
3. A single-working-medium vapor combined cycle method consisting of thirteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (5) of the M2 kg of working medium, performing a heat-absorption process to set the state (5) to (6) of the M2 kg of working medium, performing a depressurization process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set the state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
4. A single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (9) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (6) of the M2 kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the M2 kg of working medium, performing a depressurization process to set the state (7) to (8) of the M2 kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the M2 kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
5. A single-working-medium vapor combined cycle method consisting of fourteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a depressurization process to set the state (5) to (6) of the M1 kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the M1 kg of working medium and the H kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (7) of the M2 kg of working medium, performing a heat-absorption process to set the state (7) to (8) of the M2 kg of working medium, performing a depressurization process to set the state (8) to (9) of the M2 kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
6. A single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set the state (2) to (3) of the M1 kg of working medium, performing a depressurization process to set the state (3) to (4) of the M1 kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the M1 kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (5) of the M2 kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set a state (6) to (9) of the X kg of working medium, performing a heat-absorption process to set a state (6) to (7) of the (M1+M2−X) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2−X) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2−X) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
7. A single-working-medium vapor combined cycle method consisting of fifteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (8) of the H kg of working medium, performing a pressurization process to set a state (8) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set the state (6) to (7) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (7) to (8) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (9) to (1) of the (M1+H) kg of working medium.
8. A single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (7) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (6) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
9. A single-working-medium vapor combined cycle method consisting of sixteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (7) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (9) of the H kg of working medium, performing a pressurization process to set a state (9) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (5) to (6) of the (M2−M) kg of working medium, performing a depressurization process to set a state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (9) to (c) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (c) to (1) of the (M1+H) kg of working medium.
10. A single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (9) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (6) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M2−M) kg of working medium, performing a depressurization process to set a state (7) to (8) of the (M2−M) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M2−M) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
11. A single-working-medium vapor combined cycle method consisting of seventeen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a depressurization process to set the state (5) to (6) of the (M1+M) kg of working medium, performing a mixed heat-releasing process to set a state (6) to (9) of the (M1+M) kg of working medium and the H kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (7) of the (M2−M) kg of working medium, performing a heat-absorption process to set the state (7) to (8) of the (M2−M) kg of working medium, performing a depressurization process to set a state (8) to (9) of the (M2−M) kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
12. A single-working-medium vapor combined cycle method consisting of eighteen processes which are conducted with M1 kg of working medium, M2 kg of working medium and H kg of working medium separately or jointly: performing a pressurization process to set a state (1) to (2) of the M1 kg of working medium, performing a heat-absorption process to set the state (2) to (b) of the M1 kg of working medium, performing a heat-absorption and vaporization process to set a state (b) to (3) of the (M1+M) kg of working medium, performing a depressurization process to set the state (3) to (4) of the (M1+M) kg of working medium, performing a heat-absorption process to set the state (4) to (5) of the (M1+M) kg of working medium, performing a pressurization process to set a state (1) to (e) of the H kg of working medium, performing a heat-absorption process to set the state (e) to (c) of the H kg of working medium, performing a pressurization process to set a state (c) to (a) of the M2 kg of working medium, performing a heat-releasing and condensation process to set a state (a) to (b) of the M kg of working medium, performing a pressurization process to set a state (a) to (5) of the (M2−M) kg of working medium, performing a heat-absorption process to set a state (5) to (6) of the (M1+M2) kg of working medium, performing a depressurization process to set a state (6) to (9) of the X kg of working medium, performing a heat-absorption process to set the state (6) to (7) of the (M1+M2−X) kg of working medium, performing a depressurization process to set the state (7) to (8) of the (M1+M2−X) kg of working medium, performing a mixed heat-releasing process to set a state (8) to (9) of the (M1+M2−X) kg of working medium and the H kg of working medium, performing a mixed heat-releasing process to set a state (9) to (c) of the (M1+M2) kg of working medium and the H kg of working medium, performing a depressurization process to set a state (c) to (d) of the (M1+H) kg of working medium, performing a heat-releasing and condensation process to set the state (d) to (1) of the (M1+H) kg of working medium.
US17/606,446 2019-04-25 2020-04-20 Single-working-medium vapor combined cycle Abandoned US20220195895A1 (en)

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