CN111852586A - Combined cycle power plant - Google Patents

Combined cycle power plant Download PDF

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Publication number
CN111852586A
CN111852586A CN202010433103.2A CN202010433103A CN111852586A CN 111852586 A CN111852586 A CN 111852586A CN 202010433103 A CN202010433103 A CN 202010433103A CN 111852586 A CN111852586 A CN 111852586A
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CN
China
Prior art keywords
communicated
evaporator
expander
temperature heat
circulating pump
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Pending
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CN202010433103.2A
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Chinese (zh)
Inventor
李鸿瑞
李华玉
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Individual
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Individual
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K7/00—Steam 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steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K13/00—General layout or general methods of operation of complete plants
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K17/00—Using steam or condensate extracted or exhausted from steam engine plant
    • F01K17/02—Using steam or condensate extracted or exhausted from steam engine plant for heating purposes, e.g. industrial, domestic
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K21/00—Steam engine plants not otherwise provided for
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K9/00—Plants characterised by condensers arranged or modified to co-operate with the engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B35/00—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for
    • F04B35/006—Piston pumps specially adapted for elastic fluids and characterised by the driving means to their working members, or by combination with, or adaptation to, specific driving engines or motors, not otherwise provided for driven by steam engines
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B37/00—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
    • F04B37/10—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use
    • F04B37/12—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for special use to obtain high pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B9/00—Piston machines or pumps characterised by the driving or driven means to or from their working members
    • F04B9/08—Piston machines or pumps characterised by the driving or driven means to or from their working members the means being fluid
    • F04B9/12—Piston machines or pumps characterised by the driving or driven means to or from their working members the means being fluid the fluid being elastic, e.g. steam or air
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

The invention provides a combined cycle power device, and belongs to the technical field of energy and power. The condenser is provided with a condensate pipeline, the evaporator is further provided with a steam channel communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel communicated with the expander, the condenser is also provided with a low-pressure steam channel communicated with the second evaporator, the evaporator is also provided with a low-pressure steam channel communicated with the evaporator, and the low-pressure steam channel is respectively communicated with the compressor directly and the condenser through the second expander; the high-temperature heat exchanger and the second evaporator are also respectively communicated with the outside through a heat source medium channel, the condenser is also communicated with the outside through a cooling medium channel, and the expander is connected with the compressor and transmits power to form a combined cycle power device.

Description

Combined cycle power plant
The technical field is as follows:
the invention belongs to the technical field of energy and power.
Background art:
Cold demand, heat demand and power demand, which are common in human life and production; among them, the conversion of thermal energy into mechanical energy is an important way to obtain and provide power. In general, the temperature of the heat source decreases with the release of heat, and the heat source is variable. When fossil fuel is used as a source energy source, the heat source has the dual characteristics of high temperature and variable temperature, so that a power device based on single thermodynamic cycle is difficult to convert more heat energy into mechanical energy; for high-quality fuel, high thermal efficiency can be obtained by adopting the traditional gas-steam combined cycle, but the problems of high manufacturing cost, large investment, thermal efficiency to be improved and the like still exist.
Taking an external combustion type steam power device as an example, a heat source of the external combustion type steam power device belongs to a high-temperature and variable-temperature heat source; when Rankine cycle is taken as a theoretical basis and steam is taken as a cycle working medium to realize thermal power conversion, the limitation of temperature resistance, pressure resistance and safety of materials is applied, so that no matter what parameters are adopted for operation, large temperature difference loss exists between the cycle working medium and a heat source, irreversible loss is large, the heat efficiency is low, and the potential for improving the heat efficiency is great.
People need to simply, actively, safely and efficiently utilize heat energy to obtain power, and therefore the combined cycle steam power plant has the advantages of high heat efficiency, high safety, adaptability to high-temperature heat sources or variable-temperature heat sources and capability of coping with various fuels.
The invention content is as follows:
the invention mainly aims to provide a combined cycle power plant, and the specific contents are set forth in the following sections:
1. the combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser is provided with a condensate pipeline, the evaporator is further provided with a steam channel communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel communicated with the expander, the condenser is also provided with a low-pressure steam channel communicated with the second evaporator, the evaporator is also provided with a low-pressure steam channel communicated with the evaporator, and the low-pressure steam channel is respectively communicated with the compressor directly and the condenser through the second expander; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
2. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a heat supply device; the condenser is provided with a condensate pipeline, the evaporator is further provided with a steam channel which is communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the heat supply device, and the heat supply device is also provided with a low-pressure steam channel which is respectively communicated with the compressor directly and is communicated with the condenser of the second expander through a second circulating pump and a second evaporator; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator is also provided with a heat source medium channel communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, the heat supplier is also provided with a heated medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
3. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser is provided with a condensate pipeline, a steam channel of the evaporator is communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel communicated with an expander, the condenser is also provided with a low-pressure steam channel communicated with the evaporator after the condensate pipeline is communicated with the second evaporator through a second circulating pump, the second evaporator is provided with a steam channel communicated with the expander through a middle steam inlet channel, and the evaporator is also provided with a low-pressure steam channel which is respectively communicated with the compressor directly and communicated with the condenser through the second expander; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
4. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser is provided with a condensate pipeline, the evaporator is further provided with a steam channel communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel communicated with an expander, the condenser is also provided with a low-pressure steam channel communicated with the second evaporator, the second evaporator is further provided with a steam channel communicated with the expander through a middle steam inlet channel, and the second evaporator and the low-pressure steam channel are respectively directly communicated with the compressor and the condenser through the second expander; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator is also provided with a heat source medium channel communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
5. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser is provided with a condensate pipeline, the evaporator is further provided with a steam channel communicated with the high-temperature heat exchanger after the condensate pipeline is communicated with the evaporator through a circulating pump, the compressor is provided with a steam channel communicated with the high-temperature heat exchanger, the high-temperature heat exchanger is also provided with a steam channel communicated with the expander, the condenser is also provided with a condensate pipeline, the second evaporator is communicated with the second evaporator through a second circulating pump, the second evaporator is further provided with a steam channel communicated with the expander through a middle steam inlet channel, the expander is also provided with a low-pressure steam channel communicated with the evaporator, the evaporator is also provided with a low-pressure steam channel communicated with the second evaporator, and the second evaporator is also provided with a low-pressure steam channel which is respectively communicated; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
6. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser is provided with a condensate pipeline which is communicated with the evaporator through a circulating pump, the evaporator is also provided with a steam channel which is communicated with a high-temperature heat exchanger through a high-temperature heat regenerator, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger through the high-temperature heat regenerator, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the evaporator through a low-pressure steam channel which is communicated with the evaporator after the condensate pipeline is communicated with the second evaporator through a second circulating pump, and the evaporator is also provided with a low-pressure steam channel which is communicated with the compressor directly and the condenser through the second expander respectively; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
7. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator, a heat supply device and a high-temperature heat regenerator; the condenser is provided with a condensate pipeline which is communicated with the evaporator through a circulating pump, the evaporator is also provided with a steam channel which is communicated with a high-temperature heat exchanger through a high-temperature heat regenerator, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger through the high-temperature heat regenerator, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the heat supply device through the high-temperature heat regenerator after the condensate pipeline is communicated with the second evaporator through a second circulating pump, and the second evaporator is also provided with a steam channel which is communicated with the expander through an intermediate steam inlet channel; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator is also provided with a heat source medium channel communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, the heat supplier is also provided with a heated medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
8. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser is provided with a condensate pipeline which is communicated with the evaporator through a circulating pump, the evaporator is also provided with a steam channel which is communicated with a high-temperature heat exchanger through a high-temperature heat regenerator, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger through the high-temperature heat regenerator, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the evaporator through a high-temperature heat regenerator after the condensate pipeline is communicated with the second evaporator through a second circulating pump, and the evaporator is also provided with a steam channel which is communicated with the expander through an intermediate steam inlet channel; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
9. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser is provided with a condensate pipeline which is communicated with the evaporator through a circulating pump, the evaporator is also provided with a steam channel which is communicated with a high-temperature heat exchanger through a high-temperature heat regenerator, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger through the high-temperature heat regenerator, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the second evaporator through a high-temperature heat regenerator, and the second evaporator is also provided with a low-pressure steam channel which is respectively communicated with the compressor directly and the condenser through the second expander; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator is also provided with a heat source medium channel communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
10. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser is provided with a condensate pipeline which is communicated with the evaporator through a circulating pump, the evaporator is also provided with a steam channel which is communicated with a high-temperature heat exchanger through a high-temperature heat regenerator, the compressor is provided with a steam channel which is communicated with the high-temperature heat exchanger through the high-temperature heat regenerator, the high-temperature heat exchanger is also provided with a steam channel which is communicated with the expander, the condenser is also provided with a low-pressure steam channel which is communicated with the second evaporator through a low-pressure steam channel which is also communicated with the second evaporator after the condensate pipeline is communicated with the second evaporator through a second circulating pump, and the second evaporator and the low-pressure steam channel are respectively and directly communicated with the compressor and the condenser through the second expander; the high-temperature heat exchanger is also provided with a heat source medium channel communicated with the outside, the condenser is also provided with a cooling medium channel communicated with the outside, the evaporator or the heat source medium channel is also communicated with the outside, the second evaporator is also provided with a heat source medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a combined cycle power device; wherein, or the expander is connected with the compressor, the circulating pump and the second circulating pump and transmits power.
11. A combined cycle power device is characterized in that a low-temperature heat regenerator and a third circulating pump are added in any one of the combined cycle power devices 1-10, a condenser with a condensate pipeline communicated with an evaporator through the circulating pump is adjusted to be a condenser with a condensate pipeline communicated with the low-temperature heat regenerator through the circulating pump, a compressor is additionally provided with a middle steam extraction channel communicated with the low-temperature heat regenerator, and the low-temperature heat regenerator is further communicated with the evaporator through the condensate pipeline through the third circulating pump to form the combined cycle power device.
12. A combined cycle power plant, in any of the combined cycle power plants described in items 1-11, a newly added heat regenerator and a newly added circulating pump are added, the condenser is adjusted to have a condensate pipeline communicated with a second evaporator through the second circulating pump, the condenser has a condensate pipeline communicated with the newly added heat regenerator through the second circulating pump, the compressor is additionally provided with a middle steam extraction channel communicated with the newly added heat regenerator, the newly added heat regenerator has a condensate pipeline communicated with the second evaporator through the newly added circulating pump, and a combined cycle power plant is formed.
Description of the drawings:
FIG. 1 is a schematic 1 st thermodynamic system diagram of a combined cycle power plant according to the present invention.
FIG. 2 is a schematic thermodynamic system diagram of the 2 nd principle of a combined cycle power plant provided in accordance with the present invention.
FIG. 3 is a schematic thermodynamic system diagram of the 3 rd principle of a combined cycle power plant provided in accordance with the present invention.
FIG. 4 is a diagram of a 4 th principal thermodynamic system of a combined cycle power plant provided in accordance with the present invention.
FIG. 5 is a diagram of a 5 th principal thermodynamic system of a combined cycle power plant provided in accordance with the present invention.
FIG. 6 is a 6 th principal thermodynamic system diagram of a combined cycle power plant provided in accordance with the present invention.
FIG. 7 is a 7 th principle thermodynamic system diagram of a combined cycle power plant provided in accordance with the present invention.
FIG. 8 is a diagram of an 8 th principle thermodynamic system of a combined cycle power plant provided in accordance with the present invention.
FIG. 9 is a diagram of a 9 th principal thermodynamic system of a combined cycle power plant provided in accordance with the present invention.
FIG. 10 is a 10 th principal thermodynamic system diagram of a combined cycle power plant provided in accordance with the present invention.
FIG. 11 is a diagram of a principal 11 thermodynamic system of a combined cycle power plant provided in accordance with the present invention.
FIG. 12 is a 12 th principle thermodynamic system diagram of a combined cycle power plant provided in accordance with the present invention.
In the figure, 1-compressor, 2-expander, 3-second expander, 4-circulating pump, 5-second circulating pump, 6-high temperature heat exchanger, 7-condenser, 8-evaporator (waste heat boiler), 9-second evaporator (second waste heat boiler), 10-heat supplier, 11-high temperature heat regenerator, 12-low temperature heat regenerator, 13-third circulating pump; a-adding a heat regenerator and B adding a circulating pump.
The specific implementation mode is as follows:
it is to be noted that, in the description of the structure and the flow, the repetition is not necessary; obvious flow is not described. The invention is described in detail below with reference to the figures and examples.
The combined cycle power plant shown in fig. 1 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser 7 is provided with a condensate pipeline, the evaporator 8 is communicated with the high-temperature heat exchanger 6 through a steam channel after the condensate pipeline is communicated with the evaporator 8 through the circulating pump 4, the compressor 2 is provided with a steam channel communicated with the high-temperature heat exchanger 6, the high-temperature heat exchanger 6 is also provided with a steam channel communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline, the second evaporator 9 is communicated with the second evaporator 9 through a second circulating pump 5, the second evaporator 9 is also provided with a steam channel communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is also provided with a low-pressure steam channel communicated with the second evaporator 9, the second evaporator 9 is also provided with a low-pressure steam channel communicated with the evaporator 8, and the evaporator 8 is also provided with a low-pressure steam channel which is respectively communicated with the compressor 2 directly; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 flows through the expander 1 to reduce pressure and work; the second path of condensate of the condenser 7 is boosted by a second circulating pump 5 and enters a second evaporator 9, absorbs heat, is heated, vaporized and overheated, and then enters the expansion machine 1 through a middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 gradually releases heat and cools through the second evaporator 9 and the evaporator 8, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path enters the condenser 7 to release heat and condense after flowing through the second expander 3 to reduce the pressure and do work; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 2 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a heat supply device; the condenser 7 has a condensate pipeline, after the condensate pipeline is communicated with the evaporator 8 through the circulating pump 4, the evaporator 8 has a steam channel to communicate with the high-temperature heat exchanger 6, the compressor 2 has a steam channel to communicate with the high-temperature heat exchanger 6, the high-temperature heat exchanger 6 also has a steam channel to communicate with the expander 1, the condenser 7 also has a condensate pipeline, after the condensate pipeline is communicated with the second evaporator 9 through the second circulating pump 5, the second evaporator 9 has a steam channel to communicate with the expander 1 through the middle steam inlet channel, the expander 1 also has a low-pressure steam channel to communicate with the heat supply device 10, the heat supply device 10 also has a low-pressure steam channel to directly communicate with the compressor 2 and communicate with the condenser 7 through the second expander 3 respectively; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the evaporator 8 is also provided with a heat source medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, the heat supplier 10 is also provided with a heated medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 flows through the expander 1 to reduce pressure and work; the second path of condensate of the condenser 7 is boosted by a second circulating pump 5 and enters a second evaporator 9, absorbs heat, is heated, vaporized and overheated, and then enters the expansion machine 1 through a middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 is subjected to heat release and temperature reduction through the heat supply device 10, and then is divided into two paths, wherein the first path enters the compressor 2 for pressure rise and temperature rise, and the second path enters the condenser 7 for heat release and condensation after passing through the second expander 3 for pressure reduction and work done; the heat source medium provides driving heat load through the high-temperature heat exchanger 6, the evaporator 8 and the second evaporator 9, the cooling medium takes low-temperature heat load through the condenser 7, the medium to be heated takes medium-temperature heat load through the heater 10, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside, so that a combined cycle power device is formed.
The combined cycle power plant shown in fig. 3 is implemented as follows:
(1) Structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser 7 is provided with a condensate pipeline, the evaporator 8 is communicated with the high-temperature heat exchanger 6 through a steam channel after the condensate pipeline is communicated with the evaporator 8 through the circulating pump 4, the compressor 2 is provided with a steam channel communicated with the high-temperature heat exchanger 6, the high-temperature heat exchanger 6 is also provided with a steam channel communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline, the second evaporator 9 is communicated with the second evaporator 9 through a second circulating pump 5, the second evaporator 9 is provided with a steam channel communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is also provided with a low-pressure steam channel communicated with the evaporator 8, and the evaporator 8 is also provided with a low-pressure steam channel which is respectively communicated with the compressor 2 directly and the condenser 7 through; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 flows through the expander 1 to reduce pressure and work; the second path of condensate of the condenser 7 is boosted by a second circulating pump 5 and enters a second evaporator 9, absorbs heat, is heated, vaporized and overheated, and then enters the expansion machine 1 through a middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 passes through the evaporator 8 to release heat and reduce temperature, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path passes through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 4 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser 7 is provided with a condensate pipeline, the evaporator 8 is communicated with the high-temperature heat exchanger 6 through a steam channel after the condensate pipeline is communicated with the evaporator 8 through the circulating pump 4, the compressor 2 is provided with a steam channel communicated with the high-temperature heat exchanger 6, the high-temperature heat exchanger 6 is also provided with a steam channel communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline, the second evaporator 9 is communicated with the second evaporator 9 through a second circulating pump 5, the second evaporator 9 is provided with a steam channel communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is also provided with a low-pressure steam channel communicated with the second evaporator 9, and the second evaporator 9 is also provided with a low-pressure steam channel which is respectively communicated with the compressor 2 directly and communicated with the condenser 7; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the evaporator 8 is also provided with a heat source medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 flows through the expander 1 to reduce pressure and work; the second path of condensate of the condenser 7 is boosted by a second circulating pump 5 and enters a second evaporator 9, absorbs heat, is heated, vaporized and overheated, and then enters the expansion machine 1 through a middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 passes through the second evaporator 9 to release heat and reduce temperature, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path passes through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6, the evaporator 8 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside, so that a combined cycle power device is formed.
The combined cycle power plant shown in fig. 5 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser 7 is provided with a condensate pipeline, the evaporator 8 is communicated with the high-temperature heat exchanger 6 through a steam channel after the condensate pipeline is communicated with the evaporator 8 through the circulating pump 4, the compressor 2 is provided with a steam channel communicated with the high-temperature heat exchanger 6, the high-temperature heat exchanger 6 is also provided with a steam channel communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline, the second evaporator 9 is communicated with the second evaporator 9 through a second circulating pump 5, the second evaporator 9 is further provided with a steam channel communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is also provided with a low-pressure steam channel communicated with the evaporator 8, the evaporator 8 is also provided with a low-pressure steam channel communicated with the second evaporator 9, and the second evaporator 9 is also provided with a low-pressure steam channel which is respectively communicated with the compressor 2 directly; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 flows through the expander 1 to reduce pressure and work; the second path of condensate of the condenser 7 is boosted by a second circulating pump 5 and enters a second evaporator 9, absorbs heat, is heated, vaporized and overheated, and then enters the expansion machine 1 through a middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 gradually releases heat and cools through the evaporator 8 and the second evaporator 9, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path enters the condenser 7 to release heat and condense after flowing through the second expander 3 to reduce the pressure and do work; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 6 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser 7 is provided with a condensate pipeline which is communicated with the evaporator 8 through a circulating pump 4, the evaporator 8 is also provided with a steam channel which is communicated with a high-temperature heat exchanger 6 through a high-temperature heat regenerator 11, the compressor 2 is provided with a steam channel which is communicated with the high-temperature heat exchanger 6 through the high-temperature heat regenerator 11, the high-temperature heat exchanger 6 is also provided with a steam channel which is communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline which is communicated with a second evaporator 9 through a second circulating pump 5, then the steam channel of the second evaporator 9 is communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is also provided with a low-pressure steam channel which is communicated with the second evaporator 9 through the high-temperature heat regenerator 11, the second evaporator 9 is also provided with a low-pressure steam channel which is communicated with the evaporator 8, and the evaporator 8 is also provided with a low-pressure; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, flows through the high-temperature heat regenerator 11 to absorb heat, raise temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; steam discharged by the compressor 2 flows through the high-temperature heat regenerator 11 to absorb heat and raise the temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise the temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 flows through the high-temperature heat regenerator 11, the second evaporator 9 and the evaporator 8 to gradually release heat and cool, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and heat, and the second path flows through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 7 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator, a heat supply device and a high-temperature heat regenerator; the condenser 7 is provided with a condensate pipeline which is communicated with the evaporator 8 through a circulating pump 4, the evaporator 8 is also provided with a steam channel which is communicated with a high-temperature heat exchanger 6 through a high-temperature heat regenerator 11, the compressor 2 is provided with a steam channel which is communicated with the high-temperature heat exchanger 6 through the high-temperature heat regenerator 11, the high-temperature heat exchanger 6 is also provided with a steam channel which is communicated with the expander 1, the condenser 7 is also provided with a low-pressure steam channel which is communicated with the heat supply device 10 through the high-temperature heat regenerator 11 after the condensate pipeline is communicated with the second evaporator 9 through a second circulating pump 5, and the second evaporator 9 is further provided with a steam channel which is communicated with the expander 1 through a middle steam inlet channel, and the heat supply device 10 is also provided with a low-pressure steam channel which is respectively; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the evaporator 8 is also provided with a heat source medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, the heat supplier 10 is also provided with a heated medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, flows through the high-temperature heat regenerator 11 to absorb heat, raise temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; steam discharged by the compressor 2 flows through the high-temperature heat regenerator 11 to absorb heat and raise the temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise the temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 flows through the high-temperature heat regenerator 11 and the heat supplier 10 to gradually release heat and cool, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path flows through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6, the evaporator 8 and the second evaporator 9, the cooling medium takes low-temperature heat load through the condenser 7, the medium to be heated takes medium-temperature heat load through the heater 10, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside, so that a combined cycle power device is formed.
The combined cycle power plant shown in fig. 8 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser 7 is provided with a condensate pipeline which is communicated with the evaporator 8 through a circulating pump 4, the evaporator 8 is also provided with a steam channel which is communicated with a high-temperature heat exchanger 6 through a high-temperature heat regenerator 11, the compressor 2 is provided with a steam channel which is communicated with the high-temperature heat exchanger 6 through the high-temperature heat regenerator 11, the high-temperature heat exchanger 6 is also provided with a steam channel which is communicated with the expander 1, the condenser 7 is also provided with a low-pressure steam channel which is communicated with the evaporator 8 through the high-temperature heat regenerator 11 after the condensate pipeline is communicated with the second evaporator 9 through a second circulating pump 5, and the second evaporator 9 is further provided with a steam channel which is communicated with the expander 1 through an intermediate steam inlet channel, and the evaporator 8 is also provided with a low-pressure steam channel which is respectively communicated with the compressor; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, flows through the high-temperature heat regenerator 11 to absorb heat, raise temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; steam discharged by the compressor 2 flows through the high-temperature heat regenerator 11 to absorb heat and raise the temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise the temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 flows through the high-temperature heat regenerator 11 and the evaporator 8 to gradually release heat and cool, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path flows through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 9 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser 7 is provided with a condensate pipeline which is communicated with the evaporator 8 through a circulating pump 4, the evaporator 8 is also provided with a steam channel which is communicated with a high-temperature heat exchanger 6 through a high-temperature heat regenerator 11, the compressor 2 is provided with a steam channel which is communicated with the high-temperature heat exchanger 6 through the high-temperature heat regenerator 11, the high-temperature heat exchanger 6 is also provided with a steam channel which is communicated with the expander 1, the condenser 7 is also provided with a low-pressure steam channel which is communicated with the second evaporator 9 through the high-temperature heat regenerator 11 after the condensate pipeline is communicated with the second evaporator 9 through a second circulating pump 5, the steam channel of the second evaporator 9 is communicated with the expander 1 through an intermediate steam inlet channel, and the second evaporator 9 is also provided with a low-pressure steam channel which is respectively communicated with the compressor 2 directly and the condenser 7 through; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the evaporator 8 is also provided with a heat source medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, flows through the high-temperature heat regenerator 11 to absorb heat, raise temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; steam discharged by the compressor 2 flows through the high-temperature heat regenerator 11 to absorb heat and raise the temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise the temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 flows through the high-temperature heat regenerator 11 and the second evaporator 9 to gradually release heat and cool, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and the temperature, and the second path flows through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6, the evaporator 8 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside, so that a combined cycle power device is formed.
The combined cycle power plant shown in fig. 10 is implemented as follows:
(1) structurally, the system mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser 7 is provided with a condensate pipeline which is communicated with the evaporator 8 through a circulating pump 4, the evaporator 8 is also provided with a steam channel which is communicated with a high-temperature heat exchanger 6 through a high-temperature heat regenerator 11, the compressor 2 is provided with a steam channel which is communicated with the high-temperature heat exchanger 6 through the high-temperature heat regenerator 11, the high-temperature heat exchanger 6 is also provided with a steam channel which is communicated with the expander 1, the condenser 7 is also provided with a condensate pipeline which is communicated with the second evaporator 9 through a second circulating pump 5, then the second evaporator 9 is further provided with a steam channel which is communicated with the expander 1 through an intermediate steam inlet channel, the expander 1 is further provided with a low-pressure steam channel which is communicated with the evaporator 8 through the high-temperature heat regenerator 11, the evaporator 8 is further provided with a low-pressure steam channel which is communicated with the second evaporator 9, and the second evaporator 9 is further; the high-temperature heat exchanger 6 is also provided with a heat source medium channel communicated with the outside, the condenser 7 is also provided with a cooling medium channel communicated with the outside, the second evaporator 9 is also provided with a heat source medium channel communicated with the outside, and the expander 1 is connected with the compressor 2 and transmits power.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, flows through the high-temperature heat regenerator 11 to absorb heat, raise temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; steam discharged by the compressor 2 flows through the high-temperature heat regenerator 11 to absorb heat and raise the temperature, and then enters the high-temperature heat exchanger 6 to absorb heat and raise the temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 flows through the high-temperature heat regenerator 11, the evaporator 8 and the second evaporator 9 to gradually release heat and cool, and then is divided into two paths, wherein the first path enters the compressor 2 to increase the pressure and heat, and the second path flows through the second expander 3 to reduce the pressure and do work and then enters the condenser 7 to release heat and condense; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in FIG. 11 is implemented as follows:
(1) structurally, in the combined cycle power plant shown in fig. 1, a low-temperature heat regenerator and a third circulating pump are added, a condensate pipeline of a condenser 7 is communicated with an evaporator 8 through a circulating pump 4, the condenser 7 is adjusted to be communicated with a low-temperature heat regenerator 12 through the circulating pump 4, a middle steam extraction channel is additionally arranged on a compressor 2 and is communicated with the low-temperature heat regenerator 12, and the low-temperature heat regenerator 12 is communicated with the evaporator 8 through a condensate pipeline of the third circulating pump 13.
(2) In the process, the condensate of the condenser 7 is boosted by the circulating pump 4 and enters the low-temperature heat regenerator 12, and is mixed with the extracted steam from the compressor 2 to absorb heat and raise the temperature, and the extracted steam is mixed with the condensate to release heat and condense; the condensate of the low-temperature heat regenerator 12 is boosted by a third circulating pump 13 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, and then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature; the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce the pressure and do work, the second path of condensate of the condenser 7 enters the second evaporator 9 after being boosted by the second circulating pump 5 to absorb heat, raise the temperature, vaporize and overheat, and then enters the expander 1 to reduce the pressure and do work through the middle steam inlet channel; the low-pressure steam discharged by the expander 1 gradually releases heat and cools through the second evaporator 9 and the evaporator 8, and then is divided into two paths, namely the first path enters the compressor 2, and the second path enters the condenser 7 to release heat and condense after passing through the second expander 3 to reduce pressure and do work; the low-pressure steam entering the compressor 2 is compressed to a certain degree and then divided into two paths, wherein the first path enters the low-temperature heat regenerator 12 through the middle steam extraction channel, and the second path continues to increase the pressure and the temperature; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The combined cycle power plant shown in fig. 12 is implemented as follows:
(1) structurally, in the combined cycle power plant shown in fig. 1, a newly added heat regenerator and a newly added circulating pump are added, a condensate pipeline of a condenser 7 is communicated with a second evaporator 9 through a second circulating pump 5 and is adjusted to be communicated with the newly added heat regenerator A through the second circulating pump 5, a middle steam extraction channel of the compressor 7 is additionally arranged to be communicated with the newly added heat regenerator A, and the newly added heat regenerator A is communicated with the second evaporator 9 through a condensate pipeline of the newly added circulating pump B.
(2) In the process, the first path of condensate of the condenser 7 is boosted by the circulating pump 4 and enters the evaporator 8 to absorb heat, raise temperature, vaporize and overheat, then enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, the steam discharged by the compressor 2 enters the high-temperature heat exchanger 6 to absorb heat and raise temperature, and the steam discharged by the high-temperature heat exchanger 6 enters the expander 1 to reduce pressure and do work; the second path of condensate of the condenser 7 is boosted by the second circulating pump 5 and enters the newly-added heat regenerator A, and is mixed with the extracted steam from the compressor 2 to absorb heat and raise the temperature, and the extracted steam is mixed with the condensate to release heat and condense; the condensate of the newly added heat regenerator A is boosted by the newly added circulating pump B and enters the second evaporator 9 to absorb heat, raise temperature, vaporize and overheat, and then enters the expansion machine 1 through the middle steam inlet channel to reduce pressure and do work; the low-pressure steam discharged by the expander 1 gradually releases heat and cools through the second evaporator 9 and the evaporator 8, and then is divided into two paths, namely the first path enters the compressor 2, and the second path enters the condenser 7 to release heat and condense after passing through the second expander 3 to reduce pressure and do work; the low-pressure steam entering the compressor 2 is compressed to a certain degree and then is divided into two paths, wherein the first path enters the newly-added heat regenerator A through the middle steam extraction channel, and the second path continues to increase the pressure and the temperature; the heat source medium provides driving heat load through the high-temperature heat exchanger 6 and the second evaporator 9, the cooling medium takes away low-temperature heat load through the condenser 7, the expander 1 provides power for the compressor 2, and the expander 1 and the second expander 3 provide power to the outside to form a combined cycle power device.
The effect that the technology of the invention can realize-the combined cycle power device provided by the invention has the following effects and advantages:
(1) the circulating working medium completes high-temperature heat absorption under low pressure, the temperature difference loss between the circulating working medium and a high-temperature heat source is small, and the heat efficiency of a system and the safety of the device are improved.
(2) The cycle working medium mainly depends on the condensation phase change process to realize low-temperature heat release, the temperature difference loss between the cycle working medium and the environment is controllable, and the heat efficiency of the device is favorably improved.
(3) The low-pressure high-temperature operation mode is adopted in the high-temperature area, the contradiction that the heat efficiency, the circulating medium parameters and the pressure and temperature resistance of the pipe are difficult to reconcile in the traditional steam power device is solved, so that the temperature difference loss between a heat source and the circulating medium can be greatly reduced, and the heat efficiency of the device is greatly improved.
(4) The lower part is circulated and graded, which is beneficial to reducing the irreversible loss of temperature difference and providing the thermal efficiency of the device.
(5) The equipment is shared, the heat absorption process of the lower cycle, namely Rankine cycle, is increased, and the heat efficiency of the device is improved.
(6) And a single working medium is adopted, so that the operation cost is reduced, and the adjustment flexibility of the thermal power device is improved.
(7) When the high-temperature expansion machine is shared, the number of core equipment is reduced, and the system investment is favorably reduced and the heat efficiency of the device is favorably improved.
(8) The device can effectively deal with high-temperature heat sources and variable-temperature heat sources, and deal with high-quality fuels and non-high-quality fuels, and has wide application range.
(9) On the premise of realizing high thermal efficiency, low-pressure operation can be selected, so that the operation safety of the device is greatly improved.
(10) The heat recovery of the enterprise device can be simply, actively, safely and efficiently realized.
(11) The heat efficiency can be effectively improved by applying the heat exchanger to the lower end of the gas-steam combined cycle.
(12) When the system is applied to a coal-fired thermodynamic system, the original advantages of the traditional steam power cycle, namely water vapor as a working medium, can be kept, and the working parameter range is wide; according to the actual condition, the working in the subcritical, critical, supercritical or ultra supercritical state can be selected.

Claims (12)

1. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through the circulating pump (4), then the evaporator (8) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6), the compressor (2) is provided with a steam channel communicated with the high-temperature heat exchanger (6), the high-temperature heat exchanger (6) is also provided with a steam channel communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline communicated with the second evaporator (9) through the second circulating pump (5), then the second evaporator (9) is provided with a steam channel communicated with the expander (1) through a middle steam inlet channel, the expander (1) is also provided with a low-pressure steam channel communicated with the second evaporator (9), the second evaporator (9) is also provided with a low-pressure steam channel communicated with the evaporator (8), and the evaporator (8) and the low-pressure steam channel are respectively and directly communicated with the compressor (2) and communicated with the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
2. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a heat supply device; the condenser (7) is provided with a condensate pipeline, the evaporator (8) is communicated with the high-temperature heat exchanger (6) through a circulating pump (4), a steam channel is communicated with the high-temperature heat exchanger (6), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a low-pressure steam channel which is communicated with the heat supply device (10), and the heat supply device (10) and the low-pressure steam channel are respectively communicated with the compressor (2) and the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) is also provided with a heat source medium channel communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, the heat supplier (10) is also provided with a heated medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
3. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser (7) is provided with a condensate pipeline, the evaporator (8) is communicated with the high-temperature heat exchanger (6) through a circulating pump (4), a steam channel is communicated with the high-temperature heat exchanger (6), the high-temperature heat exchanger (6) is also provided with a steam channel communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline, the second evaporator (9) is communicated with the second evaporator (9) through a second circulating pump (5), a steam channel is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel communicated with the evaporator (8), and the evaporator (8) and the low-pressure steam channel are respectively and directly communicated with the compressor (2) and communicated with the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
4. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser (7) is provided with a condensate pipeline, the evaporator (8) is communicated with the high-temperature heat exchanger (6) through a circulating pump (4), a steam channel is communicated with the high-temperature heat exchanger (6), the high-temperature heat exchanger (6) is also provided with a steam channel communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline, the second evaporator (9) is communicated with the second evaporator (9) through a second circulating pump (5), the steam channel is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel communicated with the second evaporator (9), and the second evaporator (9) is also provided with a low-pressure steam channel which is respectively communicated with the compressor (2) and the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) is also provided with a heat source medium channel communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
5. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator and a second evaporator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through the circulating pump (4), then the evaporator (8) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6), the compressor (2) is provided with a steam channel communicated with the high-temperature heat exchanger (6), the high-temperature heat exchanger (6) is also provided with a steam channel communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline communicated with the second evaporator (9) through the second circulating pump (5), then the second evaporator (9) is provided with a steam channel communicated with the expander (1) through a middle steam inlet channel, the expander (1) is also provided with a low-pressure steam channel communicated with the evaporator (8), the evaporator (8) is also provided with a low-pressure steam channel communicated with the second evaporator (9), the second evaporator (9) is also provided with a low-pressure steam channel which is respectively communicated with the compressor (2) directly and communicated with the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
6. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through a circulating pump (4), the evaporator (8) is also provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through a high-temperature heat regenerator (11), the compressor (2) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through the high-temperature heat regenerator (11), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline which is communicated with the second evaporator (9) through a second circulating pump (5), then the second evaporator (9) is also provided with a steam channel which is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel which is communicated with the second evaporator (9) through the high-temperature heat regenerator (11), the second evaporator (9) is also provided with a low-pressure steam channel which is communicated with the evaporator (8), and the evaporator (8) is also provided with a low-pressure (7) Communicating; the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
7. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator, a heat supply device and a high-temperature heat regenerator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through a circulating pump (4), the evaporator (8) is also provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through a high-temperature heat regenerator (11), the compressor (2) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through the high-temperature heat regenerator (11), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline which is communicated with the second evaporator (9) through a second circulating pump (5), then the second evaporator (9) is provided with a steam channel which is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel which is communicated with a heat supply device (10) through the high-temperature heat regenerator (11), and the heat supply device (10) is also provided with a low-pressure steam channel which is respectively communicated with; the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) is also provided with a heat source medium channel communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, the heat supplier (10) is also provided with a heated medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
8. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through a circulating pump (4), the evaporator (8) is also provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through a high-temperature heat regenerator (11), the compressor (2) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through the high-temperature heat regenerator (11), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline which is communicated with the second evaporator (9) through a second circulating pump (5), then the second evaporator (9) is provided with a steam channel which is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel which is communicated with the evaporator (8) through the high-temperature heat regenerator (11), and the evaporator (8) is also provided with a low-pressure steam channel which is respectively communicated with the compressor (2; the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
9. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through a circulating pump (4), the evaporator (8) is also provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through a high-temperature heat regenerator (11), the compressor (2) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through the high-temperature heat regenerator (11), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline which is communicated with the second evaporator (9) through a second circulating pump (5), then the second evaporator (9) is provided with a steam channel which is communicated with the expander (1) through a middle steam inlet channel, and the expander (1) is also provided with a low-pressure steam channel which is communicated with the second evaporator (9) through the, the second evaporator (9) is also provided with a low-pressure steam channel which is respectively communicated with the compressor (2) directly and communicated with the condenser (7) through the second expander (3); the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) is also provided with a heat source medium channel communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
10. The combined cycle power device mainly comprises an expander, a compressor, a second expander, a circulating pump, a second circulating pump, a high-temperature heat exchanger, a condenser, an evaporator, a second evaporator and a high-temperature heat regenerator; the condenser (7) is provided with a condensate pipeline which is communicated with the evaporator (8) through a circulating pump (4), the evaporator (8) is also provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through a high-temperature heat regenerator (11), the compressor (2) is provided with a steam channel which is communicated with the high-temperature heat exchanger (6) through the high-temperature heat regenerator (11), the high-temperature heat exchanger (6) is also provided with a steam channel which is communicated with the expander (1), the condenser (7) is also provided with a condensate pipeline which is communicated with the second evaporator (9) through a second circulating pump (5), then the second evaporator (9) is also provided with a steam channel which is communicated with the expander (1) through an intermediate steam inlet channel, the expander (1) is also provided with a low-pressure steam channel which is communicated with the evaporator (8) through the high-temperature heat regenerator (11), the evaporator (8) is also provided with a low-pressure steam channel which is communicated with the second evaporator (9), and the second evaporator (9) is also provided with a low-pressure steam ) Communicating; the high-temperature heat exchanger (6) is also provided with a heat source medium channel communicated with the outside, the condenser (7) is also provided with a cooling medium channel communicated with the outside, the evaporator (8) or the heat source medium channel is also communicated with the outside, the second evaporator (9) is also provided with a heat source medium channel communicated with the outside, and the expander (1) is connected with the compressor (2) and transmits power to form a combined cycle power device; wherein, or the expander (1) is connected with the compressor (2), the circulating pump (4) and the second circulating pump (5) and transmits power.
11. A combined cycle power device is characterized in that a low-temperature heat regenerator and a third circulating pump are added in any combined cycle power device of claims 1 to 10, a condenser (7) is provided with a condensate pipeline which is communicated with an evaporator (8) through the circulating pump (4) and is adjusted to be that the condenser (7) is provided with a condensate pipeline which is communicated with a low-temperature heat regenerator (12) through the circulating pump (4), a middle steam extraction channel is additionally arranged on a compressor (2) and is communicated with the low-temperature heat regenerator (12), and the low-temperature heat regenerator (12) is provided with a condensate pipeline which is communicated with the evaporator (8) through the third circulating pump (13) to form the combined cycle power device.
12. A combined cycle power device is characterized in that in any combined cycle power device of claims 1-11, a newly added heat regenerator and a newly added circulating pump are added, a condenser (7) is communicated with a second evaporator (9) through a second circulating pump (5) and adjusted to be a condenser (7) which is communicated with a newly added heat regenerator (A) through a second circulating pump (5), a middle steam extraction channel is additionally arranged on a compressor (2) and communicated with the newly added heat regenerator (A), and the newly added heat regenerator (A) is communicated with the second evaporator (9) through a newly added circulating pump (B) through a condensed liquid pipeline to form the combined cycle power device.
CN202010433103.2A 2019-05-19 2020-05-16 Combined cycle power plant Pending CN111852586A (en)

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CN201910455467 2019-05-19

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022141611A1 (en) * 2021-01-03 2022-07-07 李华玉 Dual-fuel combined cycle steam power device
WO2022141610A1 (en) * 2021-01-03 2022-07-07 李华玉 Dual-fuel combined circulating steam power device
WO2022161112A1 (en) * 2021-01-27 2022-08-04 李华玉 Dual-fuel combined cycle steam power device
WO2022166504A1 (en) * 2021-02-07 2022-08-11 李华玉 Dual-fuel combined cycle steam power plant

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2022141611A1 (en) * 2021-01-03 2022-07-07 李华玉 Dual-fuel combined cycle steam power device
WO2022141610A1 (en) * 2021-01-03 2022-07-07 李华玉 Dual-fuel combined circulating steam power device
WO2022161112A1 (en) * 2021-01-27 2022-08-04 李华玉 Dual-fuel combined cycle steam power device
WO2022166504A1 (en) * 2021-02-07 2022-08-11 李华玉 Dual-fuel combined cycle steam power plant

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