Supercritical carbon dioxide Rankine cycle system and combined cycle system
阅读说明:本技术 一种超临界二氧化碳朗肯循环系统及联合循环系统 (Supercritical carbon dioxide Rankine cycle system and combined cycle system ) 是由 陈宜 徐东杰 陈铮 徐小东 于 2018-08-13 设计创作,主要内容包括:本发明提供一种超临界二氧化碳朗肯循环系统及联合循环系统,该超临界二氧化碳朗肯循环系统包括:第一加热器;第二加热器,第二加热器的烟气入口与第一加热器的烟气出口连通,第二加热器的工质出口与第一加热器的工质入口连通;回热器,回热器的冷流体出口和第一加热器的工质入口连通,回热器的热流体出口与冷却系统的入口连接;二氧化碳循环泵,二氧化碳循环泵的工质出口分别与回热器的冷流体入口及第二加热器的工质入口连通;二氧化碳透平,二氧化碳透平的入口与第一加热器的工质出口连通,二氧化碳透平的出口与回热器的热流体入口连通;与所二氧化碳透平连接的第一发电机;以及冷凝器。这样,可以使联合循环系统的结构比较简单和紧凑。(The invention provides a supercritical carbon dioxide Rankine cycle system and a combined cycle system, wherein the supercritical carbon dioxide Rankine cycle system comprises: a first heater; the flue gas inlet of the second heater is communicated with the flue gas outlet of the first heater, and the working medium outlet of the second heater is communicated with the working medium inlet of the first heater; a cold fluid outlet of the heat regenerator is communicated with a working medium inlet of the first heater, and a hot fluid outlet of the heat regenerator is connected with an inlet of the cooling system; a working medium outlet of the carbon dioxide circulating pump is respectively communicated with a cold fluid inlet of the heat regenerator and a working medium inlet of the second heater; an inlet of the carbon dioxide turbine is communicated with a working medium outlet of the first heater, and an outlet of the carbon dioxide turbine is communicated with a hot fluid inlet of the heat regenerator; a first generator coupled to the carbon dioxide turbine; and a condenser. In this way, the combined cycle system can be made relatively simple and compact in construction.)
1. A supercritical carbon dioxide Rankine cycle system, characterized by comprising:
a first heater;
the flue gas inlet of the second heater is communicated with the flue gas outlet of the first heater, and the working medium outlet of the second heater is communicated with the working medium inlet of the first heater;
the cold fluid outlet of the heat regenerator is communicated with the working medium inlet of the first heater;
a working medium outlet of the carbon dioxide circulating pump is respectively communicated with a cold fluid inlet of the heat regenerator and a working medium inlet of the second heater;
an inlet of the carbon dioxide turbine is communicated with a working medium outlet of the first heater, and an outlet of the carbon dioxide turbine is communicated with a hot fluid inlet of the heat regenerator;
a first generator coupled to the carbon dioxide turbine;
and a working medium inlet of the condenser is communicated with a hot fluid outlet of the heat regenerator, and a working medium outlet of the condenser is communicated with a working medium inlet of the carbon dioxide circulating pump.
2. The supercritical carbon dioxide rankine cycle system of claim 1, further comprising:
a solar reflector;
and the heat absorption pipe is arranged on the solar reflector, the inlet of the heat absorption pipe is communicated with the outlet of the carbon dioxide circulating pump, and the outlet of the heat absorption pipe is communicated with the working medium inlet of the first heater.
3. The supercritical carbon dioxide rankine cycle system of claim 1, further comprising:
the inlet of the seawater circulating pump is communicated with the ocean, and the outlet of the seawater circulating pump is communicated with the seawater inlet of the condenser;
wherein, the seawater outlet of the condenser is communicated with the ocean.
4. A combined cycle system, comprising:
the gas turbine circulating system comprises a compressor, a combustion chamber, a gas turbine and a second generator, wherein the combustion chamber is respectively communicated with the compressor and the gas turbine, and the gas turbine is respectively connected with the compressor and the second generator;
and a flue gas inlet of the supercritical carbon dioxide Rankine cycle system is communicated with an outlet of the gas turbine.
5. The combined cycle system of claim 4, wherein the supercritical carbon dioxide rankine cycle system comprises:
a flue gas inlet of the first heater is communicated with an outlet of the gas turbine, and the flue gas inlet of the first heater is a flue gas inlet of the supercritical carbon dioxide Rankine cycle system;
the flue gas inlet of the second heater is communicated with the flue gas outlet of the first heater, and the working medium outlet of the second heater is communicated with the working medium inlet of the first heater;
the cold fluid outlet of the heat regenerator is communicated with the working medium inlet of the first heater;
a working medium outlet of the carbon dioxide circulating pump is respectively communicated with a cold fluid inlet of the heat regenerator and a working medium inlet of the second heater;
an inlet of the carbon dioxide turbine is communicated with a working medium outlet of the first heater, and an outlet of the carbon dioxide turbine is communicated with a hot fluid inlet of the heat regenerator;
a first generator coupled to the carbon dioxide turbine;
and a working medium inlet of the condenser is communicated with a hot fluid outlet of the heat regenerator, and a working medium outlet of the condenser is communicated with a working medium inlet of the carbon dioxide circulating pump.
6. The combined cycle system of claim 5, wherein the supercritical carbon dioxide rankine cycle system further comprises:
a solar reflector;
and the heat absorption pipe is arranged on the solar reflector, the inlet of the heat absorption pipe is communicated with the outlet of the carbon dioxide circulating pump, and the outlet of the heat absorption pipe is communicated with the working medium inlet of the first heater.
7. The combined cycle system of claim 6, wherein the solar reflector is a parabolic trough reflector or a linear Fresnel reflector.
8. The combined cycle system of claim 5, wherein the supercritical carbon dioxide rankine cycle system further comprises:
the inlet of the seawater circulating pump is communicated with the ocean, and the outlet of the seawater circulating pump is communicated with the seawater inlet of the condenser;
wherein, the seawater outlet of the condenser is communicated with the ocean.
Technical Field
The invention relates to the technical field of power generation, in particular to a supercritical carbon dioxide Rankine cycle system and a combined cycle system.
Background
With the continuous development of power generation technology, the combined cycle technology is greatly popularized and applied. The combined cycle is a combined working system consisting of thermodynamic cycle systems with different working media, and when the combined cycle is used for generating power, the waste gas generated by the previous stage is used for driving the next stage of heat engine to push the generator, so that the efficiency of fuel can be greatly improved, and the generated energy is improved. Generally, the existing combined cycle system mainly consists of a gas turbine system and a steam Rankine cycle system; however, the combined cycle using such a structure is relatively large and complex.
Disclosure of Invention
The embodiment of the invention aims to provide a supercritical carbon dioxide Rankine cycle system and a combined cycle system, and solves the problems that an existing combined cycle system is large in structure and complex.
To achieve the above object, an embodiment of the present invention provides a supercritical carbon dioxide rankine cycle system, including:
a first heater;
the flue gas inlet of the second heater is communicated with the flue gas outlet of the first heater, and the working medium outlet of the second heater is communicated with the working medium inlet of the first heater;
the cold fluid outlet of the heat regenerator is communicated with the working medium inlet of the first heater;
a working medium outlet of the carbon dioxide circulating pump is respectively communicated with a cold fluid inlet of the heat regenerator and a working medium inlet of the second heater;
an inlet of the carbon dioxide turbine is communicated with a working medium outlet of the first heater, and an outlet of the carbon dioxide turbine is communicated with a hot fluid inlet of the heat regenerator;
a first generator coupled to the carbon dioxide turbine;
and a working medium inlet of the condenser is communicated with a hot fluid outlet of the heat regenerator, and a working medium outlet of the condenser is communicated with a working medium inlet of the carbon dioxide circulating pump.
Optionally, the supercritical carbon dioxide rankine cycle system further includes:
a solar reflector;
and the heat absorption pipe is arranged on the solar reflector, the inlet of the heat absorption pipe is communicated with the outlet of the carbon dioxide circulating pump, and the outlet of the heat absorption pipe is communicated with the working medium inlet of the first heater.
Optionally, the supercritical carbon dioxide rankine cycle system further includes:
the inlet of the seawater circulating pump is communicated with the ocean, and the outlet of the seawater circulating pump is communicated with the seawater inlet of the condenser;
wherein, the seawater outlet of the condenser is communicated with the ocean.
An embodiment of the present invention further provides a combined cycle system, including:
the gas turbine circulating system comprises a compressor, a combustion chamber, a gas turbine and a second generator, wherein the combustion chamber is respectively communicated with the compressor and the gas turbine, and the gas turbine is respectively connected with the compressor and the second generator;
and a flue gas inlet of the supercritical carbon dioxide Rankine cycle system is communicated with an outlet of the gas turbine.
Optionally, the supercritical carbon dioxide rankine cycle system includes:
a flue gas inlet of the first heater is communicated with an outlet of the gas turbine, and the flue gas inlet of the first heater is a flue gas inlet of the supercritical carbon dioxide Rankine cycle system;
the flue gas inlet of the second heater is communicated with the flue gas outlet of the first heater, and the working medium outlet of the second heater is communicated with the working medium inlet of the first heater;
the cold fluid outlet of the heat regenerator is communicated with the working medium inlet of the first heater;
a working medium outlet of the carbon dioxide circulating pump is respectively communicated with a cold fluid inlet of the heat regenerator and a working medium inlet of the second heater;
an inlet of the carbon dioxide turbine is communicated with a working medium outlet of the first heater, and an outlet of the carbon dioxide turbine is communicated with a hot fluid inlet of the heat regenerator;
a first generator coupled to the carbon dioxide turbine;
and a working medium inlet of the condenser is communicated with a hot fluid outlet of the heat regenerator, and a working medium outlet of the condenser is communicated with a working medium inlet of the carbon dioxide circulating pump.
Optionally, the supercritical carbon dioxide rankine cycle system further includes:
a solar reflector;
and the heat absorption pipe is arranged on the solar reflector, the inlet of the heat absorption pipe is communicated with the outlet of the carbon dioxide circulating pump, and the outlet of the heat absorption pipe is communicated with the working medium inlet of the first heater.
Optionally, the solar reflector is a parabolic trough reflector or a linear fresnel reflector.
Optionally, the supercritical carbon dioxide rankine cycle system further includes:
the inlet of the seawater circulating pump is communicated with the ocean, and the outlet of the seawater circulating pump is communicated with the seawater inlet of the condenser;
wherein, the seawater outlet of the condenser is communicated with the ocean.
One of the above technical solutions has the following advantages or beneficial effects:
according to the embodiment of the invention, the supercritical carbon dioxide Rankine cycle system and the gas turbine cycle system form the combined cycle system, and the supercritical carbon dioxide Rankine cycle system adopts supercritical carbon dioxide as a working medium, so that the combined cycle system is simpler and more compact in structure.
Drawings
Fig. 1 is a schematic structural diagram of a combined cycle system according to an embodiment of the present invention.
Detailed Description
In order to make the technical problems, technical solutions and advantages of the present invention more apparent, the following detailed description is given with reference to the accompanying drawings and specific embodiments.
As shown in fig. 1, an embodiment of the present invention provides a supercritical carbon dioxide
a
a flue gas inlet of the
a cold fluid outlet of the
a working medium outlet of the carbon
the inlet of the
a
and a working medium inlet of the
In this embodiment, the
In addition, the supercritical carbon
It should be noted that the rankine cycle system is a thermodynamic cycle system using water vapor as a working medium, and the thermodynamic cycle system can be used as a bottom cycle in a combined cycle system; the supercritical carbon dioxide
The working process of the supercritical carbon dioxide Rankine
Therefore, the working medium flow of the
Optionally, the supercritical carbon dioxide
a
and a
Wherein the
The
In this way, the supercritical carbon dioxide working medium pressurized by the carbon
Optionally, the supercritical carbon dioxide
a
wherein the seawater outlet of the
In the present embodiment, since the critical pressure and temperature of carbon dioxide are 7.38MPa and 31.1 ℃ respectively, and the condensation temperature of the supercritical carbon dioxide
Seawater can be pumped by the
In this embodiment, the working medium outlet of the carbon
As shown in fig. 1, an embodiment of the present invention further provides a combined cycle system, including:
a gas
a supercritical carbon dioxide
Wherein, in the combined cycle system, the gas
In this embodiment, the combined cycle system is formed by the supercritical carbon dioxide rankine cycle system and the gas turbine cycle system, and the supercritical carbon dioxide rankine cycle system uses supercritical carbon dioxide as a working medium, so that the combined cycle system has a relatively simple and compact structure.
Optionally, the supercritical carbon dioxide
a
a flue gas inlet of the
a cold fluid outlet of the
a working medium outlet of the carbon
the inlet of the
a
and a working medium inlet of the
The description of the supercritical carbon dioxide
Thus, by respectively communicating the working medium outlet of the carbon
Optionally, the supercritical carbon dioxide
a
and a
The description of the
In this way, the supercritical carbon dioxide working medium pressurized by the carbon
Optionally, the
Optionally, the supercritical carbon dioxide
a
wherein the seawater outlet of the
In this embodiment, the description of the
Therefore, the seawater can be used as the low-temperature cold source of the supercritical carbon dioxide by the
While the foregoing is directed to the preferred embodiment of the present invention, it will be understood by those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the invention as defined in the appended claims.
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