A supercritical carbon dioxide cogeneration system and operation method

A carbon dioxide, cogeneration technology, applied in joint combustion mitigation, steam engine installations, machines/engines, etc., can solve the problems of 50℃-140℃, difficult to match the heat release curve, difficult to use the exhausted steam, etc. The effect of reducing the temperature of the working fluid, reducing the heat exchange temperature difference at the hot end, and improving the energy utilization rate

Active Publication Date: 2022-04-05
XI AN JIAOTONG UNIV
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Problems solved by technology

[0005] At present, cogeneration units in northern my country mostly use high back pressure for heating or steam turbine extraction for heating, but in supercritical carbon dioxide systems, the exhaust steam pressure of the turbine is mostly below 10MPa. The heat is slow, and when it is lower than 60°C, the heat release curve is difficult to match, and it is easy to produce large irreversible losses. The waste heat required for heating is mostly between 50°C and 140°C. The heat supply of coal power generation system is different from the traditional high back pressure heating unit. Reasonable matching of energy levels and meeting the requirements of heating temperature and load are the problems that need to be solved in supercritical carbon dioxide power cycle.

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  • A supercritical carbon dioxide cogeneration system and operation method
  • A supercritical carbon dioxide cogeneration system and operation method
  • A supercritical carbon dioxide cogeneration system and operation method

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Embodiment Construction

[0029] The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.

[0030] working principle

[0031] The curve of enthalpy value and temperature change of carbon dioxide working medium under different pressures is as follows: figure 1 As shown, in the supercritical carbon dioxide system, the exhaust steam pressure of the turbine is mostly below 10MPa. At this time, when the temperature of the working fluid is higher than 60°C, the heat release is slow. Irreversible loss, most of the waste heat required for heating is between 50°C and 140°C, and it is difficult to utilize exhaust steam in this temperature range, so the heat supply of supercritical carbon dioxide coal-fired power generation system is different from that of traditional high back pressure heating units. When the carbon dioxide pressure is high, the heat release curve is linear and easy to match, so it is a relatively reasonable and simp...

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Abstract

The invention discloses a supercritical carbon dioxide cogeneration system and an operation method. The supercritical carbon dioxide cycle is adopted as the cogeneration power cycle, coupled with an air extraction heating system, and simultaneously provides users with two energy sources of heat and electricity; through the hot end Coupling optimization of -regeneration-heat supply process, the invention can greatly improve the energy utilization rate of the supercritical carbon dioxide power system. The system of the present invention performs reasonable energy level matching for air extraction, couples heat supply air extraction with the heat recovery system, reduces the irreversible loss of heat exchange in the system, and can meet different heat supply loads by adjusting the carbon dioxide split ratio of the heat recovery system Demand, improve the operating flexibility of the unit; also can make the system meet the heating temperature, increase the temperature of the working fluid entering the boiler, reduce the heat transfer temperature difference at the hot end, reduce irreversible losses, and improve the power generation efficiency of the unit.

Description

technical field [0001] The invention belongs to the field of cogeneration of heat and power, and in particular relates to a supercritical carbon dioxide cogeneration system and operation method. Background technique [0002] The stable growth of my country's economy is inseparable from the support of a strong energy system. my country's fossil energy structure is unbalanced, coal is the main body of my country's primary energy consumption, and coal-fired power generation is still the main power generation method in my country in a short period of time. As a large coal consumer in my country, thermal power units account for about 50% of the country's total coal consumption each year. [0003] my country's thermal power technology progress has shifted from improving initial parameters and steam reheating to full-working condition operation and deep utilization of waste heat. At the same time, central heating is carried out in the northern region to reduce pollutant emissions...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F01K25/10F01K7/32F01K17/06F01K7/38F01K13/02F01K17/02
CPCF01K25/103F01K7/32F01K17/06F01K7/345F01K7/38F01K13/02F01K17/02Y02E20/14
Inventor 刘明杨凯旋孙瑞强刘继平邢秦安严俊杰
Owner XI AN JIAOTONG UNIV
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