The effects of real gas and turbulence have a great influence on the performance of supercritical carbon dioxide (S-CO₂) dry gas seal. A typical spiral groove dry gas seal calculation model is established, and the flow equation on the end face of supercritical carbon dioxide dry gas seal is solved by CFD software to obtain the flow state of fluid between the seal slots. The influence of real gas and turbulence effects on opening force and leakage are investigated under different rotational speed. The results show that both real gas and turbulence effects make the pressure distribution of the gas film change significantly. The real gas effect improves the opening force and leakage of gas film, and the strengthening effect on the opening force becomes stronger with the increase of the rotational speed, while the effect on the leakage almost does not change with the rotational speed. At low rotational speed, the turbulence effect has a weak effect on the opening force. With the increase of rotational speed, the opening force increases sharply due to the turbulence effect, and the increase increases with the increase of rotational speed. In the high speed S-CO₂ dry gas seal, the combined effect of real gas and turbulence effect makes the opening force of gas film increase significantly, and the turbulence effect is greater than the real gas effect.

To ensure the safe and reliable operation of supercritical carbon dioxide (S-CO₂) power plant over a long period of time, referred to the material commonly used in traditional steam boiler, the material of S-CO₂ boiler is selected fromhigh temperature strength and corrosion characteristics. When CO₂ flows through the boiler, the temperature of CO₂ is high, the temperature difference between CO₂ and tube wall temperature is large, over the 30~50 ℃ of steam boiler. Then the grade of the heat-resistant steel has to be upgraded. However, requirements and methods for the material selection for steam boiler cannot be directly used for S-CO₂ boiler. The feasibility of heat-resistant steels such as T23, T91,T92, TP347HFG and Super304H used in S-CO₂ boilers is explored from using maturity and economic performance. The results show that for cooling wall, T91 could be selected at certain tube structure, but 12Cr1MoVG, T21 and T23 et al used in steam boiler could not be selected. For superheater, only austenitic steel TP347HFG and Super304H meet the material selection requirements at certain tube structure.

Combing the excellent performance of carbon dioxide thermodynamic cycle and the reutilization demands for the captured carbon dioxide, the energy storagetechnologies based on carbon dioxide thermodynamic cycle have the potential to play an important role in the future energy system which mainly consists of renewable energies. This paper presents the definition of the energy storage technology based on carbon dioxide thermodynamic cycle, and then classifies this energy storage technology into six types, which are electrothermal energy storage, compressing carbon dioxide energy storage with low, mid and highpressure gas storage, compressing carbon dioxide energy storage with low-temperature and near atmospheric temperature liquid storage, and the constant pressure gas storage energy storage. The state-of-the-art research status, advantages and disadvantages of these technologies are discussed. In general, the compressing carbon dioxide energy storage with low pressure gas storage is most mature, and there are demonstration units constructed. The compressing carbon dioxide energy storage with high pressure gas storageand the electrothermal energy storage have a good overall performance, but their costs are high. The compressing carbon dioxide energy storage with constant pressure gas storage has the highest cycle efficiency, reaching 74%~75%, and the energy storage density is up to 2 (kW·h)/m³, making it one of the most promising compressing gas energy storage technologies.

Based on the first and second laws of thermodynamics, parameters of the supercritical carbon dioxide (S-CO₂) recompression cycle, recompression reheat cycle, partial cooling cycle, partial cooling reheat cycle coal-fired power generation system were calculated and analyzed by using MATLAB software. Then, the impact of shunt coefficient, outlet and inlet pressure of the main compressor on the system circulation efficiency, equipment and exergy efficiency of the system were discussed respectively, and the four types of circulation systems were compared and analyzed. The results show that the cycle efficiency varies with the same parameters under different cycle layout or the same cycle layout and different operating parameters. There is a shunt coefficient for exergy efficiency and exergy efficiency to reach an optimal value. There is a coupling relationship between the influence of outlet and inlet pressure of the main compressor and the shunt coefficient on the circulation efficiency. For different parameter changes, exergy efficiency of system is mainly affected by exergy efficiency of different equipment. Reheat can increase circulation efficiency and exergy efficiency of the system, while some cooling cycles are relatively less sensitive to parameter changes.

The combination of supercritical carbon dioxide Brayton cycle and lead cooled fast reactor is considered as one of the most ideal power cycles. The system transfers heat through the intermediate heat exchanger, and its performance affects the efficient and safe operation of the whole power generation system. Due to the significant differences in physical properties and heat mass transport properties between supercritical carbon dioxide and liquid lead bismuth eutectic, the symmetrical structure cannot match the heat transfer requirements of the working fluids on both sides. In this study, an asymmetric compact coupled heat exchanger was constructed, and the coupled heat transfer characteristics of supercritical carbon dioxide and liquid lead bismuth eutectic were studied by numerical simulation. Increasing the inlet velocity of the cold side fluid will significantly enhance the heat transfer; When the inlet velocity of LBE at the hot side is increased, the total heat transfer coefficient first decreases and then increases; When the inlet temperature of the cold and hot fluid of the heat exchanger is increased, the heat transfer coefficient of the heat exchanger first decreases and then increases, and there is an optimal value; Due to the high proportion of thermal resistance in the cold side, the similarities and differences of heat transfer characteristics of cold side supercritical carbon dioxide under buoyancy and thermal acceleration under different operating parameters are compared; It is found that in the quasi critical region, the strong buoyancy will greatly enhance the cold side heat transfer, while the acceleration effect will inhibit the heat transfer.

Liquid metal fast reactor/concentration solar power system coupled with supercritical carbon dioxide (S-CO₂) Brayton cycle power system will surely lead the revolutionary development in the field of energy and power in future. Due to the special properties of liquid metal and S-CO₂, the Pr number of liquid metals is low; the physical properties of S-CO₂ steep varies in the pesudocrtical region, thus its flow and heat transfer characteristics are different from those of conventional fluids, their heat transfer mechanism is relatively complex, and the conjugated heat transfer mechanism is not clear. This study summarizes the main research results of supercritical CO₂, liquid metal, conjugated heat transfer and conjugated heat exchanger at home and abroad in experiments, numerical simulation and prediction models, points out the problems in the research of CO₂, liquid metals and their conjugating heat transfer between the two fluids, the discussion can provide valuable reference for the design and safe operation of advanced power cycle and multiple working fluids coupling power systems.

The supercritical carbon dioxide cycle has many advantages, such as high cycle efficiency, small equipment size, convenient transportation and installation, and easy to reach the critical point. Considering the huge cold energy of LNG, it can not only be used as coolant in the combined cycle system, but also the natural gas after heat transfer can be used as fuel input in the combined cycle, and the rest can be supplied to urban users. A gas turbine/supercritical carbon dioxide combined cycle system based on the utilization of LNG cold energy is proposed in this paper. Select the appropriate cost formula to calculate and analyze the investment cost, operating income and recovery cycle of the circulating power generation system in detail. The influence of some key parameters (such as maximum temperature, maximum pressure, minimum temperature, minimum pressure and shunt ratio) on the power generation characteristics and economy of the supercritical carbon dioxide cycle in the combined cycle system was studied. The results show that with the increase of each single parameter, the cost of equipment investment will first increase and then decrease, but the effect of power generation on income is dominant. Taking the yield as the measurement standard, the higher the maximum temperature, the better, the lower the minimum temperature, the better. Under other parameters, there are optimal values to maximize the yield.The key parameters were optimized by genetic algorithm to maximize the cumulative income. After optimization, the recovery cycle was 5.86 years, and the cumulative income (20 years) was 2.287 billion yuan.

Aiming at the problem of waste heat utilization of gas turbine, the technologies of intermediate cooling, intermediate reheating and split flow recompression were introduced into the supercritical carbon dioxide (S-CO₂) power cycle with heat recovery and six cycle schemes were established. Taking the cycle efficiency and the cycle net output power of the S-CO₂ cycle as the optimization objectives, the genetic algorithm was used to optimize the parameters of each scheme, and the earnings of optimization results were compared. The results show that the cycle efficiency can be improved in varying degrees by introducing one intermediate cooling, one intermediate reheat and one split flow recompression when the optimization goal is to maximize the cycle efficiency. The cycle efficiency of the sixth scheme that introduces one split flow recompression and one intermediate reheat is the highest, which reaches 43.29%. When the optimization goal is to maximize the net cycle output work, the introduction of primary intermediate cooling can increase the net output power, the introduction of primary intermediate reheating can reduce the net output power of the power cycle, and the one split recompression degenerates into no split scheme. The second scheme that introduces primary intermediate cooling has the largest net output power reaching 82 620.02 kW. When the cycle net output work is taken as the optimization objective, the economy of the six schemes is more advantageous because the waste heat utilization efficiency of gas turbine smoke exhaust is higher. The second scheme has the largest operating earnings in 20 years, which is RMB 5.065 billion.

In view of the deviation between the actual heat transfer performance and the theory of printed circuit plate heat exchanger due to processing errors and deformation during service, the shape characteristics of the actual micro-channel were measured and obtained by using ultra-depth of field microscope technology. The micro-channel heat transfer with different channel shapes was numerically simulated, and the influence of channel shape on thermal performance was analyzed. According to the results of numerical simulation, a new heat transfer characteristic correlation formula was obtained, which can provide a theoretical basis for evaluating the heat transfer performance of the actual service of supercritical carbon dioxide printed circuit plate heat exchangers.

A cooling system was designed for a supercritical carbon dioxide (S-CO₂) axial turbine. The dry gas seal, shaft and casing were cooled by extracting the low temperature S-CO₂ in the pipeline behind the compressor to ensure that the dry gas seal operating temperature was below 200 ℃. The flow and heat transfer characteristics of the cooling system were analyzed using the coupled heat transfer method, and the temperature distributions of solid domains such dry gas seal, shaft and casing of different cooling schemes were compared. The research shows that the temperature drop of the shaft reaches 220.3 ℃ when the_shaft cooling scheme is adopted, and the maximum temperature of the dry gas seal is 229.1 ℃. Further introduction of S-CO₂ with lower temperature and larger flow rate to cool the casing can inhibit the heating effect of the high temperature mainstream at the turbine inlet. The temperature drop of the shaft increases to 244.1 ℃, and the maximum temperature of the dry gas seal decreases to 181.2 ℃. Meanwhile, the reasonable temperature gradient of the cooled domains such as the dry gas seal, shaft and casing is achieved. The cooling system designed in this paper provides a solution for the safe and reliable operation of S-CO₂ axial turbines.