CO
2 transport is a crucial part of CCUS. Nonetheless, due to the physical property differences between CO
2 and natural gas and oil, CO
2 pipeline transport is distinct from natural gas and oil transport. Gaseous CO
2 transportation has become the preferred scheme for transporting impurity-containing CO
2 tail gas in purification plants due to its advantages of simple technology, low cost, and high safety, which are well suited to the scenarios of low transportation volume and short distance in purification plants. The research on its physical property and state parameters is precisely aimed at optimizing the process design of gaseous transportation so as to further improve transportation efficiency and safety. Therefore, it has important engineering practical significance. Firstly, this paper collected and analyzed the research cases of CO
2 transport both domestically and internationally, revealing that phase state and physical property testing of CO
2 gas containing impurities is the basic condition for studying CO
2 transport. Subsequently, the exhaust gas captured by the purification plant was captured after hydrodesulfurization treatment, and the characteristics of the exhaust gas components were obtained by comparing before and after treatment. By preparing fluid samples with varied CO
2 content and conducting the flash evaporation test and PV relationship test, the compression factor and density of natural gas under different temperatures and pressures were obtained. It is concluded that under the same pressure in general, the higher the CO
2 content, the smaller the compression factor. Except for pure CO
2, the higher the CO
2 content, the higher the density under constant pressure, which is related to the content of C
2 and heavier hydrocarbon components. At the same temperature, the higher the CO
2 content, the higher the viscosity under the same pressure; the lower the pressure, the slower the viscosity growth slows down. The higher the CO
2 content at the same temperature, the higher the specific heat at constant pressure. With the decrease in temperature, the CO
2 content reaching the highest specific heat at the identical pressure gradually decreases. Finally, BWRS, PR, and SRK equations of state were utilized to calculate the compression factor and density of the gas mixture with a molar composition of 50% CO
2 and the gas mixture with a molar composition of 100% CO
2. Compared with the experimental results, the most suitable equation of state is selected as the PR equation, which refers to the parameter setting of critical nodes of CO
2 gas transport.
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