2019
DOI: 10.1016/j.applthermaleng.2019.113786
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Heat transfer characteristics of carbon dioxide cross flow over tube bundles at supercritical pressures

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Cited by 17 publications
(3 citation statements)
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“…1, the corresponding Ma of primary-side hot helium is 0.039, so it can be treated as an incompressible viscous fluid with constant properties. Helium properties are calculated using the NIST real gas package which is a material database based on the Thermodynamic and Transport Properties of Refrigerants and Refrigerant Mixtures Database (REFPROP v9.1) provided by the National Institute of Standards and Technology (NIST) (Zhao et al, 2017;Gao et al, 2019). Table 2 lists the helium properties, where 5 significant digits are reserved.…”
Section: Physical Modelsmentioning
confidence: 99%
“…1, the corresponding Ma of primary-side hot helium is 0.039, so it can be treated as an incompressible viscous fluid with constant properties. Helium properties are calculated using the NIST real gas package which is a material database based on the Thermodynamic and Transport Properties of Refrigerants and Refrigerant Mixtures Database (REFPROP v9.1) provided by the National Institute of Standards and Technology (NIST) (Zhao et al, 2017;Gao et al, 2019). Table 2 lists the helium properties, where 5 significant digits are reserved.…”
Section: Physical Modelsmentioning
confidence: 99%
“…A cha is the area of hot airflow channel which is stacked by two bricks together, A cha = L × D × N, where N is the number of bricks in a row. Based on the Nusselt-Number N u , the heat transfer coefficient h conv can be calculated by the Zukauskas formula [24]. λ is the thermal conductivity.…”
Section: Thermal Convectionmentioning
confidence: 99%
“…In heat convection, multiple round holes can be approximately regarded as the tube bundle. The average heat transfer performance of the tube bundle is related to the flow Reynolds-number (R e ) [24].…”
Section: Thermal Convectionmentioning
confidence: 99%