2021
DOI: 10.1016/j.enconman.2021.114029
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CFD aided design and analysis of a precooler with zigzag channels for supercritical CO2 power cycle

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Cited by 62 publications
(17 citation statements)
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“…Likewise, the value of the š‘Ÿ increase with the surge in the value of for all values of , but the increase is tinier in comparison with the boost linked with . Despite the above discussion, it is to be noted here for sCO 2 -BC that the size of the heat exchanger is much larger than its turbomachinery [4,39,40]. Therefore, the layout size of sCO 2 -BC is dominated by PCHEs and marginally affected by the size of its turbomachinery.…”
Section: Instancesmentioning
confidence: 77%
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“…Likewise, the value of the š‘Ÿ increase with the surge in the value of for all values of , but the increase is tinier in comparison with the boost linked with . Despite the above discussion, it is to be noted here for sCO 2 -BC that the size of the heat exchanger is much larger than its turbomachinery [4,39,40]. Therefore, the layout size of sCO 2 -BC is dominated by PCHEs and marginally affected by the size of its turbomachinery.…”
Section: Instancesmentioning
confidence: 77%
“…Apart from its higher efficiency, the sCO 2 -BC is favorable when environmental factors, such as global warming potential (GWP) and climate change, and economic factors are taken into consideration. Furthermore, (sCO 2 ) Brayton cycle has a simpler and compact cycle layout with no requirement of the condenser and almost ten-times smaller turbomachinery in comparison to the Rankine cycle [4]. The critical temperature (T c = 31.1 0 ) of CO 2 is nearly ambient that allows its pairing with a wide range of heat sources.…”
Section: Introductionmentioning
confidence: 99%
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“…Various models like Langmuir, Freundlich, Elovich, Temkin, Fowler-Guggenheim, and Kiselev have been reported to be used. [162][163][164] RPB has also been reported to be highly effective for the polymerization of monomers to polymers, like isobutylene to highly reactive polyisobutylene. This process is known as cationic polymerization.…”
Section: Rpb Technology For the Other Applicationsmentioning
confidence: 99%
“…Consequently, the k āˆ’ turbulence model is not appropriate for flows with the boundary layer separation, flows with sudden changes in the mean streamflow, flows in revolving fluids, and flows over curved surfaces. On the other hand, the shear stress turbulence (SST) model combines two models [19][20][21][22][23][24][25], i.e., k āˆ’ Ļ‰ and k āˆ’ turbulence models according to the distance from the wall. Wilcox k āˆ’ Ļ‰ is utilized to resolve the flow in the vicinity of the walls for accurate prognostication of the boundary layer, whereas the k āˆ’ turbulence model is solving the flow in fully developed regions to gain advantage from its robustness, economy, and free stream independence [13,19].…”
Section: Computational Model 21 Governing Equationsmentioning
confidence: 99%