1. Experimental investigation and thermodynamic modeling of adsorption equilibria of MSC30 with R32 for supercritical adsorption cooling systems.
- Author
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Yang, Zhaosheng, Sultan, Muhammad, Thu, Kyaw, and Miyazaki, Takahiko
- Subjects
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COOLING systems , *HEAT pumps , *ADSORPTION (Chemistry) , *ACTIVATED carbon , *SUPERCRITICAL carbon dioxide , *WORKING fluids - Abstract
• Experimental measurements of the adsorption characteristics of MSC30+R32 over a wide temperature range. • Development of an improved adsorption potential model for predicting isotherm data of various adsorbent-adsorbate pairs under supercritical conditions. • Validation of the proposed models using experimental data and comparison with traditional empirical equations. • Evaluation of the performance of an adsorption heat pump utilizing MSC30/R32 as the working fluid under supercritical conditions, with insights into the underlying mechanisms. In the present study, the adsorption isotherms of difluoromethane (R32) on the activated carbon (MSC 30) throughout a temperature range of 25 °C to 150 °C and pressures up to 3000 kPa are measured for possible application in adsorption cooling systems. The Dubinin-Astakhov model was used to fit the experimental data. A thermodynamic model is proposed in this study to investigate the adsorption potential under supercritical conditions. The model is validated using the isotherm data from the experiments and literatures for different working pairs. The validation results exhibited a good agreement between the proposed model and the experimental data, signifying the precision and dependability of the model. The corresponding adsorption isosteric heat model was derived and verified, taking into account both the inclusion and exclusion of the adsorbed volume correction. Furthermore, the developed models were utilized in the equilibrium analysis of an adsorption heat pump to evaluate the performance of the system in terms of the theoretical coefficient of performance (COP) and specific cooling energy (SCE). The analysis covered the driving heat source temperature ranging from 30 °C to 150 °C, with different evaporation temperatures and adsorption temperatures. The results showed that the maximum COP value of 0.47 for the adsorption heat pump system employing the MSC30+R32 pair was achieved at a desorption temperature of 115 °C, at which the SCE was 315.5 kJ·kg−1. The results can potentially improve the accuracy of predicting adsorption behavior and contribute to the development of more efficient and effective adsorption systems. [ABSTRACT FROM AUTHOR]
- Published
- 2024
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