Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model

The working fluids are crucial for developing the absorption refrigeration system. Our previous work has proposed three novel working pairs, which uses the low-GWP HFCs (R32, R152a and R161) as the refrigerants and the polyethylene-glycol dimethylether solvent DMETEG as the absorbent. To explore the...

Full description

Bibliographic Details
Main Authors: Zhang Xiao, Cai Liang, Qiao Jingyi
Format: Article
Language:English
Published: EDP Sciences 2021-01-01
Series:E3S Web of Conferences
Online Access:https://www.e3s-conferences.org/articles/e3sconf/pdf/2021/43/e3sconf_icsce2021_02052.pdf
id doaj-2ac0118c641a4844aaa244762853b79a
record_format Article
spelling doaj-2ac0118c641a4844aaa244762853b79a2021-06-11T07:21:12ZengEDP SciencesE3S Web of Conferences2267-12422021-01-012670205210.1051/e3sconf/202126702052e3sconf_icsce2021_02052Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC modelZhang Xiao0Cai Liang1Qiao Jingyi2School of Energy and Environment, Southeast UniversitySchool of Energy and Environment, Southeast UniversitySchool of Energy and Environment, Southeast UniversityThe working fluids are crucial for developing the absorption refrigeration system. Our previous work has proposed three novel working pairs, which uses the low-GWP HFCs (R32, R152a and R161) as the refrigerants and the polyethylene-glycol dimethylether solvent DMETEG as the absorbent. To explore the VLE behaviors of HFCs in other longer chain structures of polyethylene-glycol dimethylether solvents, the modified UNIFAC (Dortmund) model was applied for prediction. The previous binary parameters showed large deviations from the experimental data. Then the new binary parameters were obtained by regression. For R32+DMEDEG and R152a/R161+DMETrEG, the prediction ARAD results were reduced from 17.13%, 24.06% and 12.48% to 3.71%, 2.61% and 6.86%, respectively. Finally, the VLE data of R161 + PGDE at the temperatures of 293.15-343.15K were predicted.https://www.e3s-conferences.org/articles/e3sconf/pdf/2021/43/e3sconf_icsce2021_02052.pdf
collection DOAJ
language English
format Article
sources DOAJ
author Zhang Xiao
Cai Liang
Qiao Jingyi
spellingShingle Zhang Xiao
Cai Liang
Qiao Jingyi
Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
E3S Web of Conferences
author_facet Zhang Xiao
Cai Liang
Qiao Jingyi
author_sort Zhang Xiao
title Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
title_short Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
title_full Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
title_fullStr Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
title_full_unstemmed Predictions of the vapor-liquid equilibrium data for low-GWP Hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified UNIFAC model
title_sort predictions of the vapor-liquid equilibrium data for low-gwp hydrofluorocarbons + polyethylene-glycol dimethylether solvents by modified unifac model
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2021-01-01
description The working fluids are crucial for developing the absorption refrigeration system. Our previous work has proposed three novel working pairs, which uses the low-GWP HFCs (R32, R152a and R161) as the refrigerants and the polyethylene-glycol dimethylether solvent DMETEG as the absorbent. To explore the VLE behaviors of HFCs in other longer chain structures of polyethylene-glycol dimethylether solvents, the modified UNIFAC (Dortmund) model was applied for prediction. The previous binary parameters showed large deviations from the experimental data. Then the new binary parameters were obtained by regression. For R32+DMEDEG and R152a/R161+DMETrEG, the prediction ARAD results were reduced from 17.13%, 24.06% and 12.48% to 3.71%, 2.61% and 6.86%, respectively. Finally, the VLE data of R161 + PGDE at the temperatures of 293.15-343.15K were predicted.
url https://www.e3s-conferences.org/articles/e3sconf/pdf/2021/43/e3sconf_icsce2021_02052.pdf
work_keys_str_mv AT zhangxiao predictionsofthevaporliquidequilibriumdataforlowgwphydrofluorocarbonspolyethyleneglycoldimethylethersolventsbymodifiedunifacmodel
AT cailiang predictionsofthevaporliquidequilibriumdataforlowgwphydrofluorocarbonspolyethyleneglycoldimethylethersolventsbymodifiedunifacmodel
AT qiaojingyi predictionsofthevaporliquidequilibriumdataforlowgwphydrofluorocarbonspolyethyleneglycoldimethylethersolventsbymodifiedunifacmodel
_version_ 1721382864982900736