Adsorption kinetics of difluoromethane on biomass-derived activated carbon through experimental and modeling approaches

• High-precision TGA provides MAC/R32 kinetics over 30–90°C and pressures of 0–3000 kPa. • Dual-PFO fits all uptake curves with high accuracy (average R² = 0.9976). • Global P–T correlations are established for α , k 1 , and k 2 in the dual-PFO model. • Fast branch links to mesopores; slow branch reflects micropore-controlled transport. • Embedded dual-PFO kinetics in a two-bed ACS model to predict COP and CP. This study investigated the adsorption kinetics of difluoromethane (R32) on mangrove-derived activated carbon (MAC) over 30–90°C and 0–3000 kPa using a thermogravimetric (TGA) setup. To capture the transient uptake and investigate the equilibrium pressure effects on adsorption kinetics, a dual pseudo-first-order (dual-PFO) model was adopted, in which total uptake is expressed as the sum of two branches with distinct rate constants ( k 1 , k 2 ); their contributions to total uptake are characterized by the fractional capacity α . The model fitted all the experiments with high accuracy (average R 2 = 0.9976). Parameter analysis showed that α and k 1 decrease as the equilibrium pressure increases, whereas k 2 is nearly pressure-invariant. Applying the dual-PFO model to literature datasets (Maxsorb III/R32 and MAC/CO 2 ), α , k 1 and k 2 exhibited the same pressure dependence trend as MAC/R32. Comparison of fitted parameters across three working pairs together with pore-structure differences between MAC and Maxsorb III indicates a mesopore-associated fast branch and a micropore-controlled slow branch. Parameters ( α , k 1 , k 2 ) were regressed as functions of pressure and temperature, yielding a global correlation formula that reproduces representative curves with high accuracy. Embedding the correlation in a dynamic two-bed R32/MAC adsorption cooling model yielded a coefficient of performance (COP) of 0.173 and a cooling power (CP) of 1.47 kW under representative conditions ( T evap = 10°C, T cond = 30°C, T des = 75°C), suggesting that MAC/R32 is a promising working pair and that the dual-PFO kinetics can facilitate system-level performance evaluation under the examined conditions.

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Publication Details

Journal
International Journal of Heat and Mass Transfer
Published
2026-02-04
DOI
https://doi.org/10.1016/j.ijheatmasstransfer.2026.128471
Primary Topic
Carbon Dioxide Capture Technologies
Type
article
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article

Adsorption kinetics of difluoromethane on biomass-derived activated carbon through experimental and modeling approaches

Bidyut Baran Saha, Yuetuo Lu, Md. Amirul Islam, Huiyuan Bao et al.
International Journal of Heat and Mass Transfer
Carbon Dioxide Capture Technologies
article

Adsorption kinetics of difluoromethane on biomass-derived activated carbon through experimental and modeling approaches

Bidyut Baran Saha, Yuetuo Lu, Md. Amirul Islam, Huiyuan Bao, Sixu Zhang
article en

Abstract

• High-precision TGA provides MAC/R32 kinetics over 30–90°C and pressures of 0–3000 kPa. • Dual-PFO fits all uptake curves with high accuracy (average R² = 0.9976). • Global P–T correlations are established for α , k 1 , and k 2 in the dual-PFO model. • Fast branch links to mesopores; slow branch reflects micropore-controlled transport. • Embedded dual-PFO kinetics in a two-bed ACS model to predict COP and CP. This study investigated the adsorption kinetics of difluoromethane (R32) on mangrove-derived activated carbon (MAC) over 30–90°C and 0–3000 kPa using a thermogravimetric (TGA) setup. To capture the transient uptake and investigate the equilibrium pressure effects on adsorption kinetics, a dual pseudo-first-order (dual-PFO) model was adopted, in which total uptake is expressed as the sum of two branches with distinct rate constants ( k 1 , k 2 ); their contributions to total uptake are characterized by the fractional capacity α . The model fitted all the experiments with high accuracy (average R 2 = 0.9976). Parameter analysis showed that α and k 1 decrease as the equilibrium pressure increases, whereas k 2 is nearly pressure-invariant. Applying the dual-PFO model to literature datasets (Maxsorb III/R32 and MAC/CO 2 ), α , k 1 and k 2 exhibited the same pressure dependence trend as MAC/R32. Comparison of fitted parameters across three working pairs together with pore-structure differences between MAC and Maxsorb III indicates a mesopore-associated fast branch and a micropore-controlled slow branch. Parameters ( α , k 1 , k 2 ) were regressed as functions of pressure and temperature, yielding a global correlation formula that reproduces representative curves with high accuracy. Embedding the correlation in a dynamic two-bed R32/MAC adsorption cooling model yielded a coefficient of performance (COP) of 0.173 and a cooling power (CP) of 1.47 kW under representative conditions ( T evap = 10°C, T cond = 30°C, T des = 75°C), suggesting that MAC/R32 is a promising working pair and that the dual-PFO kinetics can facilitate system-level performance evaluation under the examined conditions.

International Journal of Heat and Mass TransferVol. 260
Kyushu University (JP)
Life below water
Openalex Percentile: Top 67%
Carbon Dioxide Capture Technologies
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