Mass transfer approaches for CO2 separation in non-isothermal and non-adiabatic pressure swing adsorption system for biomethane upgrading

被引:14
作者
Abd, Ammar Ali [1 ,4 ]
Othman, Mohd Roslee [1 ,3 ]
Helwani, Zuchra [2 ]
机构
[1] Univ Sains Malaysia, Sch Chem Engn, Nibong Tebal 14300, Pulau Pinang, Malaysia
[2] Univ Riau, Dept Chem Engn, Pekanbaru 28293, Indonesia
[3] Ind Univ Ho Chi Minh City, Chem Engn Dept, 12 Nguyen Van Bao, Ho Chi Minh City, Vietnam
[4] Al Qasim Green Univ, Coll Engn, Babylon 51002, Iraq
关键词
Biogas upgrading; Mass transfer; Biomethane; Pressure swing adsorption; Carbon dioxide capture; FIXED-BED ADSORPTION; ACTIVATED CARBON; KINETIC SEPARATION; MOLECULAR-SIEVE; LANDFILL GAS; MIXTURES; BIOGAS; PURIFICATION; CAPTURE; METHANE;
D O I
10.1016/j.fuel.2022.125642
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The mass transfer of CO2 over solid materials can be quite complex. The complexity arises as a result of the adsorbent's complex surface morphology and dynamic process operating conditions. In this study, a new model was proposed to predict the mass transfer behavior of CO2 over silica gel in biogas upgrading process in which three mass transfer systems (lumped, micro-/macropore, and particle) were introduced. An overview for such mathematical models for CO2 mass transfer was conducted and then a new non-adiabatic and non-isothermal model for pressure swing adsorption (PSA) that is different from the existing models in the literature, i.e., adiabatic and isothermal models, was built and assessed. The new model was executed using Aspen Adsorption and validated using experimental data reported previously over silica gel bed. The validation was performed by comparing molar fractions of CH4 and CO2, temperature profile of silica gel bed, and bio-CH4 purity and recovery with previously reported experimental data. The particle mass transfer system, which estimated the adsorption rate and gas concentration profile in the adsorbent's particle, recorded the highest bio-CH4 purity of 99.12%. Lumped approach, which comprised mass transfer resistances in one overall resistance and ignored the dispersion effect, recorded bio-CH4 purity of 97.63% followed by micro-/macropore, which accounted micro and macropore resistance individually, with purity of 84.65%. Particle mass transfer approach yielded the highest bio-CH4 recovery of 96.745%, followed by lumped (95.41077%), and micro/macropore (82.433%) systems. Particle mass transfer was one of the most realistic systems in predicting the CO2 diffusion over silica gel due to its comprehensive heat/mass transfer consideration along with its assumption of uniform pore structure that fitted well with the true nature of the microporous silica character.
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页数:18
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