Synergistic integration of zeolite engineering and fixed-bed column design for enhanced biogas upgrading: Adsorbent synthesis, CO2/CH4 separation kinetics, and regeneration assessment

[Display omitted] •Zeolite system produces near-pure methane for enhanced fuel applications.•Modified zeolites upgrade biogas from 69% to 99.29% CH4.•Dual-chemical activation boosts zeolite adsorption in fixed-bed column.•Dual chemically-activated zeolites achieve 97.77 ± 0.01 % CO2 adsorption.•Opti...

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Published in:Separation and purification technology Vol. 355; p. 129772
Main Authors: Sidabutar, Rivaldi, Trisakti, Bambang, Irvan, Michael, Michael, Vanness, Vanness, Alexander, Vikram, Natasya, Yenny, Pasaribu, Della Sri Kristina, Alamsyah, Vandria, Zaiyat, M. Ziniddin Zidan, Syafriandy, Syafriandy, Fath, M. Thoriq Al, Dalimunthe, Nisaul Fadilah, Abdul, Peer Mohamed, Takriff, Mohd Sobri
Format: Journal Article
Language:English
Published: Elsevier B.V 01-03-2025
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Abstract [Display omitted] •Zeolite system produces near-pure methane for enhanced fuel applications.•Modified zeolites upgrade biogas from 69% to 99.29% CH4.•Dual-chemical activation boosts zeolite adsorption in fixed-bed column.•Dual chemically-activated zeolites achieve 97.77 ± 0.01 % CO2 adsorption.•Optimal conditions: 30-min adsorption, 17-min desorption at 40 °C. Biogas, a renewable energy vector derived from anaerobic digestion of organic waste, requires CO2 separation to enhance its calorific value for engine fuel. This study integrates CO2/CH4 separation in biogas using a novel approach integrating dual chemically-activated zeolites and fixed-bed column purification. Biogas produced via CSTR/ultrafiltration (69 % CH4, 30 % CO2, 14 ppm H2S) was further upgraded using HCl + NaOH and H2SO4 + NaOH activated zeolites. Optimal absorption capacity of 97.77 ± 0.01 % was achieved at 140 mesh, 60-minute H2SO4 + NaOH activation, 2-hour calcination (400 °C), and 200 mL/min flow rate. Breakthrough was observed at 18.12 min. Langmuir isotherm (R2 = 0.9992) and Elovich kinetics (R2 = 0.9846) best described the adsorption process. XRD analysis showed significant crystal size reduction post-activation (53.31 nm to 16.90 nm). Notably, BET analysis revealed enhanced surface properties surface area of 286.71 m2/g, pore volume of 0.213 cc/g, and pore diameter of 3.532 Å. An innovative dual-column system with non-isothermal TSA protocol optimized CO2 adsorption (30 mins) and desorption (17 mins, 40 °C, 100 mL/min), yielding superior near-pure methane biogas (99.29 % CH4, 0.66 % CO2, trace H2S). A methane loss of 2.75 % during upgrading demonstrated high CO2 selectivity. This synergistic approach presents a promising solution for sustainable biogas purification and engine fuel applications.
AbstractList [Display omitted] •Zeolite system produces near-pure methane for enhanced fuel applications.•Modified zeolites upgrade biogas from 69% to 99.29% CH4.•Dual-chemical activation boosts zeolite adsorption in fixed-bed column.•Dual chemically-activated zeolites achieve 97.77 ± 0.01 % CO2 adsorption.•Optimal conditions: 30-min adsorption, 17-min desorption at 40 °C. Biogas, a renewable energy vector derived from anaerobic digestion of organic waste, requires CO2 separation to enhance its calorific value for engine fuel. This study integrates CO2/CH4 separation in biogas using a novel approach integrating dual chemically-activated zeolites and fixed-bed column purification. Biogas produced via CSTR/ultrafiltration (69 % CH4, 30 % CO2, 14 ppm H2S) was further upgraded using HCl + NaOH and H2SO4 + NaOH activated zeolites. Optimal absorption capacity of 97.77 ± 0.01 % was achieved at 140 mesh, 60-minute H2SO4 + NaOH activation, 2-hour calcination (400 °C), and 200 mL/min flow rate. Breakthrough was observed at 18.12 min. Langmuir isotherm (R2 = 0.9992) and Elovich kinetics (R2 = 0.9846) best described the adsorption process. XRD analysis showed significant crystal size reduction post-activation (53.31 nm to 16.90 nm). Notably, BET analysis revealed enhanced surface properties surface area of 286.71 m2/g, pore volume of 0.213 cc/g, and pore diameter of 3.532 Å. An innovative dual-column system with non-isothermal TSA protocol optimized CO2 adsorption (30 mins) and desorption (17 mins, 40 °C, 100 mL/min), yielding superior near-pure methane biogas (99.29 % CH4, 0.66 % CO2, trace H2S). A methane loss of 2.75 % during upgrading demonstrated high CO2 selectivity. This synergistic approach presents a promising solution for sustainable biogas purification and engine fuel applications.
ArticleNumber 129772
Author Irvan
Alamsyah, Vandria
Dalimunthe, Nisaul Fadilah
Trisakti, Bambang
Takriff, Mohd Sobri
Zaiyat, M. Ziniddin Zidan
Sidabutar, Rivaldi
Fath, M. Thoriq Al
Alexander, Vikram
Michael, Michael
Syafriandy, Syafriandy
Natasya, Yenny
Pasaribu, Della Sri Kristina
Vanness, Vanness
Abdul, Peer Mohamed
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  givenname: M. Ziniddin Zidan
  surname: Zaiyat
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  surname: Syafriandy
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  givenname: M. Thoriq Al
  surname: Fath
  fullname: Fath, M. Thoriq Al
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  givenname: Nisaul Fadilah
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  surname: Abdul
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  organization: Department of Chemical and Process Engineering, Faculty of Engineering and Built Environment, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor Darul Ehsan, Malaysia
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  givenname: Mohd Sobri
  surname: Takriff
  fullname: Takriff, Mohd Sobri
  organization: Department of Chemical and Process Engineering, Faculty of Engineering and Built Environment, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor Darul Ehsan, Malaysia
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Keywords Zeolite modification
Regeneration
Biogas upgrading
CO2/CH4 separation
Fixed bed
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Snippet [Display omitted] •Zeolite system produces near-pure methane for enhanced fuel applications.•Modified zeolites upgrade biogas from 69% to 99.29%...
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StartPage 129772
SubjectTerms Biogas upgrading
CO2/CH4 separation
Fixed bed
Regeneration
Zeolite modification
Title Synergistic integration of zeolite engineering and fixed-bed column design for enhanced biogas upgrading: Adsorbent synthesis, CO2/CH4 separation kinetics, and regeneration assessment
URI https://dx.doi.org/10.1016/j.seppur.2024.129772
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