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 |
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Main Authors: | , , , , , , , , , , , , , , |
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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. |
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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 |
Author_xml | – sequence: 1 givenname: Rivaldi surname: Sidabutar fullname: Sidabutar, Rivaldi email: rivaldi@usu.ac.id organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 2 givenname: Bambang surname: Trisakti fullname: Trisakti, Bambang organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 3 surname: Irvan fullname: Irvan organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 4 givenname: Michael surname: Michael fullname: Michael, Michael organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 5 givenname: Vanness surname: Vanness fullname: Vanness, Vanness organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 6 givenname: Vikram surname: Alexander fullname: Alexander, Vikram organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 7 givenname: Yenny surname: Natasya fullname: Natasya, Yenny organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 8 givenname: Della Sri Kristina surname: Pasaribu fullname: Pasaribu, Della Sri Kristina organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 9 givenname: Vandria surname: Alamsyah fullname: Alamsyah, Vandria organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 10 givenname: M. Ziniddin Zidan surname: Zaiyat fullname: Zaiyat, M. Ziniddin Zidan organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 11 givenname: Syafriandy surname: Syafriandy fullname: Syafriandy, Syafriandy organization: Institute for Research, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 12 givenname: M. Thoriq Al surname: Fath fullname: Fath, M. Thoriq Al organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 13 givenname: Nisaul Fadilah surname: Dalimunthe fullname: Dalimunthe, Nisaul Fadilah organization: Department of Chemical Engineering, Faculty of Engineering, Universitas Sumatera Utara, Medan 20155, Indonesia – sequence: 14 givenname: Peer Mohamed surname: Abdul fullname: Abdul, Peer Mohamed organization: Department of Chemical and Process Engineering, Faculty of Engineering and Built Environment, Universiti Kebangsaan Malaysia, 43600 Bangi, Selangor Darul Ehsan, Malaysia – sequence: 15 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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•Zeolite system produces near-pure methane for enhanced fuel applications.•Modified zeolites upgrade biogas from 69% to 99.29%... |
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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 |
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