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CO 2 Absorption from Biogas Using Piperazine-Promoted 2-Amino-2-methyl-1-propanol: Process Performance in a Packed Column

Author

Listed:
  • Viga Rajiman

    (Faculty of Chemical Engineering Technology, Universiti Malaysia Perlis, Kompleks Pusat Pengajian Jejawi 3, Arau 02600, Perlis, Malaysia)

  • Hairul Nazirah Abdul Halim

    (Faculty of Chemical Engineering Technology, Universiti Malaysia Perlis, Kompleks Pusat Pengajian Jejawi 3, Arau 02600, Perlis, Malaysia
    Centre of Excellence for Biomass Utilization, Universiti Malaysia Perlis, Kompleks Pusat Pengajian Jejawi 3, Arau 02600, Perlis, Malaysia)

  • Azmi Mohd Shariff

    (Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

  • Muhammad Zubair Shahid

    (Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

  • Abdulhalim Shah Maulud

    (Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

  • Kok Keong Lau

    (Department of Chemical Engineering, Universiti Teknologi PETRONAS, Bandar Seri Iskandar 32610, Perak, Malaysia)

  • Lian See Tan

    (Department of Chemical and Environmental Engineering (CHEE), Malaysia-Japan International Institute of Technology (MJIIT), Universiti Teknologi Malaysia (UTM), Jalan Sultan Yahya Petra, Kuala Lumpur 54100, Wilayah Persekutuan Kuala Lumpur, Malaysia)

Abstract

In this work, CO 2 absorption from simulated biogas is investigated using different blends of a PZ + AMP solution in an absorption system at CO 2 partial pressures ranging between 20 and 110 kPa. The collected data were presented as CO 2 removal profiles along the packed column and were evaluated in terms of CO 2 removal efficiency (%) and average overall volumetric mass transfer coefficient in the gas phase ( K G a v ¯ ). An increased PZ concentration in the AMP solution was found to significantly increase the CO 2 removal efficiency and K G a v ¯ values. It was observed that, when conducted at different CO 2 partial pressures, gas and liquid flow rates, and chemical concentrations, the L a m i n e / G C O 2 ratio strongly influenced the process behaviour in the packed column. Additionally, the optimal inlet liquid temperature was observed to be 35 ± 2 °C in this study.

Suggested Citation

  • Viga Rajiman & Hairul Nazirah Abdul Halim & Azmi Mohd Shariff & Muhammad Zubair Shahid & Abdulhalim Shah Maulud & Kok Keong Lau & Lian See Tan, 2022. "CO 2 Absorption from Biogas Using Piperazine-Promoted 2-Amino-2-methyl-1-propanol: Process Performance in a Packed Column," Sustainability, MDPI, vol. 14(12), pages 1-22, June.
    • Handle: RePEc:gam:jsusta:v:14:y:2022:i:12:p:7095-:d:835183
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    References listed on IDEAS

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    1. Rattanaphan, Supaporn & Rungrotmongkol, Thanyada & Kongsune, Panita, 2020. "Biogas improving by adsorption of CO2 on modified waste tea activated carbon," Renewable Energy, Elsevier, vol. 145(C), pages 622-631.
    2. Hosseini-Ardali, Seyed Mohsen & Hazrati-Kalbibaki, Majid & Fattahi, Moslem & Lezsovits, Ferenc, 2020. "Multi-objective optimization of post combustion CO2 capture using methyldiethanolamine (MDEA) and piperazine (PZ) bi-solvent," Energy, Elsevier, vol. 211(C).
    3. Hassankiadeh, Mojtaba Nabipoor & Jahangiri, Alireza, 2018. "Application of aqueous blends of AMP and piperazine to the low CO2 partial pressure capturing: New experimental and theoretical analysis," Energy, Elsevier, vol. 165(PB), pages 164-178.
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