Journal
CHEMICAL ENGINEERING JOURNAL
Volume 269, Issue -, Pages 148-158Publisher
ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2015.01.100
Keywords
Bio-hydrogen; Biogas; Dark fermentation; Activated carbon; CO2 capture; Breakthrough test
Categories
Funding
- Spanish MINECO [ENE2011-23467]
- European Regional Development Fund (ERDF)
- Principado de Asturias (PCTI)
- European Social Fund
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The biological production of H-2 by dark fermentation is being extensively investigated due to the great potential of the two-phase hydrogen/methane fermentation process for recovering energy from carbohydrate-rich wastes. However, the purification of the bio-hydrogen and biogas obtained is needed to produce high-purity H-2 and CH4 streams appropriate for industrial application. In this study, the performance of three activated carbons (No1KCla-600, No1KClb-1000 and No2OS-1000), synthesized from phenol-formaldehyde resins, as potential adsorbents for CO2 capture from bio-hydrogen and biogas streams has been evaluated under dynamic conditions. Adsorption-desorption cycles by means of temperature swings were conducted at ambient temperature and atmospheric pressure with CO2/H-2 (40/60 and 70/30 vol.%) and CO2/CH4 (50/50 vol.%) binary gas mixtures in a purpose-built fixed-bed set-up. The performance of the resin-derived carbons to separate CO2 was superior to that of reference commercial carbons in terms of CO2 uptake, breakthrough time and column efficiency. These adsorbents presented high CO2/H-2 and CO2/CH4 selectivity values, were easily completely regenerated and did not show capacity decay after multiple cycling. Breakthrough capacities reached 2.11 and 2.03 mmol g(-1) at 25 degrees C for 70/30 CO2/H-2 and 50/50 CO2/CH4, respectively. The NO2OS-1000 adsorbent, produced from phenol-formaldehyde resin and olive stones (20:80 wt.), gave the greatest values of CO2 capture capacity on a volumetric basis and CO2/CH4 selectivity, which may be advantageous to biogas purification applications because it reduces the size of the necessary equipment. (C) 2015 Elsevier B.V. All rights reserved.
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