TY - JOUR
T1 - Comparative life cycle assessment and economic analysis of methanol/hydrogen production processes for fuel cell vehicles
AU - Wu, Wei
AU - Pai, Ching Ting
AU - Viswanathan, Karthickeyan
AU - Chang, Jo Shu
N1 - Funding Information:
This work was financially supported by the Ministry of Science and Technology of R.O.C. (Taiwan) under grant 1072211E006101, and thanks to National Cheng Kung University, Taiwan Grants- NCKU 90 and Beyond for Research Fellow with grant number HUB109-22T-3–173.
Publisher Copyright:
© 2021 Elsevier Ltd
PY - 2021/6/1
Y1 - 2021/6/1
N2 - The life cycle assessment (LCA) of hydrogen/methanol production processes connected with hydrogen fuel cell vehicle (HFCV) and methanol reformer-embedded fuel cell vehicle (MRFCV) are addressed. According to the scope definition of well-to-wheel and the four steps of LCA methodology, the ReCiPe endpoint score of the natural gas-fed methanol production process named by SC1MeOH is up to 2.06 kPt, which is higher than the natural gas-fed hydrogen production process called SC2H2 by 50.3%. The new biomethanol production process termed by SC3MeOH, which is a combination of anaerobic co-digestion, microalgae production process, and combined heat and power (CHP), is validated to reduce the environmental impact of SC1MeOH by 93.6% due to wheat straw (waste) and microalgae as inlet sources, almost zero air pollutants, 58% carbons stored in the soil of the wheatland, and no grid supply. A comparative LCA shows that the MRFCV connected with SC3MeOH is lower than the HFCV associated with SC2H2 by 40%. The Levelized cost of methanol (LCOM) for SC3MeOH (about 3.08USD/kgMeOH) is higher than SC1MeOH by 18.6%. These comparisons show that the MRFCV connected with SC3MeOH is an HFVC for green cars due to relatively low investments in storage facilities and transport and minimum environmental impacts.
AB - The life cycle assessment (LCA) of hydrogen/methanol production processes connected with hydrogen fuel cell vehicle (HFCV) and methanol reformer-embedded fuel cell vehicle (MRFCV) are addressed. According to the scope definition of well-to-wheel and the four steps of LCA methodology, the ReCiPe endpoint score of the natural gas-fed methanol production process named by SC1MeOH is up to 2.06 kPt, which is higher than the natural gas-fed hydrogen production process called SC2H2 by 50.3%. The new biomethanol production process termed by SC3MeOH, which is a combination of anaerobic co-digestion, microalgae production process, and combined heat and power (CHP), is validated to reduce the environmental impact of SC1MeOH by 93.6% due to wheat straw (waste) and microalgae as inlet sources, almost zero air pollutants, 58% carbons stored in the soil of the wheatland, and no grid supply. A comparative LCA shows that the MRFCV connected with SC3MeOH is lower than the HFCV associated with SC2H2 by 40%. The Levelized cost of methanol (LCOM) for SC3MeOH (about 3.08USD/kgMeOH) is higher than SC1MeOH by 18.6%. These comparisons show that the MRFCV connected with SC3MeOH is an HFVC for green cars due to relatively low investments in storage facilities and transport and minimum environmental impacts.
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U2 - 10.1016/j.jclepro.2021.126959
DO - 10.1016/j.jclepro.2021.126959
M3 - Article
AN - SCOPUS:85104058638
SN - 0959-6526
VL - 300
JO - Journal of Cleaner Production
JF - Journal of Cleaner Production
M1 - 126959
ER -