4.6 Article

A techno-economic and life cycle assessment for the production of green methanol from CO2: catalyst and process bottlenecks

Journal

JOURNAL OF ENERGY CHEMISTRY
Volume 68, Issue -, Pages 255-266

Publisher

ELSEVIER
DOI: 10.1016/j.jechem.2021.09.045

Keywords

CO2; Methanol; Kinetic modeling; Process simulation; Life cycle assessment

Funding

  1. King Abdullah University of Science and Technology (KAUST)
  2. Spanish Ministry of Science and Innovation
  3. ERDF funds [CTQ2016-77812-R]
  4. Basque Government [IT1218-19]
  5. Spanish Ministry of Education, Culture and Sport [FPU15-01666]
  6. Spanish Ministerio de Ciencia, Innovacion y Universidades
  7. European Regional Development Fund (ERDF/FEDER) [RTI2018-096294-B-C31]
  8. Banco de Santander
  9. Universidad Publica de Navarra

Ask authors/readers for more resources

This study provides a comprehensive analysis of the process of converting CO2 into green methanol, including kinetic analysis of catalysts, process simulation, techno-economic assessment, and life cycle evaluation. The results indicate that using renewable energy is crucial for CO2 abatement and profitable methanol production.
The success of catalytic schemes for the large-scale valorization of CO2 does not only depend on the development of active, selective and stable catalytic materials but also on the overall process design. Here we present a multidisciplinary study (from catalyst to plant and techno-economic/lifecycle analysis) for the production of green methanol from renewable H-2 and CO2. We combine an in-depth kinetic analysis of one of the most promising recently reported methanol-synthesis catalysts (InCo) with a thorough process simulation and techno-economic assessment. We then perform a life cycle assessment of the simulated process to gauge the real environmental impact of green methanol production from CO2. Our results indicate that up to 1.75 ton of CO2 can be abated per ton of produced methanol only if renewable energy is used to run the process, while the sensitivity analysis suggest that either rock-bottom H-2 prices (1.5 $ kg(-1)) or severe CO2 taxation (300 $ per ton) are needed for a profitable methanol plant. Besides, we herein highlight and analyze some critical bottlenecks of the process. Especial attention has been paid to the contribution of H-2 to the overall plant costs, CH4 trace formation, and purity and costs of raw gases. In addition to providing important information for policy makers and industrialists, directions for catalyst (and therefore process) improvements are outlined. (C) 2021 Science Press and Dalian Institute of Chemical Physics, Chinese Academy of Sciences. Published by ELSEVIER B.V. and Science Press.

Authors

I am an author on this paper
Click your name to claim this paper and add it to your profile.

Reviews

Primary Rating

4.6
Not enough ratings

Secondary Ratings

Novelty
-
Significance
-
Scientific rigor
-
Rate this paper

Recommended

No Data Available
No Data Available