Measurement of H–LW–V and Dissociation Enthalpy of Carbon Dioxide Rich Synthetic Natural Gas Mixtures

2014 ◽  
Vol 59 (11) ◽  
pp. 3502-3509 ◽  
Author(s):  
Khalik M. Sabil ◽  
Qazi Nasir ◽  
Bezhad Partoon ◽  
Akbar A. Seman
2012 ◽  
Vol 53 ◽  
pp. 1-8 ◽  
Author(s):  
Mert Atilhan ◽  
Santiago Aparicio ◽  
Ferdi Karadas ◽  
Kenneth R. Hall ◽  
Rafael Alcalde

2009 ◽  
Vol 23 (3) ◽  
pp. 1640-1650 ◽  
Author(s):  
Andrew S. Brown ◽  
Martin J. T. Milton ◽  
Gergely M. Vargha ◽  
Richard Mounce ◽  
Chris J. Cowper ◽  
...  

2010 ◽  
Vol 55 (7) ◽  
pp. 2498-2504 ◽  
Author(s):  
Mert Atilhan ◽  
Santiago Aparicio ◽  
Rafael Alcalde ◽  
Gustavo A. Iglesias-Silva ◽  
Mahmoud El-Halwagi ◽  
...  

2018 ◽  
Vol 141 (2) ◽  
Author(s):  
William L. Becker ◽  
Michael Penev ◽  
Robert J. Braun

Power-to-gas to energy systems are of increasing interest for low carbon fuels production and as a low-cost grid-balancing solution for renewables penetration. However, such gas generation systems are typically focused on hydrogen production, which has compatibility issues with the existing natural gas pipeline infrastructures. This study presents a power-to-synthetic natural gas (SNG) plant design and a techno-economic analysis of its performance for producing SNG by reacting renewably generated hydrogen from low-temperature electrolysis with captured carbon dioxide. The study presents a “bulk” methanation process that is unique due to the high concentration of carbon oxides and hydrogen. Carbon dioxide, as the only carbon feedstock, has much different reaction characteristics than carbon monoxide. Thermodynamic and kinetic considerations of the methanation reaction are explored to design a system of multistaged reactors for the conversion of hydrogen and carbon dioxide to SNG. Heat recuperation from the methanation reaction is accomplished using organic Rankine cycle (ORC) units to generate electricity. The product SNG has a Wobbe index of 47.5 MJ/m3 and the overall plant efficiency (H2/CO2 to SNG) is shown to be 78.1% LHV (83.2% HHV). The nominal production cost for SNG is estimated at 132 $/MWh (38.8 $/MMBTU) with 3 $/kg hydrogen and a 65% capacity factor. At U.S. DOE target hydrogen production costs (2.2 $/kg), SNG cost is estimated to be as low as 97.6 $/MWh (28.6 $/MMBtu or 1.46 $/kgSNG).


2019 ◽  
Vol 34 ◽  
pp. 293-302 ◽  
Author(s):  
Chundong Zhang ◽  
Ruxing Gao ◽  
Ki-Won Jun ◽  
Seok Ki Kim ◽  
Sun-Mi Hwang ◽  
...  

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