Techno-economic analysis of adiabatic four-stage CO2 methanation process for optimization and evaluation of power-to-gas technology

Author(s):  
Sungho Park ◽  
Kwangsoon Choi ◽  
Changhyeong Lee ◽  
Suhyun Kim ◽  
Youngdon Yoo ◽  
...  
2021 ◽  
Vol 173 ◽  
pp. 12-23
Author(s):  
Robert Bedoić ◽  
Hrvoje Dorotić ◽  
Daniel Rolph Schneider ◽  
Lidija Čuček ◽  
Boris Ćosić ◽  
...  

2021 ◽  
Vol 50 ◽  
pp. 101610
Author(s):  
Maxime Hervy ◽  
Jonathan Maistrello ◽  
Larissa Brito ◽  
Mathilde Rizand ◽  
Etienne Basset ◽  
...  

2020 ◽  
Vol 202 ◽  
pp. 106365 ◽  
Author(s):  
Antonio Vita ◽  
Cristina Italiano ◽  
Lidia Pino ◽  
Massimo Laganà ◽  
Marco Ferraro ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (9) ◽  
pp. 1670 ◽  
Author(s):  
Martin Thema ◽  
Tobias Weidlich ◽  
Manuel Hörl ◽  
Annett Bellack ◽  
Friedemann Mörs ◽  
...  

Power-to-Methane as one part of Power-to-Gas has been recognized globally as one of the key elements for the transition towards a sustainable energy system. While plants that produce methane catalytically have been in operation for a long time, biological methanation has just reached industrial pilot scale and near-term commercial application. The growing importance of the biological method is reflected by an increasing number of scientific articles describing novel approaches to improve this technology. However, these studies are difficult to compare because they lack a coherent nomenclature. In this article, we present a comprehensive set of parameters allowing the characterization and comparison of various biological methanation processes. To identify relevant parameters needed for a proper description of this technology, we summarized existing literature and defined system boundaries for Power-to-Methane process steps. On this basis, we derive system parameters providing information on the methanation system, its performance, the biology and cost aspects. As a result, three different standards are provided as a blueprint matrix for use in academia and industry applicable to both, biological and catalytic methanation. Hence, this review attempts to set the standards for a comprehensive description of biological and chemical methanation processes.


2017 ◽  
Vol 11 ◽  
pp. 16-24 ◽  
Author(s):  
Frédéric David Meylan ◽  
Frédéric-Paul Piguet ◽  
Suren Erkman

2022 ◽  
Author(s):  
Dominik Meyer ◽  
Jannik Schumacher ◽  
Jens Friedland ◽  
Robert Güttel

The utilization of renewable electricity for power-to-gas (PtG) applications induces fluctuations in the H2 availability from water electrolysis. For subsequent methanation of CO or CO2 the unsteady-state operation of the respective reactor allows to minimize H2 storage capacities. However, the impact of temporal fluctuations in feed gas composition on the methanation reaction and the respective transient kinetics has not yet been fully understood. We investigated the methanation of various CO/CO2 (COx) feed gas mixtures under periodically changing gas compositions with emphasis on the effect of the frequency on the reactor response. We show that the frequency response of CH4 exhibits a characteristic hysteresis, which depends on the switching direction between COx-lean and COx-rich feeds and their composition. From the shape of the hysteresis we are able to conclude on the preferred COx species being hydrogenated to CH4 under respective conditions, which also provides mechanistic insights. By applying high cycling frequencies, the highly reactive species present under CO methanation conditions can even selectively be activated, which explains the higher reactivity compared to steady-state conditions reported, frequently.


2019 ◽  
Vol 3 (9) ◽  
pp. 2521-2529 ◽  
Author(s):  
Boreum Lee ◽  
Hyunjun Lee ◽  
Juheon Heo ◽  
Changhwan Moon ◽  
Sangbong Moon ◽  
...  

A stochastic techno-economic analysis is conducted to evaluate economic feasibility for power-to-gas technology using a high-pressure PEM water electrolyzer.


Catalysts ◽  
2020 ◽  
Vol 10 (3) ◽  
pp. 283 ◽  
Author(s):  
Eduard Alexandru Morosanu ◽  
Fabio Salomone ◽  
Raffaele Pirone ◽  
Samir Bensaid

Power to gas systems is one of the most interesting long-term energy storage solutions. As a result of the high exothermicity of the CO2 methanation reaction, the catalyst in the methanation subsystem is subjected to thermal stress. Therefore, the performance of a commercial Ni/Al2O3 catalyst was investigated over a series of 100 hour-long tests and in-process relevant conditions, i.e. 5 bar from 270 to 500 °C. Different characterization techniques were employed to determine the mechanism of the observed performance loss (N2 physisorption, XRD, TPO). The TPO analysis excluded carbon deposition as a possible cause of catalyst aging. The BET analysis evidenced a severe reduction in the total surface area for the catalyst samples tested at higher temperatures. Furthermore, a direct correlation was found between the catalyst activity decline and the drop of the catalyst specific surface. In order to correctly design a reliable methanation reactor, it is essential to have a kinetic model that includes also the aging kinetics. For this purpose, the second set of experiments was carried out, in order to determine the intrinsic kinetics of the catalyst. The kinetic parameters were identified by using nonlinear regression analysis. Finally, a power-law aging model was proposed to consider the performance loss in time.


2021 ◽  
Author(s):  
Changgwon Choe ◽  
Boreum Lee ◽  
Ayeon Kim ◽  
Seunghyun Cheon ◽  
Hankwon Lim

The analytic hierarchy process was performed to determine the best alternative for green methane production based on the results of technical assessment, economic analysis, and life cycle assessment.


2019 ◽  
Vol 377 ◽  
pp. 120233 ◽  
Author(s):  
Fabio Salomone ◽  
Emanuele Giglio ◽  
Domenico Ferrero ◽  
Massimo Santarelli ◽  
Raffaele Pirone ◽  
...  

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