Process simulation of single-step dimethyl ether production via biomass gasification

2009 ◽  
Vol 27 (5) ◽  
pp. 599-605 ◽  
Author(s):  
Fudong Ju ◽  
Hanping Chen ◽  
Xuejun Ding ◽  
Haiping Yang ◽  
Xianhua Wang ◽  
...  
Author(s):  
Aristide Giuliano ◽  
Enrico Catizzone ◽  
Cesare Freda

The production of dimethyl ether from renewables or waste is a promising strategy to push towards a sustainable energy transition of alternative eco-friendly diesel fuel. In this work, we simulate the synthesis of dimethyl ether from a syngas (a mixture of CO, CO2 and H2) produced from gasification of digestate. In particular, a thermodynamic analysis was performed to individuate the best process conditions and syngas conditioning processes to maximize yield to dimethyl etehr (DME). Process simulation was carried out by ChemCAD software, and it was particularly focused on the effect of process conditions of both water gas shift and CO2 absorption by Selexol® on the syngas composition, with a direct influence on DME productivity. The final best flowsheet and the best process conditions were evaluated in terms of CO2 equivalent emissions. Results show direct DME synthesis global yield was higher without the WGS section and with a carbon capture equal to 85%. The final environmental impact was found equal to −113 kgCO2/GJ, demonstrating that DME synthesis from digestate may be considered as a suitable strategy for carbon dioxide recycling.


2005 ◽  
Vol 106 (1-4) ◽  
pp. 265-270 ◽  
Author(s):  
Andrés T. Aguayo ◽  
Javier Ereña ◽  
Irene Sierra ◽  
Martin Olazar ◽  
Javier Bilbao

Eng ◽  
2020 ◽  
Vol 1 (1) ◽  
pp. 2-30
Author(s):  
Ioannis Voultsos ◽  
Dimitrios Katsourinis ◽  
Dimitrios Giannopoulos ◽  
Maria Founti

The energetic and environmental performance of a cogeneration biomass gasification plant, situated in Thessaly, Greece is evaluated via a methodology combining process simulation and Life Cycle Assessment (LCA). Initially, the gasification process of the most common agricultural residues found in the Thessaly region is simulated to establish the effect of technical parameters such as gasification temperature, equivalence ratio and raw biomass moisture content. It is shown that a maximum gasification efficiency of approximately 70% can be reached for all feedstock types. Lower efficiency values are associated with increased raw biomass moisture content. Next, the gasifier model is up-scaled, achieving the operation of a 1 MWel and 2.25 MWth cogeneration plant. The Life Cycle Assessment of the operation of the cogeneration unit is conducted using as input the performance data from the process simulation. Global Warming Potential and the Cumulative Demand of Non-Renewable Fossil Energy results suggest that the component which had the major share in both impact categories is the self-consumption of electricity of the plant. Finally, the key conclusion of the present study is the quantification of carbon dioxide mitigation and non-renewable energy savings by comparing the biomass cogeneration unit operation with conventional reference cases.


1990 ◽  
Vol 45 (8) ◽  
pp. 2735-2741 ◽  
Author(s):  
J.J. Lewnard ◽  
T.H. Hsiung ◽  
J.F. White ◽  
D.M. Brown

2017 ◽  
Vol 540 ◽  
pp. 68-74 ◽  
Author(s):  
Yuxi Hua ◽  
Xiaoming Guo ◽  
Dongsen Mao ◽  
Guanzhong Lu ◽  
Garry L. Rempel ◽  
...  

2016 ◽  
Vol 6 (4) ◽  
pp. 1054-1063 ◽  
Author(s):  
M. Gentzen ◽  
W. Habicht ◽  
D. E. Doronkin ◽  
J.-D. Grunwaldt ◽  
J. Sauer ◽  
...  

Model kit for bifunctional catalysts: colloidal Cu/Zn-based nanoparticles were synthesized and used as building blocks in syngas to dimethyl ether (STD) catalysts.


2014 ◽  
Vol 228 ◽  
pp. 175-182 ◽  
Author(s):  
Yeong Jun Lee ◽  
Min Hye Jung ◽  
Jong-Bae Lee ◽  
Kwang-Eun Jeong ◽  
Hyun-Seog Roh ◽  
...  

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