Production of Hydrogen-Rich Gas by Formic Acid Decomposition over CuO-CeO2/γ-Al2O3 Catalyst
Full article
Общее |
Language:
Английский,
Genre:
Full article,
Status:
Published,
Source type:
Original
|
Journal |
Energies
ISSN: 1996-1073
|
Output data |
Year: 2019,
Volume: 12,
Number: 18,
Article number
: 3577,
Pages count
: 10
DOI:
10.3390/en12183577
|
Tags |
formic acid decomposition; hydrogen production; CuO-CeO2/γ-Al2O3; multifuel processor; copper catalyst; oxygenates;
fuel cell |
Authors |
Pechenkin Alexey
1,2
,
Badmaev Sukhe
1,2
,
Belyaev Vladimir
1
,
Sobyanin Vladimir
1
|
Affiliations |
1 |
Boreskov Institute of Catalysis
|
2 |
Department of Natural Sciences, Novosibirsk State University
|
|
Funding (1)
1
|
Federal Agency for Scientific Organizations
|
0303-2016-0011
|
Formic acid decomposition to H2-rich gas was investigated over a CuO-CeO2/γ-Al2O3 catalyst. The catalyst was characterized by XRD, HR TEM and EDX methods. A 100% conversion of formic acid was observed over the copper-ceria catalyst under ambient pressure, at 200–300 °C, N2:HCOOH = 75:25 vol.% and flow rate 3500–35,000 h−1 with H2 yield of 98%, wherein outlet CO concentration is below the equilibrium data (<0.5 vol.%). The copper-ceria catalyst proved to be promising for multifuel processor application, and the H2 generation from dimethoxymethane, methanol, dimethyl ether and formic acid on the same catalyst for fuel cell supply.