共 103 条
Catalytic Hydrogen Production from Methane: A Review on Recent Progress and Prospect
被引:273
作者:

Chen, Luning
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Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA

Qi, Zhiyuan
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Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA

Zhang, Shuchen
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Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA

Su, Ji
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Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA
Lawrence Berkeley Natl Lab, Mat Sci Div, Mol Foundry, Berkeley, CA 94720 USA Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA

Somorjai, Gabor A.
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Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA
Univ Calif Berkeley, Dept Chem, Berkeley, CA 94720 USA Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA
机构:
[1] Lawrence Berkeley Natl Lab, Mat Sci Div, Berkeley, CA 94720 USA
[2] Lawrence Berkeley Natl Lab, Mat Sci Div, Mol Foundry, Berkeley, CA 94720 USA
[3] Univ Calif Berkeley, Dept Chem, Berkeley, CA 94720 USA
来源:
关键词:
hydrogen economic;
methane conversion;
heterogeneous catalysts;
LOW-TEMPERATURE;
CARBON NANOFIBERS;
PARTIAL OXIDATION;
NICKEL-CATALYSTS;
SYNTHESIS GAS;
FE CATALYSTS;
NI CATALYSTS;
DIRECT DECOMPOSITION;
FILAMENTOUS CARBON;
PROCESS PARAMETERS;
D O I:
10.3390/catal10080858
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
Natural gas (Methane) is currently the primary source of catalytic hydrogen production, accounting for three quarters of the annual global dedicated hydrogen production (about 70 M tons). Steam-methane reforming (SMR) is the currently used industrial process for hydrogen production. However, the SMR process suffers with insufficient catalytic activity, low long-term stability, and excessive energy input, mostly due to the handling of large amount of CO(2)coproduced. With the demand for anticipated hydrogen production to reach 122.5 M tons in 2024, novel and upgraded catalytic processes are desired for more effective utilization of precious natural resources. In this review, we summarized the major descriptors of catalyst and reaction engineering of the SMR process and compared the SMR process with its derivative technologies, such as dry reforming with CO2(DRM), partial oxidation with O-2, autothermal reforming with H2O and O-2. Finally, we discussed the new progresses of methane conversion: direct decomposition to hydrogen and solid carbon and selective oxidation in mild conditions to hydrogen containing liquid organics (i.e., methanol, formic acid, and acetic acid), which serve as alternative hydrogen carriers. We hope this review will help to achieve a whole picture of catalytic hydrogen production from methane.
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Boreskov Inst Catalysis, Novosibirsk 630090, Russia Boreskov Inst Catalysis, Novosibirsk 630090, Russia

Ismagilov, ZR
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Boreskov Inst Catalysis, Novosibirsk 630090, Russia Boreskov Inst Catalysis, Novosibirsk 630090, Russia

Likholobov, VA
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Boreskov Inst Catalysis, Novosibirsk 630090, Russia Boreskov Inst Catalysis, Novosibirsk 630090, Russia
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Ay, Hale
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Middle E Tech Univ, Chem Engn, TR-06800 Ankara, Turkey Middle E Tech Univ, Chem Engn, TR-06800 Ankara, Turkey

Uner, Deniz
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Middle E Tech Univ, Chem Engn, TR-06800 Ankara, Turkey Middle E Tech Univ, Chem Engn, TR-06800 Ankara, Turkey