Dry Reforming of Methane in DBD Plasma over Ni‐Based Catalysts: Influence of Process Conditions and Support on Performance and Durability

2019 ◽  
Vol 7 (4) ◽  
pp. 1801008 ◽  
Author(s):  
Debjyoti Ray ◽  
Devadutta Nepak ◽  
Sagar Janampelli ◽  
Partha Goshal ◽  
Ch. Subrahmanyam
Keyword(s):  
Dry Reforming ◽  
Dry Reforming Of Methane ◽  
Process Conditions ◽  
Dbd Plasma

Glass Beads Packed DBD-Plasma Assisted Dry Reforming of Methane

2017 ◽  
Vol 60 (12-14) ◽  
pp. 869-878 ◽  
Author(s):  
Debjyoti Ray ◽  
P. Manoj Kumar Reddy ◽  
Subrahmanyam Challapalli
Keyword(s):  
Dry Reforming ◽  
Glass Beads ◽  
Dry Reforming Of Methane ◽  
Dbd Plasma

Kinetic study of dry reforming of methane using hybrid DBD plasma reactor over La2O3 co-supported Ni/MgAl2O4 catalyst

2020 ◽  
Vol 45 (22) ◽  
pp. 12256-12271 ◽  
Author(s):  
Asif Hussain Khoja ◽  
Muhammad Tahir ◽  
Nor Aishah Saidina Amin ◽  
Adeel Javed ◽  
Muhammad Taqi Mehran
Keyword(s):  
Kinetic Study ◽  
Plasma Reactor ◽  
Dry Reforming ◽  
Dry Reforming Of Methane ◽  
Dbd Plasma ◽  
Supported Ni

How gas flow design can influence the performance of a DBD plasma reactor for dry reforming of methane

2021 ◽  
Vol 405 ◽  
pp. 126618
Author(s):  
Y. Uytdenhouwen ◽  
J. Hereijgers ◽  
T. Breugelmans ◽  
P. Cool ◽  
A. Bogaerts
Keyword(s):  
Gas Flow ◽  
Plasma Reactor ◽  
Dry Reforming ◽  
Dry Reforming Of Methane ◽  
Dbd Plasma

scholarly journals Carbon Dioxide Reforming of Methane over Zeolite-containing Catalysts

2016 ◽  
Vol 11 (3) ◽  
pp. 231 ◽  
Author(s):  
Sholpan S. Itkulova
Keyword(s):  
Carbon Dioxide ◽  
Acetic Acid ◽  
Main Product ◽  
Dry Reforming ◽  
Zeolite Catalysts ◽  
Dry Reforming Of Methane ◽  
Process Conditions ◽  
Carbon Dioxide Reforming ◽  
Zeolite Type

<p>Reforming of methane by carbon dioxide (dry reforming of methane) has been studied over the series of the 5% Со-М/Al<sub>2</sub>O<sub>3</sub>+ zeolite catalysts. The effect of zeolite (type, module, and amount) added to support composition on performance of the Со-М/Al<sub>2</sub>O<sub>3</sub> catalyst in dry reforming has been examined. It has been shown that syngas is a main product of dry reforming over the zeolite-containing catalysts. Also, some amount (up to 3%) of acetic acid is produced. The yield of syngas and acetic acid depends on nature and amount of zeolite and process conditions.</p>

g-C3N4 promoted DBD plasma assisted dry reforming of methane

Energy ◽  
2019 ◽  
Vol 183 ◽  
pp. 630-638 ◽  
Author(s):  
Debjyoti Ray ◽  
Devadutta Nepak ◽  
T. Vinodkumar ◽  
Ch. Subrahmanyam
Keyword(s):  
Dry Reforming ◽  
Dry Reforming Of Methane ◽  
Dbd Plasma

Carbon Dioxide Reforming Of Methane By Catalytic–Plasma Reactor Over Cu/Zn/γ–Al2O3

2012 ◽  
Author(s):  
Maryam Khoshtinat Nikoo ◽  
Mohammad Ali Sharifi ◽  
Noraishah Saidina Amin
Keyword(s):  
Carbon Dioxide ◽  
Plasma Reactor ◽  
Input Power ◽  
Dry Reforming ◽  
Dry Reforming Of Methane ◽  
Dbd Plasma ◽  
Catalytic Hydrogen ◽  
Fragmentation Reactions ◽  
H2 Yield ◽  
Al2o3 Catalyst

Dalam kajian semasa, pengaruh kuasa input untuk penukaran CH4 dan CO2 ke syngas disiasat di dalam kedua–dua reaktor silinder plasma DBD dan reaktor plasma pemangkin. Diperhatikan bahawa untuk kedua-dua reaktor, input kuasa yang lebih tinggi menyokong tindak balas pemecahan dan bukannya penggabungan semula perantaraan ringan kepada hidrokarbon yang lebih berat, meningkatkan hasil H2. Sementara itu, kehadiran mangkin Cu/Zn/Al2O3 mempertingkatkan pengeluaran H2 daripada 16.5% kepada 19.1%, manakala nisbah H2/CO kekal hampir malar berhampiran nilai 1, nisbah yang sesuai untuk proses FTS. Kata kunci: Plasma; catalytic, hydrogen; dry reforming of methane In the current study, the influence of input power for conversion of CH4 and CO2 into syngas was investigated in both DBD plasma and catalytic–plasma cylindrical reactors. It was observed that for both reactors, higher input power favored fragmentation reactions rather than recombination of light intermediates into heavier hydrocarbons, improving H2 yield. Meanwhile, the presence of Cu/Zn/Al2O3 catalyst enhanced the H2 yield from 16.5 % to 19.1%, while the H2/CO ratio remained almost constant near unity, the suitable ratio for FTS processes. Key words: Plasma, catalytic, hydrogen, dry reforming of methane

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