“…191 Recent deployments of laboratory-scale microreactors have attracted much attention due to their ability to avoid mass and heat transfer limitations (due to high surface/volume ratio), reduce pressure drop, reduce residence time to control secondary reactions and improve CO 2 conversion and DME selectivity. 192 It is also possible to attach heat exchange units and hydrophilic membranes in the microreactors. 193,194 Koybasi et al modeled a membrane microchannel reactor with rectangular permeate and catalyst-coated (wash-coated Cu-ZnO/Al 2 O 3 + H-ZSM-5) reaction channels separated by a sodalite membrane layer that allows H 2 O and H 2 transport.…”
Section: Catalysis Science and Technology Reviewmentioning
The rapid and unparalleled advancement of human civilization has been made possible by the utilization of fossil feedstocks, beginning with coal, and followed by petroleum oil and natural gas. However,...
“…191 Recent deployments of laboratory-scale microreactors have attracted much attention due to their ability to avoid mass and heat transfer limitations (due to high surface/volume ratio), reduce pressure drop, reduce residence time to control secondary reactions and improve CO 2 conversion and DME selectivity. 192 It is also possible to attach heat exchange units and hydrophilic membranes in the microreactors. 193,194 Koybasi et al modeled a membrane microchannel reactor with rectangular permeate and catalyst-coated (wash-coated Cu-ZnO/Al 2 O 3 + H-ZSM-5) reaction channels separated by a sodalite membrane layer that allows H 2 O and H 2 transport.…”
Section: Catalysis Science and Technology Reviewmentioning
The rapid and unparalleled advancement of human civilization has been made possible by the utilization of fossil feedstocks, beginning with coal, and followed by petroleum oil and natural gas. However,...
“…3 Alternatively, side reactions (eqn (5) to (9)) can also occur, resulting in solid carbon deposits that may accumulate on the catalyst surface, ultimately triggering catalyst deactivation. CO 2(g) + 4H 2(g) = CH 4(g) + 2H 2 O (g) (1) CO 2(g) + H 2(g) = CO (g) + H 2 O (g) (2) CO 2(g) + CH 4(g) = 2CO (g) + 2H 2(g) ( 3)…”
Section: Introductionmentioning
confidence: 99%
“…1 Furthermore, it offers a transition from the carbon capture and storage (CCS) strategy to a more pragmatic and favorable carbon capture and utilization (CCU) approach. 2 Depending on the specific operational conditions, this reaction may be accompanied by concurrent side reactions, as illustrated in eqn (2) to (4). These side reactions can potentially yield undesired byproducts like carbon monoxide (CO) or consume methane, consequently leading to diminished product yield and selectivity.…”
CO2 methanation presents an intriguing avenue for utilizing carbon dioxide and generating methane as synthetic natural gas. Both reducibility and basicity of catalysts play a major role in catalytic performances improvement.
“…Developing various methods and materials to achieve carbon neutrality has attracted wide attention. [1][2][3] CO 2 capture and utilization (CCU) is an effective strategy for reducing CO 2 emissions. [4][5][6] The current CCU technology mainly includes several steps, such as CO 2 capture, adsorbent regeneration, and conversion of the captured CO 2 .…”
CO2 capture and selective methanation were realized over a greenly prepared Ni/CaO/Al2O3 composite at as low as 200 °C under static pressure conditions.
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