Developing descriptors for CO2 methanation and CO2 reforming of CH4 over Al2O3 supported Ni and low-cost Ni based alloy catalysts

2018 ◽  
Vol 20 (23) ◽  
pp. 15939-15950 ◽  
Author(s):  
Koustuv Ray ◽  
Rahul Bhardwaj ◽  
Bahadur Singh ◽  
Goutam Deo

The catalytic performance of Ni can be modified by alloying with a suitable amount (25% of total metal loading) of another low-cost metal such as Fe, Co or Cu.

2013 ◽  
Vol 38 (31) ◽  
pp. 13649-13654 ◽  
Author(s):  
Dae-Woon Jeong ◽  
Won-Jun Jang ◽  
Jae-Oh Shim ◽  
Hyun-Seog Roh ◽  
In Hyuk Son ◽  
...  

2020 ◽  
Vol 44 (29) ◽  
pp. 12503-12513
Author(s):  
Penggang Lv ◽  
Dawei Liu ◽  
Bin Tian ◽  
Xiaoxun Ma ◽  
Maohong Fan ◽  
...  

A schematic diagram for the reaction of CH4 and CO2 over a Ni/bio-char catalyst.


2016 ◽  
Vol 55 (16) ◽  
pp. 4451-4460 ◽  
Author(s):  
Salvatore Abate ◽  
Chalachew Mebrahtu ◽  
Emanuele Giglio ◽  
Fabio Deorsola ◽  
Samir Bensaid ◽  
...  

2017 ◽  
Vol 380 ◽  
pp. 151-160 ◽  
Author(s):  
Sara Faiz Hanna Tasfy ◽  
Noor Asmawati Mohd Zabidi ◽  
Maizatul Shima Shaharun ◽  
Duvvria Subbarao ◽  
Ahmed Elbagir

Utilization of CO2 as a carbon source to produce valuable chemicals is one of the important ways to reduce the global warming caused by increasing CO2 in the atmosphere. Supported metal catalysts are crucial to produce clean and renewable fuels and chemicals from the stable CO2 molecules. The catalytic conversion of CO2 into methanol is recently under increased scrutiny as an opportunity to be used as a low-cost carbon source. Therefore, a series of the bimetallic Cu/ZnO-based catalyst supported by SBA-15 were synthesized via an impregnation technique with different total metal loading and tested in the catalytic hydrogenation of CO2 to methanol. The morphological and textural properties of the synthesized catalysts were determined by transmission electron microscopy (TEM), temperature programmed desorption, reduction, oxidation and pulse chemisorption (TPDRO), and N2-adsorption. The CO2 hydrogenation reaction was performed in a microactivity fixed-bed system at 250oC, 2.25 MPa, and H2/CO2 ratio of 3. Experimental results showed that the catalytic structure and performance were strongly affected by the loading of the active site. Where, the catalytic activity, the methanol selectivity as well as the space-time yield increased with increasing the metal loading until it reaches the maximum values at a metal loading of 15 wt% while further addition of metal inhibits the catalytic performance. The higher catalytic activity of 14% and methanol selectivity of 92% was obtained over a Cu/ZnO-SBA-15 catalyst with a total bimetallic loading of 15 wt%. The excellent performance of 15 wt% Cu/ZnO-SBA-15 catalyst is attributed to the presence of well dispersed active sites with small particle size, higher Cu surface area, and lower catalytic reducibility.


2004 ◽  
Vol 263 (1) ◽  
pp. 1-9 ◽  
Author(s):  
J Rynkowski ◽  
P Samulkiewicz ◽  
A.K Ladavos ◽  
P.J Pomonis

2014 ◽  
Vol 4 (6) ◽  
pp. 1759-1770 ◽  
Author(s):  
Leilei Xu ◽  
Zhichao Miao ◽  
Huanling Song ◽  
Wei Chen ◽  
Lingjun Chou

The significant roles of mesostructure and basic modifier in improving the catalytic performance of dry reforming were investigated.


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