New Journal at De Gruyter!
International Journal of Chemical Reactor Engineering
Ed. by de Lasa, Hugo / Xu, Charles Chunbao
4 Issues per year
IMPACT FACTOR increased in 2014: 0.592
5-year IMPACT FACTOR: 0.678
SCImago Journal Rank (SJR): 0.303
Source Normalized Impact per Paper (SNIP): 0.426
Volume 13 (2015)
Volume 12 (2014)
Volume 11 (2013)
Volume 10 (2012)
Volume 9 (2011)
Volume 8 (2010)
Volume 7 (2009)
Volume 6 (2008)
Volume 5 (2007)
Volume 4 (2006)
Volume 3 (2005)
Volume 2 (2004)
Volume 1 (2002)
Most Downloaded Articles
- Design and Optimization of a Fixed Bed Reactor for Direct Dimethyl Ether Production from Syngas Using Differential Evolution Algorithm by Vakili, Reza and Eslamloueyan, Reza
- Bubble Columns with Internals: A Review by Youssef, Ahmed A./ Al-Dahhan, Muthanna H. and Dudukovic, Milorad P.
- A Review of the Water Gas Shift Reaction Kinetics by Smith R J, Byron/ Loganathan, Muruganandam and Shantha, Murthy Shekhar
- Conversion of Glycerol into Value-Added Products Over Cu–Ni Catalyst Supported on γ-Al2O3 and Activated Carbon by Pudi, Satyanarayana Murty/ Mondal, Tarak/ Biswas, Prakash/ Biswas, Shalini and Sinha, Shishir
Effect of Operating Conditions for Higher Alcohols Synthesis from Synthesis Gas over Alkali-Modified Co-Rh-Mo Trimetallic Catalyst Supported on Multi-Walled Carbon Nanotubes
Citation Information: International Journal of Chemical Reactor Engineering. Volume 9, Issue 1, ISSN (Online) 1542-6580, DOI: 10.1515/1542-6580.2697, July 2011
- Published Online:
The effects of operating conditions on the higher alcohols synthesis reaction from synthesis gas were studied in a single-pass tubular downflow fixed-bed reactor, using sulfided K-promoted trimetallic Co-Rh-Mo catalyst supported on multi-walled carbon nanotubes (MWCNTs). The p CO conversion increased monotonically with increasing reaction temperature (from 275 to 350°C) and pressure (from 800 to 1400 psi), while decreasing monotonically with increasing GHSV (from 2.4 to 4.2 m3 (STP)/(kg of cat./h)). To maximize the ethanol STY and selectivity, the optimum operating conditions were determined as 330°C, 1320 psi, and 3.8 m3 (STP)/kg of cat./h). Maximum ethanol STY and selectivity were obtained using gas with H2 to CO molar ratio around 1.25.
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