Selective CO hydrogenation over bimetallic Co-Fe catalysts for the production of light paraffin hydrocarbons (C2-C4): Effect of H2/CO ratio and reaction temperature

2018 ◽  
Vol 117 ◽  
pp. 74-78 ◽  
Author(s):  
Seong Bin Jo ◽  
Ho Jin Chae ◽  
Tae Young Kim ◽  
Chul Ho Lee ◽  
Ji Un Oh ◽  
...  
Keyword(s):  
Reaction Temperature ◽  
Co Hydrogenation ◽  
Fe Catalysts

Study of K/Mn-MgO Supported Fe Catalysts with Fe(CO)5and Fe(NO3)3as Precursors for CO Hydrogenation to Light Alkenes

2013 ◽  
Vol 31 (10) ◽  
pp. 1263-1268 ◽  
Author(s):  
Liping Tang ◽  
Chengli Song ◽  
Mengli Li ◽  
Xiaolong Yang ◽  
Bin Hu
Keyword(s):  
Co Hydrogenation ◽  
Light Alkenes ◽  
Fe Catalysts

CO Hydrogenation to Light Alkenes Over Mn/Fe Catalysts Prepared by Coprecipitation and Sol-gel Methods

2005 ◽  
Vol 105 (1-2) ◽  
pp. 93-101 ◽  
Author(s):  
Chong Wang ◽  
Qingxia Wang ◽  
Xinde Sun ◽  
Longya Xu
Keyword(s):  
Co Hydrogenation ◽  
Sol Gel ◽  
Light Alkenes ◽  
Fe Catalysts

CO hydrogenation to mixed alcohols over co-precipitated Cu–Fe catalysts

2008 ◽  
Vol 9 (9) ◽  
pp. 1869-1873 ◽  
Author(s):  
Minggui Lin ◽  
Kegong Fang ◽  
Debao Li ◽  
Yuhan Sun
Keyword(s):  
Co Hydrogenation ◽  
Fe Catalysts ◽  
Mixed Alcohols

Effect of support porosity in the preparation and catalytic activity for CO hydrogenation of carbon-supported Fe catalysts

1990 ◽  
Vol 7 (2) ◽  
pp. 287-298 ◽  
Author(s):  
F. Rodriguez-Reinoso ◽  
C. Salinas-Martinez de Lecea ◽  
A. Sepulveda-Escribano ◽  
J.D. Lopez-Gonzalez
Keyword(s):  
Catalytic Activity ◽  
Co Hydrogenation ◽  
Fe Catalysts ◽  
Effect Of Support

Coke formation on HFAU and HEMT zeolites. Influence of the reaction temperature and propene pressure

1999 ◽  
Vol 96 (2) ◽  
pp. 303-318 ◽  
Author(s):  
G. A. Doka Nassionou ◽  
P. Magnoux ◽  
M. Guisnet
Keyword(s):  
Reaction Temperature ◽  
Coke Formation

EDGE AND EXAFS STUDY OF CHARCOAL SUPPORTED Pt-Fe CATALYSTS

1986 ◽  
Vol 47 (C8) ◽  
pp. C8-297-C8-300 ◽  
Author(s):  
B. MORAWECK ◽  
P. BONDOT ◽  
D. GOUPIL ◽  
P. FOUILLOUX ◽  
A. J. RENOUPREZ
Keyword(s):  
Exafs Study ◽  
Fe Catalysts

The Influence of Reaction Temperature on the Size of the Catalyst Nano-particle and the Carbon Nanotube Diameter Distributions

2008 ◽  
Author(s):  
Enkeleda Dervishi ◽  
Zhongrui Li ◽  
Fumiya Watanabe ◽  
Yang Xu ◽  
Viney Saini ◽  
...  
Keyword(s):  
Carbon Nanotube ◽  
Reaction Temperature ◽  
Nano Particle ◽  
Diameter Distributions

PEMBUATAN SURFAKTAN DARI ASAM OLEAT

2019 ◽  
Vol 1 (3) ◽  
pp. 68
Author(s):  
Puguh Setyopratomo ◽  
Edy Purwanto ◽  
H. Yefrico ◽  
H. Yefrico
Keyword(s):  
Oleic Acid ◽  
Optimum Condition ◽  
Reaction Temperature ◽  
Catalyst Concentration ◽  
Acid Number ◽  
Esterification Reaction ◽  
Number Density ◽  
Sample Analysis ◽  
Reaction Conversion ◽  
Glycerol Mono

The synthesis of glycerol mono oleic from oleic acid and glycerol is classified as an esterification reaction. This research is aimed to study the influent of reaction temperature and catalyst concentration on reaction conversion. During the experiment the temperature of reaction mixture was varied as 110 oC, 130 oC, and 150 oC, while the catalyst concentration of 1%, 3 %, and 5% was used. The batch experiment was conducted in a glass reactor equipped with termometer, agitator, and reflux condensor. The oleic acid – glycerol mol ratio of 1 : 2 was used as a mixture feed. To maintain the reaction temperature at certain level, the oil bath was used. After the temperature of reaction mixture was reached the expected value, then H2SO4 catalyst was added to the reactor.  To measure the extent of the reaction, every 30 minutes the sample was drawn out from the reactor vessel. The sample analysis include acid number, density, and viscosity measurement. From this research the optimum condition which is the temperature of reaction of 150 oC and 1% catalyst concentration was obtained. At this optimum condition the convertion reach 86% and the analysis of other physical properties of the product show the acid number of 24.12, the density of 0.922 g/cc, and the viscosity of 118.4 cp.

Control of the adiabatic flow reactor by feeding the catalyst solution

1979 ◽  
Vol 44 (8) ◽  
pp. 2352-2365
Author(s):  
Josef Horák ◽  
Zina Sojková ◽  
František Jiráček
Keyword(s):  
Steady State ◽  
Constant Temperature ◽  
Reaction Temperature ◽  
Control Algorithm ◽  
Flow Reactor ◽  
Operating Temperature ◽  
Temperature Deviation ◽  
Adiabatic Flow ◽  
Dosing Frequency ◽  
Laboratory Reactor

Control algorithm of the operating temperature is described in the reactor, which is operated at constant temperature and composition of the inlet mixture. The temperature is controlled by dosing a constant volume of the catalyst solution. The dosing frequency is determined according to the reaction temperature (deviation of the temperature from the desired value and the sign of the derivative of temperature). The control algorithm has been verified experimentally for the laboratory reactor in unstable steady state.

Control of an adiabatic continuous reactor by feeding catalyst

1980 ◽  
Vol 45 (11) ◽  
pp. 2903-2918 ◽  
Author(s):  
Josef Horák ◽  
Zina Valášková ◽  
František Jiráček
Keyword(s):  
Steady State ◽  
Reaction Temperature ◽  
Continuous Reactor ◽  
Control Element ◽  
Inlet Temperature ◽  
Switching Cycle ◽  
Point Temperature ◽  
Set Point ◽  
Constant Rate ◽  
Laboratory Reactor

Algorithms have been presented, analyzed and experimentally tested to stabilize the reaction temperature at constant inlet temperature and composition of the feed by controlled dispensing of the catalyst. The information for the control element is the course of the reaction temperature. If the temperature of the reaction mixture is below the set point, the catalyst is being fed into the reactor at a constant rate. If the reaction temperature is higher the catalyst dispenser is blocked; dispensing of the catalyst is not resumed until the set point temperature has been reached again. The amount of catalyst added is a function of the duration of the switching cycle. The effect has been discussed of the form of this function on the course of the switching cycle. The results have been tested experimentally on a laboratory reactor controlled in an unstable steady state.

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