1997
DOI: 10.3136/fsti9596t9798.3.10
|View full text |Cite
|
Sign up to set email alerts
|

Kinetic Model for Soybean Oil Hydrogenation Using Loop Reactor.

Abstract: A kinetic model including isomerization of fatty acids for soybean oil hydrogenation considering the adsorption of fatty acids on the catalyst surface affecting the hydrogenation rate has been evaluated in this study. The hydrogenation of soybean oil was conducted in a 12 1 Ioop reactor equipped with a venturi nozzle. A reduced nickel catalyst was adopted. The hydrogenation experiment was carried out an experimental design with respect to reaction temperature, flow rate of catalyst-oil mixture, hydrogen pressu… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
1

Citation Types

0
1
0

Year Published

2018
2018
2018
2018

Publication Types

Select...
1

Relationship

0
1

Authors

Journals

citations
Cited by 1 publication
(1 citation statement)
references
References 10 publications
0
1
0
Order By: Relevance
“…There are few models to describe the reactor performance during the hydrotreating of vegetable oils. The first models were focused on the hydrogenation of unsaturated compounds present in bio-oils. Velez established a conceptual industrial reactor design for hydrotreatment based on experiments with refined, bleached, and deodorized palm oil (RBDPO) by studying two cases on avoiding hot spots higher than 370 °C to control excessive product cracking and considering the flow as ideal. The molar balance equation for compound i considers the temperature and liquid residence time by the kinetic model presented in Table and does not take into account any mass-transfer effect. …”
Section: Modeling Of Catalytic Reactors For Bio-oil Conversionmentioning
confidence: 99%
“…There are few models to describe the reactor performance during the hydrotreating of vegetable oils. The first models were focused on the hydrogenation of unsaturated compounds present in bio-oils. Velez established a conceptual industrial reactor design for hydrotreatment based on experiments with refined, bleached, and deodorized palm oil (RBDPO) by studying two cases on avoiding hot spots higher than 370 °C to control excessive product cracking and considering the flow as ideal. The molar balance equation for compound i considers the temperature and liquid residence time by the kinetic model presented in Table and does not take into account any mass-transfer effect. …”
Section: Modeling Of Catalytic Reactors For Bio-oil Conversionmentioning
confidence: 99%