Experimental Quantification of Point Efficiency of Sieve Trays at Elevated Viscosity under Non-Total Reflux Conditions

Most of the data used to develop efficiency models were obtained from distillation tests under total reflux conditions. However, commercial distillation columns are generally operated in a non-total reflux mode of operation. Therefore, the current efficiency models may not be truly representative of actual efficiencies observed in the field. There is a need to develop reliable efficiency models using data on both total reflux and non-total reflux conditions. As a part of the current study, an Oldershaw column capable of operating in non-total reflux was used to measure point efficiency data for two viscous test systems: tert-amyl-alcohol/isobutanol and cyclopentanol/cyclohexanol. Results showed that the point efficiency decreased with an increase in the stripping factor and a decrease in the concentration of the light component in the feed. The effect of reflux ratio, L/V, and slope of the equilibrium curve was also studied. Important findings will be discussed along with a comparison of the point efficiency data for cyclohexane/n-heptane and the test systems used in this study.

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Publication Details

Journal
Industrial & Engineering Chemistry Research
Published
2024-10-24
DOI
https://doi.org/10.1021/acs.iecr.4c02361
Citations
2
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.37
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article

Experimental Quantification of Point Efficiency of Sieve Trays at Elevated Viscosity under Non-Total Reflux Conditions

Sayeed A. Mohammad, Izak Nieuwoudt, Clint P. Aichele, Rukhsar Ahmed et al.
2 citations
Industrial & Engineering Chemistry Research
Phase Equilibria and Thermodynamics
0.37
article

Experimental Quantification of Point Efficiency of Sieve Trays at Elevated Viscosity under Non-Total Reflux Conditions

Sayeed A. Mohammad, Izak Nieuwoudt, Clint P. Aichele, Rukhsar Ahmed, Tony Cai
article en
2 citations

Abstract

Most of the data used to develop efficiency models were obtained from distillation tests under total reflux conditions. However, commercial distillation columns are generally operated in a non-total reflux mode of operation. Therefore, the current efficiency models may not be truly representative of actual efficiencies observed in the field. There is a need to develop reliable efficiency models using data on both total reflux and non-total reflux conditions. As a part of the current study, an Oldershaw column capable of operating in non-total reflux was used to measure point efficiency data for two viscous test systems: tert-amyl-alcohol/isobutanol and cyclopentanol/cyclohexanol. Results showed that the point efficiency decreased with an increase in the stripping factor and a decrease in the concentration of the light component in the feed. The effect of reflux ratio, L/V, and slope of the equilibrium curve was also studied. Important findings will be discussed along with a comparison of the point efficiency data for cyclohexane/n-heptane and the test systems used in this study.

Industrial & Engineering Chemistry ResearchVol. 63(44)
Oklahoma State University (US), Fracture Analysis Consultants (United States) (US), Oklahoma State University Oklahoma City (US)
Openalex Percentile: Top 43%
Phase Equilibria and Thermodynamics
0.37
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