Modelling the removal of mercaptans from liquid hydrocarbon streams in structured packing columns

2008 ◽  
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C.I. Koncsag ◽  
A. Barbulescu
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X. Li ◽  
Vladimir Egorovich Zhukov ◽  
N. I. Pecherkin ◽  
O. A. Volodin ◽  
...  

2017 ◽  
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Abdulhafiz Usman ◽  
Abdullah Aitani ◽  
Sulaiman Al-Khattaf

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Abdoulaye Kane ◽  
Abdeltif Amrane ◽  
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...  

1949 ◽  
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D. J. Trevoy ◽  
H. G. Drickamer

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pp. 869-876 ◽  
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V. E. Zhukov ◽  
N. I. Pecherkin ◽  
V. Yu. Chekhovich ◽  
S. Sunder ◽  
...  

1994 ◽  
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Horacio Monella

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Haizu Zhang ◽  
...  

1938 ◽  
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C. A. Johnson ◽  
A. G. A. Piercey

The densities and compositions of both phases in the methane-n-heptane solubility equilibrium have been determined at 25°, 55°, and 85 °C. at total pressures from 35 to 250 atm. The critical pressures of complete miscibility were found, and the properties of the system are discussed. The nitrogen-n-heptane system was investigated similarly at 100.9 atm. and temperatures from 25° to 115 °C. The system composed of Viking natural gas and impure heptanes was also investigated at 25 °C. The three systems, methane-pentane, -hexane, and -heptane are compared and discussed.


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