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2
Chemical and Process Engineering
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2012
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2011
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Islam A.
2
Kabadi V.
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Zavvadi A.
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Universal liquid mixture model for vapor-liquid and liquid-liquid equilibria in hexane-butanol-water system over the temperature range 10 - 100 °C
100%
Islam A.
,
Kabadi V.
Chemical and Process Engineering
|
2011
|
issue
2
2
Full text local access
Analysis of Partition Coefficients of Ternary Liquid-Liquid Equilibrium Systems and Finding Consistency Using Uniquac Model
81%
Islam A.
,
Zavvadi A.
,
Kabadi V.
Chemical and Process Engineering
|
2012
|
issue
2
Page
/ 1
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