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Dive into the research topics where Hseen O. Baled is active.

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Featured researches published by Hseen O. Baled.


Journal of Physical Chemistry B | 2013

Effect of isomeric structures of branched cyclic hydrocarbons on densities and equation of state predictions at elevated temperatures and pressures.

Yue Wu; Babatunde A. Bamgbade; Ward A. Burgess; Deepak Tapriyal; Hseen O. Baled; Robert M. Enick; Mark A. McHugh

The cis and trans conformation of a branched cyclic hydrocarbon affects the packing and, hence, the density, exhibited by that compound. Reported here are density data for branched cyclohexane (C6) compounds including methylcyclohexane, ethylcyclohexane (ethylcC6), cis-1,2-dimethylcyclohexane (cis-1,2), cis-1,4-dimethylcyclohexane (cis-1,4), and trans-1,4-dimethylcyclohexane (trans-1,4) determined at temperatures up to 525 K and pressures up to 275 MPa. Of the four branched C6 isomers, cis-1,2 exhibits the largest densities and the smallest densities are exhibited by trans-1,4. The densities are modeled with the Peng-Robinson (PR) equation of state (EoS), the high-temperature, high-pressure, volume-translated (HTHP VT) PREoS, and the perturbed chain, statistical associating fluid theory (PC-SAFT) EoS. Model calculations highlight the capability of these equations to account for the different densities observed for the four isomers investigated in this study. The HTHP VT-PREoS provides modest improvements over the PREoS, but neither cubic EoS is capable of accounting for the effect of isomer structural differences on the observed densities. The PC-SAFT EoS, with pure component parameters from the literature or from a group contribution method, provides improved density predictions relative to those obtained with the PREoS or HTHP VT-PREoS. However, the PC-SAFT EoS, with either set of parameters, also cannot fully account for the effect of the C6 isomer structure on the resultant density.


11TH INTERNATIONAL CONFERENCE OF NUMERICAL ANALYSIS AND APPLIED MATHEMATICS 2013: ICNAAM 2013 | 2013

Equation of state density models for hydrocarbons in ultradeep reservoirs at extreme temperature and pressure conditions

Yue Wu; Babatunde A. Bamgbade; Ward A. Burgess; Deepak Tapriyal; Hseen O. Baled; Robert M. Enick; Mark A. McHugh

The necessity of exploring ultradeep reservoirs requires the accurate prediction of hydrocarbon density data at extreme temperatures and pressures. In this study, three equations of state (EoS) models, Peng-Robinson (PR), high-temperature high-pressure volume-translated PR (HTHP VT-PR), and perturbed-chain statistical associating fluid theory (PC-SAFT) EoS are used to predict the density data for hydrocarbons in ultradeep reservoirs at temperatures to 523 K and pressures to 275 MPa. The calculated values are compared with experimental data. The results show that the HTHP VT-PR EoS and PC-SAFT EoS always perform better than the regular PR EoS for all the investigated hydrocarbons.


Journal of Supercritical Fluids | 2010

Equation of state modeling of high-pressure, high-temperature hydrocarbon density data

Kun Liu; Yue Wu; Mark A. McHugh; Hseen O. Baled; Robert M. Enick; Bryan D. Morreale


Fluid Phase Equilibria | 2012

Prediction of hydrocarbon densities at extreme conditions using volume-translated SRK and PR equations of state fit to high temperature, high pressure PVT data

Hseen O. Baled; Robert M. Enick; Yue Wu; Mark A. McHugh; Ward A. Burgess; Deepak Tapriyal; Bryan D. Morreale


Fluid Phase Equilibria | 2012

Prediction of fluid density at extreme conditions using the perturbed-chain SAFT equation correlated to high temperature, high pressure density data

Ward A. Burgess; Deepak Tapriyal; Bryan D. Morreale; Yue Wu; Mark A. McHugh; Hseen O. Baled; Robert M. Enick


Fluid Phase Equilibria | 2011

Experimental measurements and equation of state modeling of liquid densities for long-chain n-alkanes at pressures to 265 MPa and temperatures to 523 K

Yue Wu; Babatunde A. Bamgbade; Kun Liu; Mark A. McHugh; Hseen O. Baled; Robert M. Enick; Ward A. Burgess; Deepak Tapriyal; Bryan D. Morreale


Fluid Phase Equilibria | 2013

Volume-translated cubic EoS and PC-SAFT density models and a free volume-based viscosity model for hydrocarbons at extreme temperature and pressure conditions☆

Ward A. Burgess; Deepak Tapriyal; Bryan D. Morreale; Yee Soong; Hseen O. Baled; Robert M. Enick; Yue Wu; Babatunde A. Bamgbade; Mark A. McHugh


International Journal of Thermophysics | 2013

Exploratory Characterization of a Perfluoropolyether Oil as a Possible Viscosity Standard at Deepwater Production Conditions of 533 K and 241 MPa

Hseen O. Baled; Deepak Tapriyal; Bryan D. Morreale; Yee Soong; Isaac K. Gamwo; Val Krukonis; Babatunde A. Bamgbade; Yue Wu; Mark A. McHugh; Ward A. Burgess; Robert M. Enick


The Journal of Chemical Thermodynamics | 2014

Viscosity of n-hexadecane, n-octadecane and n-eicosane at pressures up to 243MPa and temperatures up to 534K

Hseen O. Baled; Dazun Xing; Harrison Katz; Deepak Tapriyal; Isaac K. Gamwo; Yee Soong; Babatunde A. Bamgbade; Yue Wu; Kun Liu; Mark A. McHugh; Robert M. Enick


The Journal of Chemical Thermodynamics | 2013

Experimental density measurements of bis(2-ethylhexyl) phthalate at elevated temperatures and pressures

Babatunde A. Bamgbade; Yue Wu; Hseen O. Baled; Robert M. Enick; Ward A. Burgess; Deepak Tapriyal; Mark A. McHugh

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Babatunde A. Bamgbade

Virginia Commonwealth University

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Yue Wu

Virginia Commonwealth University

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Ward A. Burgess

United States Department of Energy

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Mark A. McHugh

Virginia Commonwealth University

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Bryan D. Morreale

United States Department of Energy

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Mark A. McHugh

Virginia Commonwealth University

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Isaac K. Gamwo

United States Department of Energy

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Kun Liu

Virginia Commonwealth University

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