Effect of Composition, Temperature, and Pressure on the Viscosities and Densities of Three Diesel Fuels

被引:25
|
作者
Rowane, Aaron J. [1 ,2 ]
Babu, Vikrant Mahesh [3 ]
Rokni, Houman B. [1 ,2 ]
Moore, Joshua D. [4 ]
Gavaises, Manolis [1 ]
Wensing, Michael [3 ]
Gupta, Ashutosh [4 ]
McHugh, Mark A. [5 ]
机构
[1] City Univ London, Dept Mech Engn & Aeronaut, Northampton Sq, London ECIV 0HB, England
[2] Afton Chem Ltd, London Rd, Bracknell RG12 2UW, Berks, England
[3] Freiedrich Alexander Univ Erlangen Nurnberg, Lehrstuhl Tech Thermodynam, Weichselgarten 8, D-91058 Erlangen, Germany
[4] Afton Chem Corp, 500 Spring St, Richmond, VA 23219 USA
[5] Virginia Commonwealth Univ, Dept Chem & Life Sci Engn, 601 W Main St, Richmond, VA 23284 USA
来源
基金
欧盟地平线“2020”;
关键词
EQUATION-OF-STATE; ASSOCIATING FLUID THEORY; CRUDE-OIL; THERMAL-CONDUCTIVITY; HYDROCARBON MIXTURES; RESERVOIR FLUIDS; CUBIC EQUATIONS; FRICTION THEORY; N-HEXADECANE; NATURAL-GAS;
D O I
10.1021/acs.jced.9b00652
中图分类号
O414.1 [热力学];
学科分类号
摘要
In this work, a rolling-ball viscometer/densimeter is used to measure high-pressure, high-temperature (HPHT) density and viscosity data from 298.2 to 532.6 K and pressures up to 300.0 MPa for three different diesel fuels. The densities and viscosities have combined expanded uncertainties of 0.6 and 2.5%, respectively, with a coverage factor, k = 2. Two of the diesels contain either a larger paraffinic or a larger aromatic content relative to the others and are standard engine test fuels. The third is an ultralow sulfur diesel that resembles an unfinished commercial diesel. Detailed compositional information is also reported for each diesel that provides a basis for interpreting the impact of composition on density and viscosity at high pressures. Both density and viscosity data are correlated to Tait-type equations with uncertainties of 0.6 and 4.0%, respectively. The Tait equations provide a facile means to compare observed differences in the density-pressure and viscosity-pressure profiles of the three different diesels. Density data are modeled with the perturbed-chain statistical associating fluid theory (PC-SAFT) equation of state (EoS) with pure component parameters calculated representing diesel as a single, pseudo-component only requiring average molecular weight (M-ave) and hydrogen-to-carbon ratio (R-H/C) as inputs. Viscosity data are modeled reasonably well using entropy scaling coupled with the PC-SAFT EoS and information on the diesel M-ave and R-H/C. The HPHT viscosity data are also modeled reasonably well with free volume theory with model parameters correlated to M-ave and R-H/C.
引用
收藏
页码:5529 / 5547
页数:19
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