Accurate
computation of shear viscosity is fundamental for describing
fluid flow and designing and developing new processes. Poly-α-olefins
(PAO’s), particularly from 1-decene, have been applied to a
variety of industrial processes. Recently, these molecules have been
applied as carbon dioxide thickeners, enhancing carbon dioxide viscosity,
which is important in carbon dioxide injection, either for enhanced
oil recovery or sequestration in geological formations. For these
applications, knowledge of the pure oligomer viscosity is crucial
to design and operate the oligomer upstream pipelines before mixing
them with carbon dioxide. Using Green–Kubo formalism with equilibrium
molecular dynamics simulations, two methods are presented in the literature
to generate the traceless, symmetric pressure tensor. In this work,
we show that these two methods provide different values of shear viscosity,
from the analysis of how the diagonal components of the traceless,
symmetric pressure tensor are computed in each method. Then, we examine
the consistency and correctness of each method: one is found to be
consistent. The other is corrected by scaling the fluctuations of
the diagonal components. Shear viscosities of supercritical carbon
dioxide, vapor and liquid n-pentane, and liquid n-decane are computed to illustrate the analysis. We also
apply the consistent method to compute the viscosity of 1-decene oligomers,
including for the first time larger-than-dimer oligomers (trimer,
tetramer, hexamer, and decamer).