The flow of an incompressible, viscous fluid past a sphere is considered for small values of the Reynolds number. In particular the drag is found to be given by \[ D = D_s\{1+{3/8}R+{9/40}R^2(log R+γ + {5/3}log 2 - {323/360})+{27/80}R^3log R+O(R^3)\}, \] where D s is the Stokes drag, R is the Reynolds number and γ is Euler's constant.
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Chester et al. (1969) studied this question.
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