Skip to main content
. 2020 Jan 21;117(5):2326–2331. doi: 10.1073/pnas.1912690117

Fig. 4.

Fig. 4.

(A) The viscosity of E. coli suspensions measured with a gap H=500μm at a shear rate γ0.04s1, as a function of volume fraction, normalized to the viscosity of the buffer η0(cserine)=(0.87+2.7×104cserine) cP, with cserine the concentration of serine in mM used to prepare the solutions. The gray area defines the presence of large-scale collective motion, observed above ϕc0.75% (vertical dashed line), as characterized in IL. (BG) Examples of velocity profiles measured by using rheoimaging in cone-plate geometry of bacterial suspensions at progressively higher volume fraction ϕ, as indicated, and for γ0.04s1 and H=170μm. (H) SD σ of ΔVx(z)=Vx(z)γappz over the entire z range, with the applied shear rate γapp=Vx(zcone)/zcone, as a function of volume fraction. Open and filled symbols indicate linear and nonlinear flow profile, respectively, for H=100μm (red), 170μm (black; each symbol corresponds to an independent experimental campaign), and 200μm (blue). Gray area defines the linear flow range based on an arbitrary threshold of σ0.43. (I and J) Examples of velocity vector fields from PIV at two ϕ below (I) and above (J) ϕc0.75%. Image width is 700μm. (K) Velocity correlation functions c(r) calculated from Eq. 5 and averaged over 5t15 min at various ϕ measured via PIV analysis of phase-contrast microscopy movies of cell suspensions in sealed capillaries with H=400μm. Error bars are ±1 SD representative of the time dependency. (L) Characteristic length l(ϕ) for which c(l,ϕ)1/e.