Dip-coating is known to have two dominant regimes based on substrate withdrawal rate; the advective regime or Landau-Levich regime, at high withdrawal velocities (≳500 µm s -1 for alcohols) and the convective regime at low withdrawal velocities (≲500 µm s -1 for alcohols). In the advective regime, the particle volume fraction in the meniscus is determined by viscosity, surface tension, and substrate withdrawal rate. In contrast, at slower withdrawal rates, particles are more concentrated in the meniscus relative to the bulk solution via convective flow induced by evaporative flux. Stick-slip banding is common when particle transport is predominately due to convective flow. It is often desirable to control band thickness, band-band distance, or even suppress banding, which is why evaporative particle transport must be understood. Evaporative transport (Qe) is defined as: 𝑄 𝑒 ≈ 𝑐𝑙 𝑐 𝑉 𝑒 (1) Where c is particle concentration, lc is capillary length (due to surface tension and substrate wettability), Ve is evaporation speed (due to solvent volatility, chamber and substrate temperature, and relative humidity, when evaporating water-miscible solvents). To control stick-slip patterning, the easiest solution is to increase the particle concentration. However, sometimes this is not always possible due to particle aggregation at high particle concentrations, or difficulties generating large quantities of specialty particles. In these cases, the capillary length can be changed by modifying surface tension or the hydrophobicity of the substrate. Alternatively, Ve is can be altered by changing the temperature or dispersant to a solvent with higher volatility. Typically, coatings prepared at temperatures too close to the boiling point lead to inhomogeneous and poorly reproducible depositions. High temperatures can also lead to the Bénard-Marangoni effect, where the surface tension varies due to a temperature gradient across the meniscus, leading to circular currents within the meniscus. One parameter that is conspicuously absent from the evaporative transport equation, and thus never independently examined, is solvent viscosity. But, is it true that viscosity has zero impact on particle transport? And how does viscosity impact particle distribution on the substrate?