We experimentally study drops formed from a nozzle into an immiscible, crossflowing phase. Depending on the operating conditions, drops are generated either in dripping or jetting mode. We investigate the impact of the continuous and dispersed phase velocities, dispersed phase viscosity and interfacial tension on the drop generation mode and size. We find that a dripping to jetting transition (DJT) takes place at a critical inner Weber number, function of the outer capillary and Ohnesorge numbers. Two jetting regimes occur depending on the phase velocity ratio. When the continuous phase velocity is significantly greater (resp. lower) than the dispersed phase velocity, jet narrowing (resp. widening) occurs. In jet widening, the critical inner Weber number depends little on the outer capillary number whereas in jet narrowing, it sharply decreases as the outer capillary number increases. We propose a comprehensive model to describe the DJT based on the attached drop equation of motion. The model satisfactorily predicts the DJT and the effect of the outer capillary number on the critical inner Weber number. It also well accounts for the drop diameter in jet narrowing. I. INTRODUCTION Membrane emulsification is an industrial process used to generate emulsions by forcing a dispersed phase through an inorganic, porous membrane into a continuous cross-flowing phase. 1 This process is usually operated in dripping (drop by drop) mode. The shear stress exerted by the continuous phase controls drop formation, so drag and the retaining capillary force are the main forces involved. In dripping mode, the drop diameter decreases with increasing shear stress, while remaining greater than the membrane pore size. A first estimate of the drop diameter may be given by a simple torque balance about the pore edge. 2 More recently, alternative fabrication methods based on microfluidics have appeared, such as flow-focusing and coflowing devices. These devices commonly operate in dripping or jetting (continuous jet) mode. 3-6 In jetting mode, the liquid thread breaks up by Plateau-Rayleigh instabilities. In certain operating conditions, drops much smaller than the nozzle diameter may be produced. The same trend is expected for membrane emulsification operated in jetting mode. Thus, it is of high interest to study the dripping to jetting transition (DJT) in this process. A DJT can occur if the liquid thread exiting the nozzle grows to a length comparable to its radius and if the pinch-off time is larger than the thread growth time. 7 The simplest case is the dripping faucet, where a dispersed phase flows from a nozzle into a stagnant, immiscible outer phase. Smith and Moss 8 studied mercury jets into gases and found that above a critical velocity (named the jetting velocity), the liquid exits the nozzle as a jet. They proposed an empirical expression for the jetting velocity, which can be recovered from a simple balance between the jet momentum flux and the retaining capillary force. Scheele and Meister 9 investigated the DJT for fifteen l...