| Flow-Focusing Microfluidic Device | A dispersed phase is hydraulically compressed by one or more continuous-phase streams until interfacial forces cause pinch-off. | Commonly produces droplets from a few micrometres to several hundred micrometres, depending on channel dimensions and flow rates. | Channel geometry, flow-rate ratio, viscosity ratio, interfacial tension, and surfactant concentration. | Monodisperse emulsions, biological assays, particle synthesis, and single-cell encapsulation. | Excellent size uniformity and precise control of droplet frequency. |
| T-Junction Microfluidic Device | A dispersed-phase stream intersects a perpendicular continuous-phase channel, where shear and pressure differences detach droplets. | Typically generates droplets in the tens-to-hundreds-of-micrometres range, with size linked to channel width and flow conditions. | Flow-rate ratio, channel width, phase viscosity, interfacial tension, and pressure drop. | Emulsion production, reaction screening, encapsulation, and laboratory-scale formulation studies. | Simple geometry, straightforward operation, and reliable droplet generation. |
| Coaxial Capillary Apparatus | Concentric capillaries introduce inner and outer fluids, enabling single or multiple emulsions through controlled breakup. | Often produces droplets from approximately 50 micrometres to the millimetre scale; nested droplets can be formed with suitable geometry. | Capillary alignment, inner and outer flow rates, fluid viscosities, wetting properties, and interfacial tension. | Core-shell particles, double emulsions, encapsulated ingredients, and controlled-release systems. | Supports complex droplet architectures and multilayer encapsulation. |
| Membrane Emulsification System | A dispersed phase is pressed through membrane pores into a continuous phase, where droplets detach at the membrane surface. | Droplet diameter is generally larger than the effective pore diameter and is commonly controlled in the micrometre range. | Membrane pore size, transmembrane pressure, cross-flow velocity, pore wetting, and surfactant level. | Food emulsions, pharmaceutical formulations, cosmetics, and scale-up research. | Gentle processing and relatively low shear compared with many high-energy emulsification methods. |
| Vibrating-Orifice Apparatus | A liquid jet exits through an orifice and is periodically disturbed so that it breaks into droplets at a controlled frequency. | Usually suited to droplets from tens of micrometres to several millimetres, depending on orifice size and operating conditions. | Orifice diameter, liquid flow rate, vibration frequency, fluid viscosity, and surface tension. | Particle production, bead formation, laboratory dispensing, and encapsulation processes. | Highly regular droplet timing and good control over jet breakup. |
| Electrospray Droplet Generator | An electric field pulls liquid into a charged cone-jet, which disintegrates into fine droplets as electrical forces overcome surface tension. | Can produce droplets from submicrometre dimensions to tens of micrometres, depending on electrical and fluid properties. | Applied voltage, nozzle-to-collector distance, flow rate, conductivity, viscosity, and surface tension. | Spray drying, pharmaceutical particles, coating, mass spectrometry interfaces, and fine-particle fabrication. | Produces very small droplets with a narrow size distribution under stable cone-jet operation. |
| Drop-on-Demand Inkjet Apparatus | A thermal or piezoelectric actuator ejects individual droplets through a small nozzle when an electrical signal is applied. | Commonly generates droplets in the tens-of-micrometres range, with exact size determined by nozzle and waveform design. | Nozzle diameter, actuation waveform, pulse frequency, liquid viscosity, surface tension, and solids loading. | Digital printing, biospotting, material deposition, micro-patterning, and localized reagent delivery. | Precise digital placement with minimal material waste and on-demand operation. |