Abstract

Membrane foaming is a promising alternative to conventional foaming methods to produce uniform bubbles. In this study, we provide a fundamental study of a cross-flow membrane foaming (CFMF) system to understand and control bubble formation for various process conditions and fluid properties. Observations with high spatial and temporal resolution allowed us to study bubble formation and bubble coalescence processes simultaneously. Bubble formation time and the snap-off bubble size () were primarily controlled by the continuous phase flow rate (); they decreased as increased, from 1.64 to 0.13 ms and from 125 to 49 µm. Coalescence resulted in an increase in bubble size (), which can be strongly reduced by increasing either continuous phase viscosity or protein concentration—factors that only slightly influence . Particularly, in a 2.5 wt % whey protein system, coalescence could be suppressed with a coefficient of variation below 20%. The stabilizing effect is ascribed to the convective transport of proteins and the intersection of timescales (i.e., μs to ms) of bubble formation and protein adsorption. Our study provides insights into the membrane foaming process at relevant (micro-) length and time scales and paves the way for its further development and application.

Highlights

  • Foams are widely used in our daily life such as in pharmaceuticals, cosmetics and foods

  • We study bubble formation as function of the transmembrane pressure (Ptrm)

  • Bubble formation only occurs if the transmembrane pressure exceeds the activation pressure

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Summary

Introduction

Foams are widely used in our daily life such as in pharmaceuticals, cosmetics and foods. Foams are conventionally produced and studied in high speed stirrer/mixer [1] and rotor-stator systems [2] that operate based on continuous fragmentation of larger bubbles into small bubbles. These traditional techniques are relatively easy to scale-up, but are associated with limitations, including high energy input and limited control over the bubble properties. The packed bed and membrane systems are capable of achieving high throughput, while that is not the case yet for microfluidic devices that are still in need of up-scaling

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