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Food by-products can be modified by extrusion processing. However, the impact of thermal and mechanical stress, respectively, on the structure and thus functional properties of dietary fiber-rich food by-products is still unknown. In the extrusion process, thermal and mechanical stress are coupled, not constant, and difficult to measure or calculate. Thus, their influence on structural changes and functional properties cannot be evaluated separately. In this work, a specific shear cell, denoted by closed cavity rheometer, was used to treat apple pomace with defined thermal and/or mechanical stress. Dietary fiber composition and fiber polysaccharide structures appeared to be more susceptible to high temperatures than mechanical stress. With increasing temperature (and mechanical stress) soluble and low-molecular-weight soluble dietary fiber contents increased, whereas insoluble fiber contents decreased. Arabinans as rhamnogalacturonan type I polysaccharides and galacturonic acid containing pectic polysaccharides were identified as being most susceptible to degradation under these conditions. Furthermore, the defined treatment affected the functional properties. Although changes in the water solubility index (WSI) and/or the water absorption index (WAI) were not detected up to 90 °C, WSI and WAI decreased significantly at a treatment temperature of 120 °C. However, at very high temperatures (160 °C), WSI and WAI increased. The application of shear and longer treatment times resulted in higher WSI values and complex viscosities as compared to low shear stress. [ABSTRACT FROM AUTHOR]

The goal of this study was to investigate the changes in oil droplet size in whey protein–stabilized emulsions during the atomization and the subsequent drying step of a spray drying process. For this purpose, experiments were performed in an atomization rig and a pilot spray dryer with two commercial pressure swirl atomizers. By comparing the oil droplet size before atomization, after atomization, and after spray drying, the changes in oil droplet size during each process step were quantified. The effect of oil droplet breakup during atomization was isolated by atomizing emulsions with 1 wt.% oil content and a protein to oil concentration ratio of 0.1. At 100 bar, the Sauter mean diameter of oil droplet size was reduced from 3.13 to 0.61 μm. Directly after breakup, coalescence of the oil droplets was observed for emulsions with a high oil content of 30 wt.%, leading to a droplet size after atomization of 1.15 μm. Increasing the protein to oil concentration ratio to 0.2 reduced coalescence during atomization and oil droplets with a mean diameter of 0.92 μm were obtained. Further coalescence was observed during the drying step: for an oil content of 30 wt.% and a protein to oil concentration ratio of 0.1 the mean droplet size increased to 1.77 μm. Powders produced at high oil contents showed a strong tendency to clump. Comparable effects were observed for a spray drying process with a different nozzle at 250 bar. The results confirm that droplet breakup and coalescence during atomization and coalescence during drying have to be taken into consideration when targeting specific oil droplet sizes in the product. This is relevant for product design in spray drying applications, in which the oil droplet size in the powder or after its redispersion determines product quality and stability. [ABSTRACT FROM AUTHOR]

Abstract: Micro-particle image velocimetry was used as an optical, non-intrusive measurement method to measure the flow pattern and visualise droplet deformation in high-pressure homogenisation disruption units of two different inlet designs (sharp-edged and conical). The flow patterns were compared either at same Reynolds numbers (Re=980) or pressure differences (Δp=52bar) each, to describe the influence of inlet geometry on the droplet disruption efficiency. Therefore, the shear and elongation rates were calculated from the velocity profiles and discussed regarding the visualised deformation of the emulsion droplets. For this, the viscosity ratio between the droplet and continuous phase was varied. Afterwards, the droplet size distributions (DSD) of emulsions with corresponding viscosity ratio passing the sharp-edged and the conical orifice were characterised. The inlet geometry influenced the flow pattern, shear and elongation rate profile, droplet deformation and finally droplet size distributions during the high-pressure homogenisation. On the one hand, sharp-edged inlet design resulted in higher axial velocity profiles and smaller droplets with slightly bimodal character. On the other hand, conical inlet design resulted in perfectly monomodal DSD but comparatively bigger droplets.Graphical abstract: [ABSTRACT FROM AUTHOR]