کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
234915 465620 2016 8 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Particle Image Velocimetry (PIV) in food powders during Vacuum-Steam-Vacuum (VSV) treatment
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
پیش نمایش صفحه اول مقاله
Particle Image Velocimetry (PIV) in food powders during Vacuum-Steam-Vacuum (VSV) treatment
چکیده انگلیسی


• Non-intrusive particle image velocimetry during countercurrent fluidization
• Characterization of non-stationary, non-uniform flow patterns during VSV treatment
• Formation of loosely-bound clusters under free fall in partial vacuum
• A physical characterization of particle and fluid dynamics
• Particle Image Velocimetry coupled with Digital Image Analysis

Fluidization of solid particles has become the state of the art technique, facilitating powder handling and processing. The case of non–stationary fluidization during a Vacuum–Steam–Vacuum (VSV) treatment of conventional milk powder was investigated. Thereby, the food material is fluidized in a free fall under partial vacuum conditions. Microbiological decontamination is achieved through a short injection of saturated steam in counterflow.Particle Image Velocimetry (PIV) and Digital Image Analysis (DIA) were used for quantification and characterization of solid motion in the highly dynamic system. The non–invasive analysis revealed three distinct flow domains, which were the free fall in partial vacuum, a transient and intermediate floating state showing turbulent mixing and the final collapse of floating state due to progressed particle agglomeration. Important insight of the process were obtained. Qualitative behavior of the underlying physics of the VSV process was well characterized using the results from PIV and DIA. The gained knowledge is applicable for various powder fluidization operations involving non–stationary conditions as well as non–uniform spatial distribution of solid particles.

Particle Image Velocimetry (PIV) was used to study the solid motion under countercurrent fluidization. Intermediate, non–stationary flow patterns were described quantitatively and qualitatively in terms of characteristic settling velocity, flow profile and agglomerate size. The method was tested in Vacuum–Steam–Vacuum (VSV) treatments, involving the fluidization of conventional milk powder in free fall. The results have revealed three distinct flow domains, which are free fall under vacuum conditions, a temporary floating state during steam injection and subsequent collapse of the floating bed due to progressed particle agglomeration.Figure optionsDownload as PowerPoint slide

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Powder Technology - Volume 299, October 2016, Pages 1–8
نویسندگان
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