Double use of concentrated sweet whey for growth and spray drying of probiotics: Towards maximal viability in pilot scale spray dryer

2017 ◽  
Vol 196 ◽  
pp. 11-17 ◽  
Author(s):  
Song Huang ◽  
Serge Méjean ◽  
Houem Rabah ◽  
Anne Dolivet ◽  
Yves Le Loir ◽  
...  
2010 ◽  
Vol 6 (1) ◽  
Author(s):  
Xuan-You Li ◽  
Ireneusz Zbicinski ◽  
Jing Wu

A scaling-up approach from drying of a thin layer wet material in a experimental tunnel to a pilot scale spray drying was developed through determining drying kinetics of quick evaporation process. Maltodextin was selected as solid material in solution to be dried. Critical moisture contents as a function of initial water evaporation rate (drying rate) shows that there is the same variation between the small scale test tunnel and the pilot scale spray dryer. Result of CFD modelling demonstrates that drying kinetics obtained from the small-scale tunnel could be properly applied to scale-up the spray drying process.


Author(s):  
Philip Steinbrunner ◽  
Bradley P. Marks ◽  
Elliot T. Ryser ◽  
Quincy J. Suehr ◽  
Sanghyup Jeong

Outbreaks and recalls associated with microbial contamination of powdered foods have raised concern for the safety of the spray drying process and its products. However, little research on the fate of bacteria during the spray drying process has been done, leaving much unknown about the risks of contamination in spray dryers. Therefore, quantifying the contamination levels of  Salmonella  and  Enterococcus faecium  (as a surrogate) in various locations within a pilot scale spray dryer can help illustrate the distribution of bacterial contamination, including the final product. A 10% w/w dispersion of water and soy protein isolate was mixed with tryptic soy broth containing yeast extract inoculated with  Salmonella  Enteritidis phage type 30 ( S.  Enteritidis PT30) or  E. faecium  NRRL B-2354. This dispersion was spray dried using a pilot scale tall-form co-current spray dryer at inlet air temperatures of 180, 200, or 220°C. After drying, samples of powder from 8 locations within the system were collected/surface swabbed, plated, and enumerated. Spray drying achieved 2.40-4.15 and 2.33-2.83 log reductions in concentration of  Salmonella  and  E. faecium,  respectively in the final powder product accumulated in the dryer’s collectors.  Salmonella  and  E. faecium  were found in varying concentrations in all locations within the spray dryer after a complete drying cycle. Differences in inlet air temperature between 180-220°C had no significant effect on the inactivation levels. As a surrogate,  E. faecium  was more resistant to spray drying than  Salmonella . Overall, spray drying is capable of significant bacterial reduction in the final powder product, which can be combined with other hurdle technologies. However, adequate cleaning and sanitization procedures must be taken into considerations to prevent cross-contamination.


1977 ◽  
Vol 16 (1) ◽  
pp. 12-18 ◽  
Author(s):  
E. W. Comings ◽  
Harry Higa ◽  
J. E. Myers ◽  
Henry Koffler ◽  
H. A. McLain

2003 ◽  
Vol 21 (7) ◽  
pp. 1273-1289 ◽  
Author(s):  
Athanasia M. Goula ◽  
Konstantinos G. Adamopoulos

Molecules ◽  
2021 ◽  
Vol 26 (21) ◽  
pp. 6700
Author(s):  
Jolanta Gawałek

Experiments detailing the spray drying of fruit and vegetable juices are necessary at the experimental scale in order to determine the optimum drying conditions and to select the most appropriate carriers and solution formulations for drying on the industrial scale. In this study, the spray-drying process of beetroot juice concentrate on a maltodextrin carrier was analyzed at different dryer scales: mini-laboratory (ML), semi-technical (ST), small industrial (SI), and large industrial (LI). Selected physicochemical properties of the beetroot powders that were obtained (size and microstructure of the powder particles, loose and tapped bulk density, powder flowability, moisture, water activity, violet betalain, and polyphenol content) and their drying efficiencies were determined. Spray drying with the same process parameters but at a larger scale makes it possible to obtain beetroot powders with a larger particle size, better flowability, a color that is more shifted towards red and blue, and a higher retention of violet betalain pigments and polyphenols. As the size of the spray dryer increases, the efficiency of the process expressed in powder yield also increases. To obtain a drying efficiency >90% on an industrial scale, process conditions should be selected to obtain an efficiency of a min. of 50% at the laboratory scale or 80% at the semi-technical scale. Designing the industrial process for spray dryers with a centrifugal atomization system is definitely more effective at the semi-technical scale with the same atomization system than it is at laboratory scale with a two-fluid nozzle.


Author(s):  
Duc Quang Nguyen ◽  
Sabah Mounir ◽  
Karim Allaf

AbstractThe powder mixture of gum arabic and maltodextrin was produced by spray drying. The inlet air temperature of spray dryer was varied from 160 °C to 260 °C and the maltodextrin content was varied from 0 to 50 % in the feed solution with the concentration of 42.5 % (w/v) total solids by weight. The properties of the finished product were characterized to examine the impact of changes in these operating parameters. The results showed that: the inlet air temperature had a stronger influence on the properties of finished product than the MD/GA ratio, whereas the feed rate was more clearly affected by the MD/GA ratio. Two optimal parameters obtained include MD/GA ratio equal to 0.615 and the inlet air temperature of spray dryer Te = 258 °C.


Energies ◽  
2020 ◽  
Vol 13 (21) ◽  
pp. 5622
Author(s):  
Diana L. Tinoco-Caicedo ◽  
Alexis Lozano-Medina ◽  
Ana M. Blanco-Marigorta

Instant coffee is produced worldwide by spray drying coffee extract on an industrial scale. This production process is energy intensive, 70% of the operational costs are due to energy requirements. This study aims to identify the potential for energy and cost improvements by performing a conventional and advanced exergy and exergoeconomic analysis to an industrial-scale spray drying process for the production of instant coffee, using actual operational data. The study analyzed the steam generation unit, the air and coffee extract preheater, the drying section, and the final post treatment process. The performance parameters such as exergetic efficiency, exergoeconomic factor, and avoidable investment cost rate for each individual component were determined. The overall energy and exergy efficiencies of the spray drying system are 67.6% and 30.6%, respectively. The highest rate of exergy destruction is located in the boiler, which amounts to 543 kW. However, the advanced exergoeconomic analysis shows that the highest exergy destruction cost rates are located in the spray dryer and the air heat exchanger (106.9 $/h and 60.5 $/h, respectively), of which 47.7% and 3.8%, respectively, are avoidable. Accordingly, any process improvement should focus on the exergoeconomic optimization of the spray dryer.


2018 ◽  
Vol 53 ◽  
pp. 01031 ◽  
Author(s):  
Fangyuan Cheng ◽  
Xueyong Zhou ◽  
Yanmei Liu

Spray drying is a kind of unit operation with high energy consumption and relatively low energy utilization, and the problem of low thermal efficiency has been attracted the attention by scholars at home and abroad. The factors affecting the thermal efficiency of spray dryer are analyzed. From a technical point of view, the thermal efficiency of spray dryer can be increased through the unit operation. Measurements for the reduction of energy saving of spray dryer were put forward.


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