scholarly journals Influence of process conditions on the physicochemical characteristics of cumaru (Amburana cearensis) powder produced by spray drying

2013 ◽  
Vol 23 (1) ◽  
pp. 132-137 ◽  
Author(s):  
Sandra M. Araruna ◽  
Aline H. Silva ◽  
Kirley M. Canuto ◽  
Edilberto R. Silveira ◽  
Luzia Kalyne A.M. Leal
2013 ◽  
Vol 23 (1) ◽  
pp. 132-137 ◽  
Author(s):  
Sandra M. Araruna ◽  
Aline H. Silva ◽  
Kirley M. Canuto ◽  
Edilberto R. Silveira ◽  
Luzia Kalyne A. M. Leal

2020 ◽  
Vol 859 ◽  
pp. 301-306
Author(s):  
Nattakanwadee Khumpirapang ◽  
Supreeya Srituptim ◽  
Worawut Kriangkrai

Garlic exerts its pharmacological activities; antihyperglycemic, antihyperlipidemia, antihypercholesterolemic, and antihypertensive activity. Therefore, the aim of this study was to determine and optimize the influence of the individual and interactive effect of process conditions variables on the yield of garlic extract powders by three factors and three level-Box-Behnken design under response surface methodology. Spray drying processes the transformation of a garlic juice extract into a dried powder, where usually maltodextrin (MD) as a drying agent is used. According to experimental design, the mixing of garlic juice extract (85 – 95 %w/w) and MD (5 – 15 %w/w) were dried at an air inlet temperature 110°C - 150°C and liquid feed flow rate 5 – 35 rpm. The optimum spray-drying process conditions which maximized the yield of garlic extract powder (31%w/w) were found as follows: air inlet temperature of 150°C, the liquid feed flow rate of 16 rpm, and 5 %w/w MD. The experimental values slightly closed to the corresponding predicted values. Hence, the developed model was adequate and possible to use.


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.


2007 ◽  
Vol 55 (26) ◽  
pp. 11044-11051 ◽  
Author(s):  
Stephan Drusch ◽  
Yvonne Serfert ◽  
Matteo Scampicchio ◽  
Benjamin Schmidt-Hansberg ◽  
Karin Schwarz

2012 ◽  
Vol 554-556 ◽  
pp. 934-937
Author(s):  
Jian Yu ◽  
Xiang Hong Li ◽  
Yong Le Liu ◽  
Chi Ling Li

The objective of this work was to study the influence of some process conditions on the microencapsulation of Gualou seed oil by spray drying. The results showed that the best parameters of microencapsulation were as follows: the ratio of arabic gum to maltodextrin was 1:1, and that of core material to wall material was 2:3; and the total solids content was 25%. The optimum spray drying conditions were that the air temperature of inlet was 180 °C, and that of outlet was 80 °C; the homogenizing pressure was 35MPa. The maximum microencapsulation efficiency was 86±0.95%.


2007 ◽  
Vol 534-536 ◽  
pp. 133-136 ◽  
Author(s):  
Byoung Kee Kim ◽  
Yong Jin Kim ◽  
Jin Chun Kim

Ni59Zr20Ti16Si2Sn3 bulk metallic glass (BMG) powders were produced by a gas atomization process, and ductile Cu powders were coated on the Ni-based BMG powders using a spray drying process in order to increase the ductility. Characteristics of the as-prepared powders with the atomization and spray drying process conditions were investigated. The atomization was conducted at 1450oC under the vacuum of 10-2 torr and the powders were mixed with water-soluble Cu nitrate. The mixture was sprayed at the temperature of 130oC to prepared initial powder. After reduction treatment, sub-micron size Cu powders were successfully coated on the surface of the atomized Ni BMG powders.


2010 ◽  
Vol 28 (4) ◽  
pp. 495-507 ◽  
Author(s):  
Banu Koc ◽  
Melike Sakin Yilmazer ◽  
Pınar Balkır ◽  
Figen Kaymak Ertekin

2020 ◽  
Vol 71 (4) ◽  
pp. 387
Author(s):  
L. Landoni ◽  
R. Alarcon ◽  
L. Vilca ◽  
N. Chasquibol ◽  
M. C. Pérez-Camino ◽  
...  

The aim of this work was to obtain sacha inchi oil (SIO) microcapsules from two different species, Plukenetia volubilis L. (SIVO) and Plukenetia huayllabambana L. (SIHO), using different biopolymers as wall materials and spray drying technology. The physicochemical characteristics such as encapsulation efficiency, particle size, morphology and oxidative stability were analyzed in order to select the best formulation that could potentially be used as an ingredient in the development of functional food. Bulk SIO and four formulations were tested for each oil ecotype, using different encapsulating agents: maltodextrin (MD), Arabic gum (AG), whey protein concentrate (WPC) and modified starch HI-CAP®-100 (H). Microcapsules made of H presented the highest oxidative stability and encapsulation efficiency compared to AG, AG:MD or AG:MD:WPC formulations.


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