𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Effect of fluidized bed drying on properties of dehydrated apples

✍ Scribed by Vrač, Nevenka ;Grüner, Matilda


Publisher
John Wiley and Sons
Year
1994
Tongue
English
Weight
413 KB
Volume
38
Category
Article
ISSN
0027-769X

No coin nor oath required. For personal study only.

✦ Synopsis


Abstract

Three sorts of apple (Idared, Golden Delicious and Jonathan) were dried in a laboratory‐type fluidized bed dryer. Apples were cleaned, cored, peeled and cut into 10 × 10 × 10 mm cubes or into slices 5 × 3 mm thick and 40 mm long. A part of the samples was dipped for 3 min prior to drying in 0.1% ascorbic acid solution. Drying temperature was 80 °C. Some physicochemical and sensory properties of fresh and dried apples were determined. Moisture content in dried samples varied between 9 and 12%. Greater quantity of water results in lower sensory characteristics. The sensory characteristics of apples were determined by a scoring system with weighed factors in a 20‐point scale. Glucose, fructose, saccharose, citric acid, malic acid and ascorbic acid levels were analysed by enzymatic methods. Contents of glucose, fructose and saccharose in dried apples were substantially unchanged compared to fresh apples. The drying process had the most influence on contents of citric and malic acids. Higher rehydration ratios were measured in spaghetti‐like sclices and in ascorbic acid treated samples. Idared had the best characteristics with regard to physicochemical and sensory results.


📜 SIMILAR VOLUMES


The effect of packing on a fluidized bed
✍ J. P. Sutherland; George Vassilatos; Hiroshi Kubota; G. L. Osberg 📂 Article 📅 1963 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 613 KB
Baffle effects on performance of catalyt
✍ Peijun Jiang; Hsiaotao Bi; Rong-Her Jean; Liang-Shih Fan 📂 Article 📅 1991 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 756 KB

Baffle effects on the performance of a catalytic circulating fluidized bed reactor were examined experimentally. The circulating fluidized bed reactor or riser was 102 mm in diameter and 6.32 m in height. Reaction was the catalytic decomposition of ozone using FCCparticles with a mean diameter of 89