The penetration by and distribution of calcium and bisulphite ions during potato scalding and hot-air dehydration

1964 ◽  
Vol 15 (4) ◽  
pp. 253-258 ◽  
Author(s):  
D. J. McWeeny ◽  
J. P. Moody ◽  
H. S. Burton
Keyword(s):  
Hot Air ◽  
2020 ◽  
Vol 85 (4) ◽  
pp. 903-909 ◽  
Author(s):  
Shoaib Younas ◽  
Changhong Liu ◽  
Hao Qu ◽  
Yu Mao ◽  
Wei Liu ◽  
...  

1975 ◽  
Vol 41 (10) ◽  
pp. 1075-1078 ◽  
Author(s):  
Eiji NIWA ◽  
Teruo NAKAYAMA ◽  
Iwao HAMADA

2007 ◽  
Vol 79 (4) ◽  
pp. 1115-1121 ◽  
Author(s):  
Dionissios P. Margaris ◽  
Adrian-Gabriel Ghiaus

2014 ◽  
Vol 37 (2) ◽  
pp. 111-121 ◽  
Author(s):  
Bengang Wu ◽  
Haile Ma ◽  
Wenjuan Qu ◽  
Bei Wang ◽  
Xin Zhang ◽  
...  
Keyword(s):  
Hot Air ◽  

2013 ◽  
Vol 65 (1) ◽  
Author(s):  
Mohd Rozainee Taib ◽  
Ida Idayu Muhamad ◽  
Chee Loong Ngo ◽  
Pang Soon Ng

Microwave vacuum and convective hot air dehydration of jackfruit (Artocarpus Heterophyllus) bulbs were carried out to study the effects of different dehydration treatments on drying characteristics, rehydration ability and quality attributes. Jackfruit bulbs were dehydrated by microwave power output of 58, 140, 220, and 321W respectively combined with vacuum level of -65 cmHg during microwave vacuum dehydration. Convective hot air dehydration was also conducted with the hot air temperature of 60, 70, and 80°C, respectively. Microwave vacuum dehydration with microwave power output of 321 W resulted in 133 times faster in drying time compared to convective hot air dehydration with hot air temperature of 60°C. All dehydration data were subjected to Newton and Page’s equation model fitting, where Page’s equation model was well fitted for all dehydration conditions with R2 > 0.994. Furthermore, microwave vacuum dehydration produced better quality of dehydrated jackfruit bulbs with higher rehydration ability and sensory attributes.


Author(s):  
M. Al Haddad ◽  
S. Mounir ◽  
V. Sobolik ◽  
K. Allaf

Dehydration of fruits and vegetables is one of the most ancient and efficient preservation methods. The quality of the product and its cost depend mainly on the final stage of drying. In the present paper we analyze physical mechanisms occurring during drying throughout heat and mass transfer for defining an efficient and economic three stage drying process of hot air drying combined to a texturing stage by DIC (Instant Controlled Pressure Drop) and finally using microwave assisted by ambient temperature air dehydration.


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