Md. Masud Alam
Senior scientific officer
Spices Research Center, Bangladesh Agricultural Research Institute, Shibganj, Bogura
Md. Nazrul Islam
Professor
Department of Food Technology and Rural Industries, Bangladesh Agricultural University, Mymensingh
Vitamin C, Food stability, Onion, Drying, Temperature
Spices Research Centre, BARI, Bogura
Postharvest and Agro-processing
Ten gram sample was blended and homogenized in a blender with 3% metaphosporic acid solution. The homogenized liquid was transferred to a 100 ml volumetric flask and adjusted 100 ml with metaphos-phoric acid solution. Content of the flask was then thoroughly mixed and filtered. Then 5 ml of the ali-quot was taken in a flask and titrated with 2-6 dichlorophenol indophenol dye. The dye had been stan-dardized with vitamin C solution to find an equivalent dye factor. The ascorbic acid content of the samples was calculated from the following formula (Rangana, 1986).
mg vitamin C/ 100g = TDV1 / V2W ×100------------------------------------------ (i)
Where,
T= Titre
D= Dye factor
V1 = Volume made up
V2 = Aliquot of extract taken for estimation
W = Weight of sample taken for estimation
Analysis of experimental data
According to Heldman (1974), any reaction which is typical in nature will occur at a rate dependent upon several factors, whether the reaction is the conversion of sucrose to glucose and fructose or the rate at which some component (such as vitamin C or thiamin) of a food is reduced in concentration by heat. The rate of the reaction is indicated by a rate constant (k) and can be described by the following general equation:
dc /- dt = KC m.................................................. (ii)
Where C represents the component concentration at any time (t) and m represents the order of reaction. Although many reactions may be of zero order, the first order reaction is described by the following equation is common in food products:
dc /- dt=KC ............................................. (iii)
In this particular type of reaction, the reaction rate is directly proportional to the concentration of the reacting substance (c). The application of a first order reaction equation is more evident if the equation (iii) is solved and expressed in the following form (Heldman, 1974):
ln C /Co = –Kt
ln C = ln Co –Kt............................................................................................. (iv)
Diffusion co-efficient and activation energy for diffusion of water during drying are available for a number of products. In general, the relationship between the diffusion co-efficient and product temperature can be represented by the Arrhenius type of equation (Heldman, 1974).
Bull. Inst. Trop. Agr., Kyushu Univ., 38: 39-46, 2015
Journal