High humidity hot air impingement blanching (HHAIB) enhances drying rate and softens texture of apricot via cell wall pectin polysaccharides degradation and ultrastructure modification.

The effects of high humidity hot air impingement blanching (HHAIB) over a range of application times (30, 60, 90, and 120 s) on drying characteristics, hardness, cell wall pectin fractions contents and nanostructure, as well ultrastructure of apricot were investigated. Results showed that HHAIB reduced drying time and decreased the hardness of apricot by 20.7%-34.5% and 46.57%-71.89%, respectively. The water-soluble pectin (WSP) contents increased after blanching, while the contents of chelate-soluble pectin (CSP) and sodium-carbonate-soluble pectin (NSP) decreased significantly (P < 0.05). The hardness and drying time were found to correlate inversely with the WSP content, but positively with CSP and NSP contents. Atomic force microscopy (AFM) detection showed the decomposition and degradation of pectin fractions during blanching. Additionally, transmission electron microscopy (TEM) observation indicated that the cell wall structure was degraded and middle lamella integrity was destroyed by blanching.

Effect of high-humidity hot air impingement blanching (HHAIB) on drying and quality of red pepper (Capsicum annuum L.).

Effects of high-humidity hot air impingement blanching (HHAIB) under different times (30, 60, 90, 120, 150, 180, 210, and 240s) on drying characteristics and quality attributes of red peppers in terms of surface colour, red pigment content, microstructure and texture were investigated. Results showed that polyphenol oxidase (PPO) residual activity of the samples decreased with increasing blanching time; it was decreased to 7% after 120s. A first-order fraction model described PPO inactivation well. Suitable HHAIB time can reduce drying time extensively. Pepper surface colour was influenced by different treatments. In terms of red pigment content, there was no significant difference for blanching time under 120s, whereas over blanching (blanching time ⩾150s) can significantly reduce the red pigment content. Microstructure observations indicate that superficial micro-cracks occur, which explain, why HHAIB enhances drying rate. The firmness, hardness, and gumminess of the samples decreased with increase of HHAIB time.

A diffusion model for drying of a heat sensitive solid under multiple heat input modes.

To obtain optimal drying kinetics as well as quality of the dried product in a batch dryer, the energy required may be supplied by combining different modes of heat transfer. In this work, using potato slice as a model heat sensitive drying object, experimental studies were conducted using a batch heat pump dryer designed to permit simultaneous application of conduction and radiation heat. Four heat input schemes were compared: pure convection, radiation-coupled convection, conduction-coupled convection and radiation-conduction-coupled convection. A two-dimensional drying model was developed assuming the drying rate to be controlled by liquid water diffusion. Both drying rates and temperatures within the slab during drying under all these four heat input schemes showed good accord with measurements. Radiation-coupled convection is the recommended heat transfer scheme from the viewpoint of high drying rate and low energy consumption.

Intermittent drying of bioproducts--an overview.

Unlike the conventional practice of supplying energy for batch drying processes at a constant rate, newly developed intermittent drying processes employ time-varying heat input tailored to match the drying kinetics of the material being dried. The energy required may be supplied by combining different modes of heat transfer (e.g. convection coupled with conduction or radiation or dielectric heating simultaneously or in a pre-selected sequence) in a time-varying fashion so as to provide optimal drying kinetics as well as quality of the bioproduct. This is especially important for drying of heat-sensitive materials (such as foods, pharmaceutical, neutraceutical substances, herbs, spices and herbal medicines). Intermittent heat supply is beneficial only for materials which dry primarily in the falling rate period where internal diffusion of heat and moisture controls the overall drying rate. Periods when little or no heat is supplied for drying allow the tempering period needed for the moisture and heat to diffuse within the material. As the moisture content increases at the surface of the biomaterial during the tempering period, the rate of drying is higher when heat input is resumed. It is possible to control the heat input such that the surface temperature of the product does not exceed a pre-determined value beyond which thermal damage of the material may occur. This process results in reduction in the use of thermal energy as well as the mass of air used in convective drying. Thus, the thermal efficiency of such a process is higher. The quality of the product, as such color and ascorbic acid content, is also typically superior to that obtained with a continuous supply of heat. However, in some cases, there will be a nominal increase in drying time. In the case of microwave-assisted and heat pump drying, for example, the capital cost of the drying system can also be reduced by drying in the intermittent mode. This paper provides an overview of the basic process, selected results from experiments and mathematical models for a variety of biomaterials dried in a wide assortment of dryers. It begins with a classification of intermittent drying processes that may be applied e.g. time-varying temperature, air flow rate, operating pressure as well as heat input by different modes and in different temporal variations. The beneficial effects of improving the quality of dried bioproducts by different intermittent processes are also included and discussed.