Convective drying (CD) |
hot drying air |
Solids—fruits, vegetables, fruit and vegetable pomace |
Moisture exchange between the food product and the hot air flowing through the drying chamber |
Long shelf-life, simple design; Easy operation; Low cost |
High inlet gas temperature or very dry gas; Long drying time, exposure to oxidation; Generates off flavors; Crust formation on the product surface due to the high temperatures |
Food industry; Vegetable and fruit dry products; Pomace processing—functional ingredients production |
[31,37,38,39,40] |
Spray drying (SD) |
hot drying gas (usually air) |
Liquid—i.e., juices, purée, solutions, vegetable milk |
Transformation of liquid product into dry powder form in one-step processing operation |
Low moisture content and high-quality products; Long shelf-life; Similar size and shape of dried material; Continuous operation Lower cost than freeze-drying |
Might lead to bioactive compounds loss and stickiness due to the high temperature, equipment size, products with large fat content require a defat process, high installation cost |
Powder production; Microencapsulation; Production of instant powders |
[41,42,43,44] |
Freeze-drying (FD) |
|
All types of food |
Two steps process: (1) freezing the water from the raw material; (2) heating of the frozen solid to induce the moisture sublimation |
Prevents oxidation damages; Minimize chemical compounds changes; Minimal shrinkage and shift of soluble solids; Retention of volatile compounds; Maintenance of porous structure |
Very high facilities cost; Slow and expensive process |
Production of heat-sensitive compounds i.e., vitamins, microbial cultures, and antibiotics; Production of high-quality products with high final cost: exotic fruits, vegetables, soup ingredients, mushrooms, and juices |
[1,2] |
Osmotic dehydration (OD) |
sugar, salt (sodium chloride) solutions, concentrate juices, polyols solutions |
Fruits, vegetables |
Moisture reduction by immersion of the raw material in a high osmotic pressure solution → moisture transfer from the food to the solution driven by the difference in osmotic pressure |
Maintenance of the physicochemical and sensory parameters; When carried out in concentrated juices might enhance product quality |
High final moisture content; Usually needs further drying; High content of sugar or salt in the product when dehydrated in this type of solution; Difficulty in predicting final chemical composition when dehydrated in concentrated juices |
Fruit chips production; Production of dried fruits i.e., plums as a pre-treatment before further drying |
[45,46,47,48] |
Intermittent drying |
hot air, microwave power, vacuum and infrared |
Fruits, vegetables |
Intermittent microwave heating is led by applying microwave energy as sequential pulses, where power ratio has an important role in drying kinetics |
Protect bioactive compounds, color, texture; reduce the browning effects and enhance the shelf life. |
Higher power ratio can damage important compounds such as ascorbic acid. |
Plant-based food material; Fruits: kiwi, papaya, banana, guava, carrot, etc. |
[33,35,36] |