| Literature DB >> 36225212 |
Mirian Pateiro1, Márcio Vargas-Ramella1,2, Daniel Franco1,3, Adriano Gomes da Cruz4, Gökhan Zengin5, Manoj Kumar6, Kuldeep Dhama7, José M Lorenzo1,8.
Abstract
Berries are among the fruits with the highest nutritional and commercial value. This paper reviews the conventional and emerging dehydration methods most commonly used as postharvest treatment and discusses their efficacy in maintaining and/or improving the nutritional and functional qualities of dried berries. The characteristics of the conventional methods (e.g., convective drying, freeze-drying, spray-drying, osmotic dehydration), their pre-treatments, their combination, and intermittent drying, as well as their potential disadvantages are discussed. The use of emerging dehydration techniques (e.g., electromagnetic radiation drying, explosion puffing drying, heat pump drying, low-pressure superheated steam drying, microwave drying) allows to improve the quality of the dried berries compared to conventional techniques, in addition to reducing drying times, increasing drying speed and energy efficiency. Finally, the use of pre-treatments and the combination of technologies can enhance the quality of the final product as a result of the improvement in the effectiveness of the dehydration process.Entities:
Keywords: Berry; Bioactive compounds; Dehydration technology; Drying method; Fruit quality; Phenolic compounds
Year: 2022 PMID: 36225212 PMCID: PMC9550524 DOI: 10.1016/j.fochx.2022.100465
Source DB: PubMed Journal: Food Chem X ISSN: 2590-1575
Conventional and emerging dehydration methods comparison: mechanisms, advantages, disadvantages, cost benefits and practical application.
| Methods | Mechanism | Advantages | Disadvantages | Cost benefits |
|---|---|---|---|---|
| Convective drying | Hot air [1] | Easy operation and simple design [1] | Long drying times [2] with high temperatures [4] | Low cost [1] |
| Spray-drying | Hot gas [3] | Single step process [3] | High temperatures reached result in loss of bioactive compounds, and wall depositions (due to sugars and acids) in products | High size and high installation cost [5] |
| Freeze-drying | Low pressure (vacuum) and temperature with microwave [6][9] | High rehydration rateHigh quality products (bioactive compounds and vitamins retention) | Long drying time and requires pre-treatment (freezing) [8] | High cost (equipment and energy): one of the most expensive [5][7][8], cost up to 8-fold higher than conventional hot air [10] |
| Osmotic dehydration | Hypertonic solution [11] | No thermal treatment with high properties preservation [11] | High moisture in final product and berries chemical composition modification (depends on solution utilized) [11] | Low cost (energy and equipment) |
| Heat pump drying | Hot air [9] | Reduce energy, time, and temperature demand by heat recovering while dehumidify the air [9] | Thermal treatment (depends on settings) with loss of bioactive compounds (phenolics content) [12] | Low energy consumption [12]PA: high quality products when combined with other methods |
| Electromagnetic radiation drying | Microwave (MW) [15]Infrared (IR) | MW: high quality products (similar to freeze-drying with lower drying time), high energy efficiency [15]IR: quick and effective moisture reduction, simple equipment (compared to conventional) | MW: thermal treatment (bioactive compounds degradation) [15], chestnut, penetration, reflection, and refraction effect [8] | MW: low cost (compared to conventional); PA: industrial application in berries [15] |
| Explosion puffing drying | Steam or gas, and vacuum [19][24] | Saves energy and time when used as intermediate stage of dehydration [19] or with pre-treatments [24] | Thermal treatment can affect bioactive compounds content, antioxidant activity and sensorial properties of berries [19][24] | Cheaper alternative to freeze-drying |
| Low-pressure superheated drying | Steam and vacuum [5][8] | Energy efficient, better-quality product due to low temperature and low oxygen [5][8] | Few information available [8][22][23] and complex method [5] | Low cost: can reduce 50 % of energy consumption (compared to low temperature conventional methods) [8] |
[1] Bustos et al. (2018), [2] Zielinska et al. (2018), [3] Gagneten et al. (2019), [4] Qi et al. (2021), [5] Calín-Sánchez et al. (2020), [6] Zielinska et al. (2018), [7] Quispe-Fuentes et al. (2018), [8] Sun et al. (2019), [9] Figiel and Michalska (2017), [10] Téllez-Pérez et al. (2020), [11] Ghellam et al. (2021), [12] Xiong et al. (2021), [13] Tajudin, Tasirin, Ang, Rosli, & Lim (2019), [14] Taşeri et al. (2018), [15] Kumar & Karim (2019), [16] Moses et al. (2014), [17] Jiang et al. (2019), [18] Raghavi et al. (2018), [19] Chen et al. (2017), [20] Boudhrioua, Bahloul, Ben Slimen, & Kechaou (2009), [21] Marra, Zhang, & Lyng (2009), [22] Sehrawat, Nema, & Kaur (2018), [23] Kongsoontornkijkul, Ekwongsupasarn, Chiewchan, & Devahastin (2006), [24] Zou, Teng, Huang, Dai, & Wei (2013).
Fig. 1Five stages of the drying speed during dehydration. I: pre-heat; II: constant rate; III: first falling rate; IV: second falling rate; V: equilibrium drying rate. CM: Critical moisture content. EQ: Equilibrium of moisture content.
Fig. 2a) Heat pump drying: 1. Drying chamber, 2. Compression evaporator, 3. Condenser, 4. Fan rack, 5. Partition board, 6. Fresh berries, 7. Hot air flow, 8. Cooled air flow, 9. External fan; b) Radio frequency drying: 1. Drying chamber, 2. Fresh berries, 3. Conveyor belt, 4. Radio frequency shield, 5. Electrode, 6. Electromagnetic field, 7. Dehydrated berries; and c) Refractance window drying: 1. Drying chamber, 2. Fresh berries, 3. Conveyor belt, 4. Hot water flume, 5. Surrounding air (water vapor + air), 6. Exhaustor, 7. Dried berries, 8. Cooling water, 9. Water tank and heat unit, 10. Hot water pump.
Fig. 3a) Explosion puffing drying: 1. Steam generator, 2. Decompression valve, 3. Vacuum chamber, 4. Puffing chamber, 5. Vacuum pump, 6. Air compressor; b) Low-pressure superheated steam drying: 1. Steam generator, 2. Valve, 3. Steam reservoir, 4. Steam regulator, 5. Drying chamber, 6. Electric fan, 7. Vacuum pump, 8. Fresh berries, 9. Sample holder.
Dehydration effect on berries quality, bioactive compounds, and shelf life.
| Berry | Dehydration method | Effects | Reference | ||
|---|---|---|---|---|---|
| Quality | Bioactive compounds | Shelf life | |||
| Berries: raspberry ( | Convective drying (50 °C for 48 h, 65 °C for 20 h, and 130 °C for 2 h) | Intermediate conditions allowed to preserve the color. Temperature above 100 °C promote the deterioration of berry characteristics. | Increase in TPC content under intermediate drying conditions, and anthocyanin (delphinidin and cyanidin derivatives) preservation | ||
| Grape berries (white cultivar Xiangfei) | Convective drying (30 °C, 40 °C, 50 °C) | Higher temperature, higher water loss rate and therefore, higher weight loss (75 % after 5 and 30 days of treatment at 50 °C and 30 °C, respectively). High temperature dehydration favours sugar accumulation. | High temperatures favoured the accumulation of some phenols (mainly gallic acid and its derivatives), while the highest accumulation of flavonoids and proanthocyanidins was achieved when lower temperatures were used. | ||
| Strawberry | Convective drying (50 °C and 60 °C, 1.5 m/s) | ΔE was greater in strawberries dried longer (9.3 | Higher loss of TPC (60.9 % | Higher temperatures retained antioxidant activity better (74.7 % | |
| Berries: blueberries, tart cherries, strawberries, and cranberries | Convective drying (70 °C, 0.76 m/s up to 32 h) Freeze-drying Refractance window drying (samples at 88 °C for 3–4 min.) | Freeze-drying: better quality retention. Higher vitamin B retention in blueberry and cherry, and C in cherry and cranberryHot air: lesser quality retention | Freeze-dried berries: higher TPC, anthocyanin and chlorogenic acid contents. Flavonoids were also superior in strawberries. | Hot-air dried samples: Less antioxidant activity, while no significant differences were found between freeze- and refractance window drying. | |
| Blackcurrant ( | Convective drying (50 °C −90 °C, 0.8 m/s Freeze-drying (24 h at 65 Pa) Microwave-vacuum drying (120 W, 240 W, 360 W, 480 W at 4–6 kPa) Convective-microwave drying | Microwave vacuum: higher bulk density and lower porosity, darkest powder | Convective drying: lower water activity and solubility. Significant loss of antioxidant capacity | ||
| Black mulberries ( | Convective drying (70 °C, 2.5 m/s, 9 h) Freeze-drying Convective-explosion puffing drying (70 °C for 3 h, 80 °C for 5 min, −0.1 MPa and 70 °C for 3 h) Freeze-explosion puffing drying (-55 °C, 0.01 kPa for 12 h, 80 °C for 5 min, −0.1 MPa and 70 °C for 3 h) | Freeze drying: best colour (L*, a*, C*)Freeze-explosion puffing drying: best texture (hardness, crispness, rehydration ratio), colour (h*) | Freeze drying: higher anthocyanin (cyanidin-3-glucoside, cyanidin-3-rutinoside) content | Freeze drying: higher antioxidant activity | |
| Blueberries rabbiteye ( | Convective: fluidized bed dryer, air-impingement dryer and forced air dryer at 85 °C and 107 °C | Fluidized bed dryer: shorter drying time | |||
| Blueberry ( | Convective drying (60 °C − 90 °C, 1 m/s Microwave-vacuum drying (1.3 W/g, 4–6 kPa) Convective-microwave-vacuum | Convective drying produced the hardest, chewiest, and gummiest blueberries, and the most relevant changes in colour density, polymeric colour, and polymeric colour percentage. | Convective drying: higher TPC content at higher air temperatureConvective | Convective (90 °C) - microwave - vacuum: higher antioxidant capacity | |
| Blueberry juice | Convective drying (85 °C Cold plasma (1 kV, 1000 Hz, 2.0 cm, O2 0–1 %, 2–6 min | Cold plasma: better colour retention | Cold plasma: long treatments decrease anthocyanin, vitamin C and antioxidant activity, and increased TPC content. High oxygen concentration decreased vitamin C concentration, and increased TPC content | Cold plasma: | |
| Chokeberry ( | Convective drying (50–70 °C, 1.2 m/s) Freeze-drying Vacuum drying (50 °C, 100 Pa, 24 h) Microwave drying (240–480 W, 4 and 6 kPa) Convective-vacuum-microwave | Separate use of convective drying and microwave reduces the quality of the dried product, while their combination improves the quality. | Freeze-drying: higher TPC and anthocyanin content | Freeze-drying: lowest aw values, which favours dried fruit stability. Antioxidant activity preservation | |
| Chokeberry ( | Convective drying (50 °C for 24 h) Freeze (−20 °C for 24 h), Freeze-drying (24 h) Swell drying (pre-drying, DIC treatment, and post-drying) | Convective drying: higher shrinkage and dense structure. | Freezing and swell drying: preserved TPC, flavonoid, and kuromanin contents | Convective drying: lower of antioxidant activity | |
| Chokeberry ( | Convective drying (60 °C, 0.8 m/s) Freeze drying Vacuum-microwave drying (240 and 360 W, 4–6 kPa, 22 °C, 1 m/s) Convective (60 °C, 4 h) – vacuum-microwave (360 W 4 h) Osmotic dehydration (45 °C, 2 h 40 °Bx) - vacuum microwave Osmotic dehydration (45 °C, 2 h 40 °Bx) - convective (60 °C for 1.5 h min) - vacuum microwave (360 W) | Freeze drying: highest porosityVacuum-microwave | |||
| Goji berries ( | Convective drying (60 °C, 5 h) Osmotic dehydration (glycerol, maltodextrin, ascorbic acid, sodium chloride for 1 h at 55 °C) with convective (60 °C, 5 h) | Combination: drying time (2 h) decrease, bright red colour and texture improved | Combination: higher TPC content | Combination: higher antioxidant capacity and shelf life prolongation (3.3 times) | |
| Golden berry ( | Convective drying (60 °C and 80 °C) Freeze-drying Infrared drying | Convective and infrared drying degraded fiber precursors (celluloses, hemicellulose and pectin), decreasing crude fiber content.Drying increased L* (freeze-drying), and decreased a* and b* values | aw values obtained guarantee stability during shelf life.Convective | ||
| Golden berry ( | Convective (70 °C,1.5 m/s) Microwave (4–10 kPa at 120 W and 480 W) | Microwave (480 W): higher resistance to compression, brightest and smooth yellow colour | Microwave drying (480 W): higher bioactive compounds | Microwave drying (480 W): better antioxidant properties and lowest aw | |
| Maqui ( | Convective (60 °C for 4.5 h) Solar (45 °C, 40 % RH, 3 days, 18 h day light) Infrared (900 W, 60 °C, 4.5 h) Vacuum (60 °C, 0.15 bar, 4 h) | Freeze-drying: highest TPC | Freeze-drying: highest antioxidant compounds | ||
| Strawberries | Convective (70 °C) Radio frequency (20 W/g) Freeze-drying (100 Pa, −55 °C.) Microwave drying (800 W, 20 W/g) | Radio frequency: better temperature uniformity and energy efficiency | Radio frequency: greater retention of TPC, carotenoid, and anthocyanins | ||
| Strawberry ( | Convective (60–100 °C, 1–2.0 m/s) - Infrared drying (100, 200, 300 W) | Drying time and fruit color quality decreased with increased power, temperature, and velocity | The application of 300 W, 60 °C, 1.0 m/s resulted in higher TPC and anthocyanin contents | 200 W, 100 °C and 1.5 m/s: optimal to preserve nutrients | |
| Wolfberry ( | Ultrasound (120 W, 0.7 W/cm2, 10 s:10 s and 10 s:90 s) - assisted vacuum drying (40–60 °C, 100 Pa). | Conditions of 50 °C, 10 s:10 s generates minor color changes and minimal quality loss | |||
| Amelanchier berries ( | Convective drying (60 °C, 3.5 m/s, 12 h) Vacuum-microwave drying (355 W, 35 min., 2.8 kPa) Convective (PT: 60 °C, 9 h, 3.5 m/s) - vacuum-microwave (370 W, 15 min, 2.8 kPa) | Convective: higher density and lower ΔE | Vacuum-microwave: retention of bioactive compounds | Vacuum-microwave: higher antioxidant activity | |
| Andean blackberry ( | Ultrasound: 0–90 µm, sonication time 10–30 min Convective drying (40–60 °C, 3 m/s, 65 % RH) | Ultrasound increased drying rate up to 5 times | Ultrasound increased the antioxidants compounds migration to the liquid medium (useful for extraction processes). Lower vibration amplitude and time of sonication resulted in higher antioxidant activity | ||
| Cranberries ( | Osmotic PT (sucrose solution 65° Brx, 21 °C, 1: 4 for 6 h)-microwave vacuum Microwave-vacuum PT (100–800 W, up to 20 min, 5 kPa)-osmotic-microwave-vacuum (100 W, 5 kPa) | Microwave-vacuum pre-treatment (100 W) produced high-quality berries | PTs: similar TPC retention | PTs: similar antioxidant activity | |
| Gapes (white) seedless ( | Convective drying Atmospheric-pressure air plasma jet PT (500 W, 25 kHz) Chemical-soaked PT (0.5 % NaOH and 2 % ethyl oleate for 30 s at 80 ∘C) | PTs individually: Decrease in drying time by more than 20 %. Effects were not significant on color and texture. | PTs: Total phenolic content and antioxidant capacity doubled | ||
| Strawberry (TianXianZui) | Vacuum-freeze drying (−50 °C, 10 Pa, heating plate temperature of 4 °C, 20 h) Ultrahigh pressure PT (100 MPa and 5 min) Ultrasound PT (25 min, 200 W and 40 kHz) Combination ultrahigh pressure-ultrasound | Ultrahigh pressure or ultrasound: Increase a*, hardness, and cross-sectional areas of the matrix | PT individually: TPC, anthocyanin, and flavonoids increased, as well as antioxidant activity | ||
| Wolfberry ( | Cold plasma (3 L/min, 20 kHz, 750 W for 15, 30, 45, 60 s) Convective drying (65 °C, 3.0 m/s) | Cold plasma PT: drying time reduction (50 %), ΔE decrease, higher rehydration ratio and L*, a*, and b*. | Cold plasma PT: Decrease in bioactive compounds with treatment time | ||
a*: Redness; b*: Yellowness; DIC: Instant controlled pressure drop; L*: lightness; PT: pre-treatment; TPC: Total phenolic content; ΔE: Color difference.
Fig. 4Application of dehydrated berries on food processing.