| Literature DB >> 35195402 |
Esra Capanoglu1, Elifsu Nemli1, Francisco Tomas-Barberan2.
Abstract
Worldwide, a huge amount of agricultural food wastes and byproducts containing valuable bioactive compounds are generated, especially throughout the entire supply chain. Minimizing food wastes and byproducts is the first option to avoid environmental problems, and to help the economy and the society. Although many countries implement policies to reduce food wastes and byproducts, and different management methods are available to utilize agricultural food wastes, they are still produced annually. Nanotechnological and biotechnological approaches are recently used as novel and green applications to valorize agricultural food wastes and improve their stability and applicability. In this Review, these approaches are covered in detail with given examples. Another valorization way of consumable food waste is using it for functional food production. This Review focuses on specific examples of functional foods with food waste as an ingredient. In addition, the problems and limitations of waste management and valorization methods are investigated, considering future perspectives.Entities:
Keywords: agricultural byproduct; agricultural food waste; biotechnology; food application; nanotechnology; waste management; waste valorization
Mesh:
Year: 2022 PMID: 35195402 PMCID: PMC9204820 DOI: 10.1021/acs.jafc.1c07104
Source DB: PubMed Journal: J Agric Food Chem ISSN: 0021-8561 Impact factor: 5.895
Figure 1Impacts of agricultural food wastes and byproducts.
Examples of Extraction Methods and Extracted Valuable Compounds from Agricultural Food Wastes and Byproducts
| agricultural food waste/byproduct | extraction method | optimal conditions of the extraction methods providing the best yield | extracted valuable compounds | ref(s) |
|---|---|---|---|---|
| kiwi juice pomace | microwave-assisted extraction with different conditions | optimal conditions for extraction at a microwave power of 400 W and pressure of 350 psi → solvent composition: 50% ethanol:water, solid-to-solvent ratio: 1:15 at 75 °C for 15 min | bioactive compounds based on | ( |
| optimized extract ( | ||||
| pistachio hard shells | extraction with different solvents/microwave-assisted extraction | optimal conditions for microwave-assisted extraction → using EtOH at 1000 W for 270 s | bioactive compounds
based on | ( |
| the highest bioactive compounds in the microwave-assisted
extract: | ||||
| extract by microwave-assisted
extraction at optimum conditions
( | ||||
| tomato processing waste | ultrasound-assisted extraction/conventional organic solvent extraction | optimal conditions for ultrasound-assisted extraction → solvent: hexane:acetone:ethanol (2:1:1 v/v/v) including 0.05% (w/v) butylated hydroxy toluene (BHT), solid liquid ratio (1:35 w/v) at 15 °C, 90 W for 30 or 15 min | ( | |
| pulp of hot pepper paste | ultrasound-assisted extraction/maceration extraction | optimal conditions for ultrasound-assisted extraction → 60% amplitude and 60 °C for 5 min | higher amount of | ( |
| optimal condition for maceration extraction for 8 h → 50 °C | content of the extract by maceration extraction at optimal
conditions ( | |||
| content
of the extract by ultrasound-assisted extraction at
optimal conditions ( | ||||
| beetroot waste | pressurized liquid extraction (at 40 °C and 7.5, 10, and 12.5 MPa for 90 min, flow rate of 3 mL min–1) | optimal conditions for pressurized liquid extraction at 40 °C for 90 min → the mixture of ethanol:water 70/30 at 10 MPa | the highest global yield of extract from leaves (36.0% w/w) with pressurized liquid extraction under optimum conditions | ( |
| extract from leaves with pressurized liquid
extraction at optimum
conditions ( | ||||
| bioactive compounds (the
most abundantly detected phenolic
compounds: | ||||
| grape pomace | ultrasound-assisted extraction/microwave-assisted extraction | optimal conditions for microwave-assisted extraction → with 2% citric acid at 1000 W for 10 min | bioactive compounds (the recoveryof | ( |
| sesame bran | enzyme-assisted extraction/ultrasound-assisted extraction/ultrasound-assisted enzymatic extraction | optimal conditions for ultrasound-assisted enzymatic extraction → pH (9.8), and 1.248 AU (Anson unit)/100 g enzyme concentration at 836 W, 43 °C for 98 min | ( | |
| the highest protein yield, total phenolic content, and antioxidant capacities with ultrasound-assisted enzymatic extraction under optimum conditions | ||||
| coffee husk | supercritical CO2 extraction | optimal conditions for supercritical CO2 extraction → solvent to raw material mass ratio: 197 kg CO2/kg husks at 373 K and 300 bar | ( | |
| pumpkin seeds | ultrasound-assisted three-phase partitioning extraction | optimal conditions for ultrasound-assisted
three-phase
partitioning extraction → (NH4)2SO4 addition:30 g/100 mL, a | ( | |
| fatty acid composition of extracted oil ( | ||||
| rice bran | conventional organic solvent-based Soxhlet extraction/subcritical CO2 Soxhlet extraction | optimal conditions for subcritical CO2 Soxhlet extraction → solvent-to-feed ratio: 24:1 at 68–70 bar and 27–29 °C | ( | |
| nearly 10 times more thermolabile compounds, such
as | ||||
| wheat bran | ultrasound-assisted enzymatic extraction | optimal conditions for ultrasound-assisted enzymatic extraction → raw material concentration: 50 g/L, enzyme dose: 4.5 g/L, at 180 W, 50 °C for 70 min | ( | |
| green plantain peels | wet extraction | optimal conditions for wet extraction → 5% w/v ascorbic acid concentration | ( | |
| increase in starch yield with increase in antioxidant concentration whereas no significant effect of immersion time on final yield | ||||
| broccoli stalk | extraction with 0.1 M nitric acid | optimal conditions for extraction with 0.1 M nitric acid → liquid-to-solid ratio of 25 (v/w), 30 min | extracted | ( |
| 75% | ||||
| pectic fraction of extract (yield 18%) | ||||
| watermelon rind | microwave-assisted extraction with different acid solutions (for 15 min at 39.9 W) | optimal conditions for microwave-assisted extraction → 1 N sulfuric acid for 15 min at 39.9 W | ( | |
| banana peels | extraction with 0.5 N hydrochloric acid/citric acid (at 90 °C for 1, 2, 3, 4 h) | optimal conditions for extraction → 0.5 N HCl at 90 °C for 4 h | ( | |
| characteristics of extracted pectin from ripe banana peels
using 0.5 N HCl for 3 h (moisture content (10.00%), ash (11.15%), | ||||
| characteristics of extracted pectin from unripe banana peels
using 0.5 N HCl for 3 h (moisture content (14.13%), ash (13.83%), | ||||
| orange peels | hot-water extraction/rapid solid liquid dynamic (RSLD) extraction/microwave-assisted extraction | optimal conditions for acidic hot-water extraction → liquid-to-solid ratio (20), pH (1.5) at 70 °C for 60 min | ( | |
| extracted pectin by acidic hot-water extraction at optimum
conditions ( | ||||
| kiwi seeds | conventional Soxhlet extraction/microwave-assisted extraction/supercritical CO2 extraction/ultrasound assisted extraction/microwave integrated Soxhlet extraction | optimal conditions for ultrasound-assisted extraction
→ 10 mg seed powder in 400 mL | ( | |
| composition of extracted oil by ultrasound-assisted
extraction
at optimum conditions ( | ||||
| the presence of off-flavors in oil samples with conventional Soxhlet extraction and ultrasound-assisted extraction | ||||
| lemon peels | sequential extraction with a combination of microwave-assisted extraction and hydrodistillation and microwave-assisted extraction | optimal conditions for combination of microwave-assisted extraction and hydrodistillation → water-to-solid ratio: 0.3 mL/g, 1st step (irradiation power: 1.2 W/g for 5 min) and 2nd step (irradiation power: 0.7 W for 15 min) | ( | |
| essential oil (potent
inhibition against | ||||
| optimal conditions for microwave-assisted extraction → 80% (v/v) ethanol, 80 °C and 50 min, with a liquid-to-solid ratio of 1:10 | ||||
| yield of essential oil and pigment: ∼2 and 6 wt %, respectively | ||||
| lemon peels | conventional Soxhlet extraction/high-pressure–high-temperature extraction | optimal conditions for high-pressure–high-temperature extraction → at 150 °C for 30 min and matrix solvent ratio: 1:15 | ( | |
| citrus peels | conventional hydrodistillation/microwave-assisted hydrodistillation | optimal conditions for microwave-assisted hydrodistillation at constant pressure (300 mbar), solid-to-liquid ratio (1:1.5) → 1st step (irradiated with 785 W for 5 min) and 2nd step (irradiated with 250 W for 15 min) | ( |
Encapsulation Methods and Their Effects for Extracted Valuable Compounds from Agricultural Food Wastes
| extract | encapsulation method | wall material | encapsulation efficiency | effects of encapsulation | references |
|---|---|---|---|---|---|
| carotenoids from carrot processing waste | spray drying/freeze-drying | whey protein/maltodextrin/Inulin | freeze-drying with pure whey protein (63.69 g/100 g) | freeze-dried encapsulate ( | ( |
| spray drying with the mixture of 71 g/100 g whey protein and 29 g/100 g inulin (53.78 g/100 g) | |||||
| spray-dried encapsulate ( | |||||
| carotenoids from tomato peels | electrospinning | Zein fibers | >90% | nanoencapsulation
process ( | ( |
| encapsulated extract ( | |||||
| phenolics and carotenoids from red pepper waste | spray drying/freeze-drying | whey protein | slightly better results for freeze-drying than spray drying method | encapsulation process ( | ( |
| phenolic compounds from winemaking waste | extrusion | alginate and chitosan | between 55% and 79% | encapsulation process ( | ( |
| more suitable and efficient wall material (the mixture of alginate and chitosan at concentrations of 1% w/v and 3% w/v, respectively, and encapsulating about 80% of the extracts) | |||||
| phenolic compounds from cornsilk | spray drying/freeze-drying/microwave drying | maltodextrin | freeze-drying (99.84%) | freeze-drying with 100% maltodextrin ( | ( |
| microwave drying (99.83%) | |||||
| spray drying (99.65%) | |||||
| phenolic compounds from unused chokeberries | spray drying/co-crystallization/ionic gelation | maltodextrin/skim milk powder/whey protein/alginate/sucrose syrup | spray drying (99.6%) | spray-dried
encapsulate ( | ( |
| co-crystallization (96.3%) | |||||
| ionic gelation (94.2%) | |||||
| encapsulated
extracts ( | encapsulated extracts ( | ||||
| phenolic compounds from golden apple and red grape pomace | nanoemulsification | chitosan/soy protein | nanoemulsification with soy protein (95%) | encapsulation process ( | ( |
| nanoemulsification with chitosan (75%) | |||||
| carotenoids and phenolic compounds from sweet potato peels | spray drying/freeze-drying | whey protein | spray drying for carotenoids and phenolics (60.0% and 61.9%, respectively) | encapsulation process ( | ( |
| freeze-drying for carotenoids and phenolics (9.34% and 64.3%, respectively) | |||||
| spray
drying ( | |||||
| blueberry residue | ionotropic gelation | sodium alginate | - | encapsulation process
(67.01% | ( |
| bioactive compounds from lemon byproducts | spray drying/freeze-drying | maltodextrin/soybean protein/ ι-carrageenan | freeze-drying with the mixture of maltodextrin and soybean protein (more efficient technique than spray drying) | encapsulation process ( | ( |
| freeze-dried encapsulate ( | |||||
| bioactive compounds from beetroot pomace | freeze-drying | soy protein | 86.14% | encapsulation process ( | ( |
| encapsulated extracts
( |
Effects of Fermentation on the Bioactive Compounds from Agricultural Food Waste/Byproducts
| agricultural food waste/byproduct | fermentation method | microorganisms | effects of fermentation | reference |
|---|---|---|---|---|
| mango seeds | solid-state fermentation | ( | ||
| practical method
for | ||||
| apricot pomace | solid-state fermentation | ( | ||
| plum fruit ( | solid-state fermentation | ( | ||
| spent coffee grounds | solid-state fermentation | ( | ||
| spent coffee grounds | fermentation | ( | ||
| tomato seed meal extract | fermentation | ( | ||
| peanut press cake | solid-state fermentation | ( | ||
| Jussara pulp | ( | |||
| the main bioconversion products from anthocyanins → protocatechuic acid | ||||
| rice bran | solid-state fermentation | ( | ||
| phenolic extract
from fermented rice bran → |
Agricultural Food Wastes and by-Products As Natural Food Additives for Different Types of Food Products
| functional additives | food product | final product quality | reference |
|---|---|---|---|
| encapsulated bioactives from red pepper waste | yogurt | ( | |
| encapsulated bioactives from grape skin | whole wheat cocoa biscuits (with 1.2, 2.3, and 3.5% addition of encapsulated extract on dough weight) | ( | |
| reduction of phenolic content (16%) during cooking | |||
| encapsulated extract
addition level ( | |||
| free and encapsulated phenolic extract from olive leaf | full-fat mayonnaise (∼80% oil) | addition of both types of extract ( | ( |
| addition of encapsulated extract ( | |||
| enriched mayonnaise
with free or encapsulated extract ( | |||
| encapsulated black mulberry waste extract | dark chocolate | chitosan coated liposomal
powders ( | ( |
| encapsulation in liposomes ( | |||
| onion skin powder | bread | ( | |
| 2%–3% of onionskin
powder
addition ( | |||
| up to 3% of onionskin powder
addition instead of wheat flour
( | |||
| lettuce waste flour | bread | ( | |
| addition of lettuce waste flour (at least 170 g kg–1) ( | |||
| enriched
bread with 170 and 575 g kg–1 addition of lettuce flour ( | |||
| olive paste flour | durum wheat spaghetti | the | ( |
| addition of 10% olive paste flour (an | |||
| addition of transglutaminase
(0.6%) to enriched pasta with
10% olive paste flour ( | |||
| enriched spaghetti with 10% olive paste flour and
0.6% transglutaminase
( | |||
| carrot pomace powder and dushab (a traditional grape juice concentrate) | cakes | addition of carrot pomace powder and dushab ( | ( |
| addition of dushab ( | |||
| grape residue flour | grape ice cream | addition of 2% of grape residue flour ( | ( |
| apple pomace powder | stirred-type yogurt | addition of apple pomace powder (2%–3%) ( | ( |
| apple pomace powder addition into the diluted yogurt system
( | |||
| coffee pulp extract | probiotic beverage with or without kefir culture | probiotic beverage from coffee pulp extract
by steam pretreatment
with kefir culture ( | ( |