Valorisation of Food Processing Wastes into High-Value Platform Chemicals: Industrial Pathways and Circular Bioeconomy Perspectives
Highlights
- Food waste can be valorized into high-value chemicals, biofuels, biopolymers, and other bio-based products through integrated biorefinery approaches.
- Cascading strategies improve resource recovery, sustainability, and circular bioeconomy outcomes.
- Techno-economic, life cycle, commercialization, and regulatory aspects are critically assessed.
- Integrated food waste biorefineries offer a sustainable pathway for waste minimization, resource efficiency, and value creation from renewable feedstocks.
- This review provides strategic guidance to support researchers, industries, and policymakers in accelerating commercialization and promoting the implementation of circular bioeconomy principles.
Abstract
1. Introduction
2. Classification and Characteristics of Food Processing Wastes (FPWs)
3. Concept of Platform Chemicals
| Feedstock Type | Conversion Process | Pretreatment (Microorganism/Enzyme/Catalyst) | Conversion Process | Platform Chemicals | References |
|---|---|---|---|---|---|
| Sugar obtained from food waste | Lactic acid fermentation | Lactobacillus sp. | - | l-lactic acid and d-lactic acid | [31] |
| Citrus peel | Dark fermentation | Escherichia coli and Clostridium species | - | Biohydrogen | [43] |
| Sweet sorghum waste | Acetone-butanol-ethanol fermentation | C. acetobutylicum | - | Biobutanol | [44] |
| Rice starch | Catalytic conversion | Pinewood sawdust-derived biochar activated by phosphoric acid | 150 °C temperature for 20 min volumetric dimethyl sulfoxide: water ratio (3:1) | Glucose (86.5 mol%) | [45] |
| Food waste collected from the students’ canteen | Two-stage enzymatic treatment | Amylase and glucoamylase | 1st stage: enzyme dosage = 150 U g(TS)−1; pH = 5.5 2nd stage: enzyme dosage = 150 U g(TS)−1; pH = 4 | Reducing sugar (204.2 g L−1) | [46] |
| Food waste collected from the university | Microbial fermentation | Bacillus sp. AM5 | 55 °C and pH 10.5 | Total volatile fatty acids (34.8 g L−1) | [47] |
| Melon rind waste | Catalytic conversion | Montmorillonite KSF clay | 180 °C temperature for 30 min volumetric tetrahydrofuran: water ratio (3:1) | Hydroxymethylfurfural (5.9% wt) | [42] |
| Food and beverage waste | Catalytic conversion | Glucoamylase conversion followed by Amberlyst 36 | 140 °C temperature for 40 min dimethyl sulfoxide: water ratio (1:1) | Hydroxymethylfurfural (71% mol%) | [47] |
| Food waste collected from the municipality | Microbial fermentation with engineered microbes | Genetically modified Yarrowia lipolytica | T = 28 °C pH = 6 | Succinic acid (54.4 gL−1) | [48] |
| Sweet potato waste | Anaerobic fermentation with engineered microbes | Genetically modified Escherichia coli | T = 37 °C; t = 48 h | Succinic acid (18.65 g L−1) | [49] |
| Simulated food waste | Mesophilic fermentation | Lactobacillus amylolyticus | T = 52 °C; pH = 5.5 | Lactic acid (0.57 g g−1) | [50] |
4. Conversion Technologies for Platform Chemical Production
4.1. Biological Processes
4.2. Thermochemical Processes
4.3. Physicochemical Methods
4.3.1. Acid–Base Hydrolysis
4.3.2. Cold Plasma-Assisted Extraction
4.3.3. Microwave-Assisted Extraction
4.3.4. Supercritical Fluid Extraction (SFE)
5. Biorefinery Approaches for Food Waste Valorisation
6. Industrial Applications of Derived Platform Chemicals
6.1. Biofuels and Energy Carriers
6.2. Bioplastics and Biodegradable Polymers
6.3. Pharmaceuticals and Nutraceuticals
6.4. Agrochemicals and Food Additives
6.5. Market Opportunities, Commercial Risks, and Competitiveness of Food Waste-Derived Platform Chemicals
6.6. Safety Considerations, Contaminant Control, and Regulatory Compliance of Food Waste-Derived Products
7. Circular Bioeconomy and Sustainability Perspectives
7.1. Resource Efficiency and Waste Minimisation
7.2. Carbon Footprint Reduction and Climate Benefits
7.3. Life Cycle Assessment (LCA) Insights
7.4. Integration with Sustainable Development Goals (SDGs)
7.5. Global Certification Frameworks and Policy Instruments for Industrial Deployment
8. Techno-Economic Analysis, Life-Cycle Assessment, and Policy Perspectives
8.1. Production Cost, Economic Feasibility, and Scalability Challenges
8.2. Feedstock Logistics and Supply-Chain Management
8.3. Market Value, Product Diversification, and Industrial Competitiveness
8.4. Energy Balance, Greenhouse-Gas Reduction, and Life-Cycle Assessment
8.5. Policy Incentives and Regulatory Frameworks
9. Challenges and Future Research Directions
9.1. Feedstock Heterogeneity and Process Optimisation
9.2. Advances in Synthetic Biology and Metabolic Engineering
9.3. Digitalisation and Smart Biorefineries
9.4. Need for Interdisciplinary and Industry–Academia Collaboration
10. Conclusions
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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| Recent Review | Focus | Scope | How the Current Review Differs |
|---|---|---|---|
| [23] | Food-waste biorefinery and circular economy | Broad discussion on the conversion of food waste into biofuels and platform chemicals | Provides a more integrated, industry-oriented roadmap that links multiple technologies and their cascading uses. |
| [24] | Circular bioeconomy and biorefineries | General biorefinery concepts across biomass streams | Focuses specifically on FPW and practical Valorisation bottlenecks |
| [25] | Urban biorefinery from food waste and sewage sludge | VFA, PHA, and biogas recovery | Covers a wide spectrum of FPW conversion routes and industrial relevance |
| [26] | Food waste valorisation technologies | Thermochemical, biochemical, and chemical routes | Emphasises cascading Valorisation and practical solutions towards development |
| [27] | Circular pathway and advanced FW Valorisation | Includes thermochemical, biological, and green extraction | Highlights high-value products along with different conversion methodologies, with their industrial case linkage |
| Food Waste | Category of Waste | Origin of Waste | Production (MMT) |
|---|---|---|---|
| Citrus and banana peels | Vegetables | Fruit and vegetable processing plant, Starch manufacturers | 114.1–124.7 |
| Fish waste | Animal | Marine industry, fish processing plants | 2 |
| Waste cooking oil | Animal and vegetable | Vegetable processing plant, distilleries, fish and egg processing plants | 4.5 |
| Dairy product | Animal | Milk processing industry | 275 |
| Main Product | Feedstock | Conversion Methodology | Conversion Efficiency (%) | References |
|---|---|---|---|---|
| Micro- and nano-cellulose fibers | Walnut shells | Cold Plasma-Assisted Extraction | ~22–26% | [65] |
| Cellulose | Saccharum officinarum | cold plasma | 60.88% | [66] |
| Hexose and pentose sugars | Corncob | Microwave-assisted | 61.2% and 60.24% | [68] |
| Biopolymer (Polyhydroxyalkanoates, PHA) | Organic fraction of municipal solid waste | Acedogenic fermentation | 114.4 g kg−1 | [73] |
| Reducing sugar | Food waste | Two-stage enzymatic hydrolysis | 204.2 g L−1 | [74] |
| Methane | Anaerobic digestion-integrated with gasification | 557–680 mL g−1 | ||
| Biooil | Banana peel waste | Pyrolysis, 500 °C, 20 min | 18–28% | [75] |
| Volatile fatty acids | Food waste | Fermentation | 649 g kg−1 | [76] |
| Methane | Municipal food waste | Anaerobic digestion | 285.7 mL g−1 | [77] |
| Biogas and biopolymer (Polyhydroxyalkanoates) | Urban food waste | Acidogenic fermentation | 76 g kg−1 PHA and 0.44–0.51 m3 | [78] |
| Parameters | Fermentation | Anaerobic Digestion | Pyrolysis | Gasification | Hydrothermal Liquefaction (HTL) | Acid/Base Hydrolysis |
|---|---|---|---|---|---|---|
| Primary product | Bioethanol, biohydrogen, VFAs | Biomethane, digestate | Biooil, biochar, syngas | Syngas (H2 and CO) | Biocrude oil | Fermentable sugars |
| Energy yield | 42% ethanol | 90% energy recovery | 52% biooil yield | 1.2 m3/kg syngas | 47–52% biocrude; 68–71% energy recovery | 86.8% sugar conversion |
| Carbon conversion | Variable (13–27% H2 efficiency) | High (76.7% vs. removal) | 52.3% | 63.6% | 65–67% | ~87% |
| Advantages | Low energy input with low temperature and atmospheric pressure | Highest environmental benefit with low carbon emissions, with high energy recovery | Fast process and works with diverse waste streams | Highest hydrogen fraction with lowest operation costs | Ideal for wet biomass with the highest biocrude yield | Highest sugar conversion efficiency |
| Limitations | Downstream processing is required | Long retention time required | High capital cost. | A very high temperature is required. | High pressure is required. | No final energy product is synthesised. |
| Platform Chemical | Feedstock Source | Conversion Process | Industrial Application | Commercial/Industrial Example | References |
|---|---|---|---|---|---|
| Ethanol | Fruit waste, lignocellulosic biomass | Enzymatic hydrolysis + fermentation (S. cerevisiae) | Biofuel, fuel blending | Beta Renewables (Italy)—40,000 tons/year | [103,104,105] |
| Biogas (Methane) | Mixed food waste | Anaerobic digestion | Electricity, heat, fuel | Germany biogas plants (>9000 units) | [91,99,106] |
| Lactic Acid | Starch-rich food waste | Lactic acid fermentation | PLA bioplastics, pharmaceuticals | NatureWorks LLC (>150,000 tons/year PLA) | [19,107,108] |
| Succinic Acid | Agro-industrial residues | Microbial fermentation (A. succinogenes) | PBS bioplastics, solvents | Reverdia (DSM-Roquette) | [92,109,110,111] |
| Citric Acid | Molasses, fruit waste | Fermentation (Aspergillus niger) | Food additive, pharmaceuticals | Global production > 2.5 million tons/year | [112,113,114] |
| Furfural | Hemicellulosic biomass | Acid hydrolysis | Resins, solvents, fuels | China (the largest producer globally) | [112,115,116] |
| Volatile Fatty Acids (VFAs) | Food waste slurry | Acidogenic fermentation | Feed additives, biofertilizers | Used in EU waste Valorisation plants | [93,117,118] |
| Pectin | Citrus peel waste | Acid extraction | Food, pharmaceuticals | Citrus processing industries (Brazil, USA) | [119,120,121] |
| Product | Petrochemical Counterpart | Major Opportunity | Key Commercial Risk | Industrial Example |
|---|---|---|---|---|
| Bioethanol | Gasoline | Renewable fuel mandates | Dependence on crude oil prices | Beta Renewables (Rivalta Scrivia, Italy) |
| PLA | Polyethene (PE) | Demand for biodegradable packaging | Higher production costs | NatureWorks (Ingeo®) (Plymouth, MN, USA) |
| PHA | Polypropylene (PP) | Complete biodegradability | Limited economies of scale | Pilot municipal biorefineries |
| Succinic acid | Maleic anhydride derivatives | Green polymer production | Expensive purification processes | Reverdia (DSM–Roquette) (Delft, The Netherlands) |
| Citric acid | Synthetic acidulants | Strong food and pharmaceutical demand | Feedstock price variability | Aspergillus niger fermentation industry |
| Biogas | Natural gas | Carbon-neutral energy generation | Feedstock logistics and storage | Decentralised Indian biogas plants |
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Maity, S.; Pal, P.; Singh, A.K.; Prakash, A.; Kondratowicz-Maciejewska, K.; Prus, P.; Sarangi, P.K. Valorisation of Food Processing Wastes into High-Value Platform Chemicals: Industrial Pathways and Circular Bioeconomy Perspectives. Resources 2026, 15, 98. https://doi.org/10.3390/resources15080098
Maity S, Pal P, Singh AK, Prakash A, Kondratowicz-Maciejewska K, Prus P, Sarangi PK. Valorisation of Food Processing Wastes into High-Value Platform Chemicals: Industrial Pathways and Circular Bioeconomy Perspectives. Resources. 2026; 15(8):98. https://doi.org/10.3390/resources15080098
Chicago/Turabian StyleMaity, Sudatta, Priti Pal, Akhilesh Kumar Singh, Anand Prakash, Krystyna Kondratowicz-Maciejewska, Piotr Prus, and Prakash Kumar Sarangi. 2026. "Valorisation of Food Processing Wastes into High-Value Platform Chemicals: Industrial Pathways and Circular Bioeconomy Perspectives" Resources 15, no. 8: 98. https://doi.org/10.3390/resources15080098
APA StyleMaity, S., Pal, P., Singh, A. K., Prakash, A., Kondratowicz-Maciejewska, K., Prus, P., & Sarangi, P. K. (2026). Valorisation of Food Processing Wastes into High-Value Platform Chemicals: Industrial Pathways and Circular Bioeconomy Perspectives. Resources, 15(8), 98. https://doi.org/10.3390/resources15080098

