Sustainable Valorization of Spent Coffee Grounds Within the Circular Economy: Innovative Applications in Food, Agriculture, Environmental, and Industrial Sectors
Abstract
1. Introduction
2. Coffee Production, Processing and Generation of By-Products
3. Ecological and Toxicological Constraints of Coffee By-Products
4. Characteristics and Chemical Composition of SCG
5. Valorization of SCG as an Additive in the Food Industry
6. Valorization of SCG in Agriculture
6.1. Valorization of SCG as Organic Fertilizer and Soil Compost
- Physical indicators. Application of SCG affects soil physical properties. For instance, reductions in bulk density and improvements in water-holding capacity have been observed, associated with increased structural stability of soil aggregates and changes in soil hydrophobicity, contributing to improved hydrological functioning [17,71,72,73]. SCG can promote macroaggregate formation and stimulate fungal development, whose polysaccharides act as binding agents. At the same time, the fine particle size of SCG can fill voids between larger soil particles, potentially reducing porosity and aeration. Although results are sometimes inconsistent due to methodological differences, SCG generally contributes to aggregate stability and enhances hydraulic properties at moderate application rates.
- Chemical indicators. SCG can increase soil organic matter (SOM) and organic carbon (SOC), including labile fractions, as well as the stability of humic substances. In addition, increased levels of essential nutrients and labile organic fractions support biochemical processes and can positively influence soil fertility [17,71,72,73]. These changes can also affect pesticide transformation and mobility and contribute to the bioremediation of contaminated soils. Soil pH may vary depending on soil type and management practices, and nutrient availability can increase for N, K, Mg, and Ca, while P, Cu, and Zn may respond differently depending on local conditions. SCG can also modify the mobility and bioavailability of potentially toxic elements, reducing the availability of metals such as Cd, Pb, or Zn, and, under certain conditions, increasing arsenic mobility.
- Biological indicators. SCG influences soil microbial communities by increasing diversity and abundance of beneficial bacteria, including plant growth-promoting rhizobacteria (PGPR) and nitrogen-fixing species. Enhanced microbial diversity is a key indicator of improved soil health, correlating with enhanced decomposition and mineralization of organic matter [17,71,72,73]. SCG can stimulate overall microbial activity and inhibit certain phytopathogens, reducing the risk of seedling damping-off or root rot. Moreover, SCG can serve as a carrier for beneficial microorganisms, such as Trichoderma, amplifying protective effects on plants. Additionally, SCG applications can reduce soil GHG emissions, contributing to decreased N2O and CO2 emissions.
6.2. Valorization of SCG as a Substrate for Edible Mushroom Cultivation
6.3. Valorization of SCG as a Substrate for Biochar Production
6.4. Valorization of SCG in Animal Feed
7. Valorization of SCGs as Adsorbent Materials for Wastewater Treatment
8. Valorization of SCG for Biofuel Production
8.1. Biogas Production from SCG
8.2. Biodiesel Production from SCG
- Single-step base-catalyzed transesterification. This is the most used method for biodiesel synthesis. The reaction occurs between alcohol (typically methanol) and triglycerides in the presence of a basic catalyst. However, this method is highly sensitive to reactant purity. The presence of water can cause saponification of esters, and free fatty acids react with the basic catalyst to form soaps, reducing process efficiency and promoting emulsion formation. These effects complicate the separation and purification of biodiesel, making this method suitable only for oils with very low free fatty acid content. This limitation highlights the importance of feedstock pre-treatment or purification prior to reaction.
- Two-step acid–base transesterification. For low-cost oils with high acidity, such as oil extracted from SCG, single-step transesterification is inefficient due to undesirable reactions between free fatty acids and basic catalysts. In such cases, a two-step approach is employed. The first stage involves acid-catalyzed esterification, converting free fatty acids into esters and thereby reducing total oil acidity. Subsequently, the pretreated oil undergoes base-catalyzed transesterification, converting the remaining triglycerides into methyl esters and glycerol. This method allows efficient utilization of high-acidity feedstocks and ensures higher biodiesel yields. Although effective, this method adds complexity and energy consumption to the process, which must be accounted for in lifecycle assessments.
- In situ transesterification. A promising alternative is in situ transesterification, in which oil extraction, esterification, and transesterification occur simultaneously. For SCG, this approach enables direct processing of the wet material, eliminating the need for drying and reducing solvent consumption and operational costs. The process produces biodiesel of comparable quality to that obtained via conventional pre-extraction methods. Typically, base catalysts are employed due to shorter reaction times and lower catalyst requirements compared to acid-catalyzed processes. While attractive for scale-up, operational stability and catalyst reuse in the in situ processes require further investigation.
8.3. Sugar Recovery and Bioethanol Production from SCG
8.4. Direct Combustion and Production of Solid Fuels from SCG
9. Valorization of SCGs in Pharmaceutical, Nutraceutical, and Biotechnological Applications
9.1. Pharmaceutical and Nutraceutical Applications of SCGs: Evidence from Preclinical Studies
9.2. Production of Lactic Acid from SCG
9.3. Production of Phenolic Compounds and Antioxidants from SCGs
10. Valorization of SCGs in the Cosmetic and Personal Care Industry
11. Valorization of SCGs in the Production of Functional and Sustainable Materials
11.1. Production of Plastics, Composites, and Bricks from SCGs
11.2. Production of Soundproofing Materials/Acoustic Panels from SCGs
11.3. Production of Electrode Materials from SCGs
12. Biorefining of SCG
13. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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| Component | Composition (%)/g/100 g Dry Matter (DM) [44] | Composition (%) [16] |
|---|---|---|
| Cellulose | 12.4 ± 0.79 | 8.6 ± 1.8 |
| Hemicellulose | 39.1 ± 1.94 (arabinose 3.6 ± 0.52; mannose 19.07 ± 0.85; galactose 16.43 ± 1.66) | 36.7 ± 5 |
| Lignin | 23.9 ± 1.7 (insoluble 17.59 ± 1.56; soluble 6.31 ± 0.37) | 0.05 ± 0.05 |
| Proteins | 17.44 ± 0.1 | 13.6 ± 3.8 |
| Nitrogen | 2.79 ± 0.1 | – |
| Ash | 1.3 ± 0.1 | – |
| Total phenolics | – | 1.5 ± 1 |
| Total sugars | – | 8.5 ± 1.2 |
| Pectic substances | – | 0.01 ± 0.005 |
| Tannins | – | 0.1 ± 0.02 |
| Chlorogenic acid | – | 2.3 ± 1 |
| Caffeine | – | 0.1 ± 0.02 |
| Cellulose | 12.4 ± 0.79 | 8.6 ± 1.8 |
| Product Type | SCG Addition (%) | Effect on Nutritional Composition | Effect on Sensory Properties | Technological/Rheological Observations | Refs. |
|---|---|---|---|---|---|
| Bread | 2, 4, 6, 8, 10 | Increased fiber, protein, and minerals; higher total carbohydrates at 2–4%; increased phenolic compounds and flavonoids | High consumer acceptance; 10% achieved the second-highest preference score | Drying is required for microbiological stability | [51,52] |
| Sponge cake | 1, 2, 3, 4, 6 | Increased fiber, minerals, and phenolic compounds; higher antioxidant activity | 2% addition had the best acceptability; 3–6% negatively affected texture and color | Aerated structure better preserved at low addition levels | [55,56] |
| Muffins | 1, 15, 16, 31, 30, 46, 61 | Increased antioxidants, phenolic compounds, caffeine, chlorogenic acid, trigonelline | Did not negatively affect overall acceptability | Can act as a functional ingredient | [57,58] |
| Biscuits | 2, 4, 6; 3.50–4.40 | Increased fiber, minerals, and amino acids; higher phenolic compounds | Good overall acceptability; color score decreased with addition | Minor rheological changes; decreased lightness, increased red component | [60,61] |
| Ice cream cones | 5, 10, 15, 20 | Increase in fiber and bioactive compounds | No significant effect on color, aroma, taste, texture, or overall acceptability | Suitable for sweet products without negative sensory impact | [62] |
| Cookies | 2–6 | Increase in fiber and antioxidants | Comparable acceptability to commercial products | Coffee aroma improved the sensory profile | [63] |
| Edible biofilms | 1–4 | Improved mechanical, antioxidant, and antimicrobial properties | – | Increased tensile strength and water resistance; polysaccharide-phenol interactions | [68] |
| Field/Subfield | Type of Valorization | Description/Benefits | Limits/Precautions | Refs. |
|---|---|---|---|---|
| Agriculture | Organic fertilizer/Compost | Enhances SOC, aggregate stability, water retention; stimulates microbial diversity, PGPR, and antioxidant activity; may reduce N2O/CO2 emissions | Raw grounds can be phytotoxic; high C/N, caffeine, and phenolics require pretreatment; dosage critical | [47,69,71,72,73,79,88,89,90,91] |
| Vermicomposting | Produces stable humus with high porosity, aeration, and nutrient content; stimulates worm biomass at 25% dose | Pure grounds reduce worm survival; mix with manure/organic residues; dose dependent | [87,92,93,94] | |
| Mushroom substrate (Pleurotus) | Supports mycelial colonization; reduces caffeine/phenolics; produces nutrient-rich biomass; eco-friendly | Growth slows >20% grounds; fruiting viable up to 20%; high phenolics inhibit development | [44,98,99,100,101] | |
| Intensive Agriculture/Environmental Applications | Biochar (slow pyrolysis) | Reduces phytotoxicity; improves soil structure, water and nutrient retention; long-term carbon sequestration; can be mineral-functionalized | Requires controlled pyrolysis; feedstock-dependent | [103,104] |
| Biochar for remediation | Filters pollutants; treats wastewater; supports catalysis; reduces contaminant mobility; porosity/C:N tunable via co-pyrolysis | Properties vary with co-pyrolysis conditions; optimization required | [105] |
| Animal/Species | SCG Inclusion (%) | Duration/Diet | Effects/Benefits | Limits/Precautions | Refs. |
|---|---|---|---|---|---|
| Dairy cattle | 5% in concentrate | – | No effect on milk yield/fat; slight protein decrease; safe in vivo | Short storage limit for wet SCG | [109] |
| Lactating goats | up to 100 g·d−1 | – | Maintains milk yield; improves antioxidant status | Dose optimization needed | [110] |
| Goats | up to 50% replacement of PKC | – | Improved digestibility, economic benefit at 25% | Higher inclusion reduces growth | [113] |
| Latxa ewes | up to 200 g·kg−1 DM | – | Reduced methane, improved milk FA profile, enhanced immune markers | Controlled levels required | [111,112] |
| Pigs | 10% | 70 days | No adverse effect on health; carcass quality maintained | 15% reduces weight gain and feed efficiency | [115] |
| 0.5% | – | No negative effect on meat quality; improved fatty acids profile in YB/YW | – | [116] | |
| Poultry/Broilers | 2.5 g·kg−1 green coffee | – | Increased feed intake, body weight, feed conversion ratio; reduced abdominal fat | – | [118] |
| 5–10% SCG | – | 5% safe, minimal impact; 10% reduces average daily gain, carcass weight | – | [117] | |
| Nile tilapia | up to 15% replacement of rice bran | 90 days | No negative effects on growth, serum biochemistry, survival | – | [119] |
| Tenebrio molitor larvae | 10–25% | – | Improved protein, vitamins A and C, polyphenols; oil quality | – | [120] |
| Biofuel | Production Process | Benefits/Advantages | Limitations/Challenges | Refs. |
|---|---|---|---|---|
| AD of wet SCG | Potential CH4 production; utilization of organic waste | Mono-digestion can inhibit the process; high lignocellulose content; pretreatment required | [134,136,137,138] | |
| Biogas | Co-digestion with other substrates (FW, AL, AS) | System stabilization; higher CH4 yields; micronutrient contribution | May inhibit fermentation; pH decrease; presence of caffeine | [135,137,138] |
| Biodiesel | Oil extraction + base/acid-base/in situ transesterification | High lipid content (10–16%); renewable source; good stability; pleasant aroma | Glycerin formation; low oxidative stability; limitations in unmodified engines; extraction costs | [141,142,146,150] |
| Bioethanol | Hydrolysis + fermentation (enzymatic or acid) | >80% sugar recovery; potential for bioethanol; co-production with biodiesel | Presence of inhibitors (caffeine, tannins); SCG variability; pretreatment required | [42,151,154] |
| Solid fuels | Direct combustion, pelletization, or briquetting; carbonization; blending with other biomass | High calorific value; low cost; waste valorization; potential to produce high-efficiency biomass pellets; enhanced energy characteristics through carbonization; compliant with ISO 17225-2 and EN 303-5 standards for certain blends | High NO2 and CO emissions; combustion optimization required; blending with other biomass may affect mechanical durability; residual moisture; further research needed for higher SCG proportions | [155,156,157,158,159,160,161] |
| Application | Target Compound/Substance | Method/Technology | Results/Effects | Quantitative Values/Observations | Refs. |
|---|---|---|---|---|---|
| Supplements and pharmaceutical products | Polyphenols (chlorogenic acid and derivatives), flavonoids | Standardized concentrated extracts | Antioxidant, anti-inflammatory, antibacterial, anticancer activities; support cellular health, energy metabolism, and blood sugar regulation | Relevant amounts of caffeoylquinic acids: 11.05–13.24 mg·g−1 (Arabica), 6.22–7.49 mg·g−1 (Robusta) | [25,61,67] |
| Dermatological products | Oils (linoleic, palmitic, stearic, oleic acids, arachidic ≤ 7%, linolenic < 5%), diterpenes (kahweol, cafestol) | Oil extraction | Moisturizes and protects the skin; anti-aging effect; PUFA/SFA ratio >1 favorable for cellular protection | Oils classified according to PUFA/SFA ratio; emollient and antioxidant properties | [25,67] |
| Lactic acid production | Carbohydrates, polysaccharides and proteins from SCGs | Chemical pretreatment + saccharification + bacterial fermentation (Lactiplantibacillus plantarum WiKim0126) | Near-theoretical yield, high purity and productivity; specific levorotatory isomer | Lactic acid concentration 22.8 g·L−1, 99.6% of theoretical yield, productivity 0.95 g·L−1·h−1, substrate 4% w/v | [175] |
| Extraction of phenolic compounds and antioxidants | Chlorogenic acid, caffeine, flavonoids | Solvents: ethanol, methanol; advanced methods: ultrasound, microwave, subcritical water, autohydrolysis, Penicillium purpurogenum GH2 fermentation, hydrothermal pretreatment | Efficient recovery of polyphenols; compounds with antioxidant activity reduce oxidative stress and protect products | Ethanol extraction efficient; advanced methods increase yield and reduce environmental impact | [42,168,173] |
| Product Type/Application | Active Compound/Ingredients | Method/Technology | Results/Effects | Quantitative Values/Observations | Refs. |
|---|---|---|---|---|---|
| Cosmetic oils (moisturizing, cleansing) | Fatty acids: palmitic, linoleic, oleic, stearic; diterpenes | Soxhlet extraction with n-hexane, room temperature maceration | Hydration, skin barrier restoration, emollient effect; skin protection and nourishment | Extraction yield: 8–16%; makeup removal efficiency 95.05 ± 3.05% for 40% oil formulations | [176,177,178,179,180] |
| Scrubs and exfoliants | Natural abrasive particles from SCGs, polyphenols, nourishing oils | Oil-in-water or water-in-oil emulsion formulation, natural emulsifiers (apricot kernel, soy lecithin, olive oil) | Gentle exfoliation, uniform particle distribution, hydration, skin compatibility | Increased stability with apricot kernel emulsifier + macadamia oil; small droplet diameters, reduced delamination | [179] |
| Biphasic and cleansing products | SCG oils, non-ionic surfactants, emollients, humectants | Incorporation into emulsions and biphasic products | High efficiency in makeup removal, maintenance of skin comfort, safety | Tested on 20 volunteers (20–22 years old), no adverse reactions | [180] |
| Hybrid exfoliating products | SCG + natural emulsifiers and nourishing oils | Stable emulsion formulation | Gentle exfoliation, hydration, skin compatibility, microplastic reduction | Stable emulsions with apricot kernel emulsifier and macadamia oil | [178] |
| Application | SCG Processing/Activation | BET Surface Area (m2·g−1) | Electrolyte/Battery Type | Electrochemical Performance | Energy/Power Density | Cycling Stability | Ref. |
|---|---|---|---|---|---|---|---|
| EDLC supercapacitor (high T) | Hydrothermal acidic hydrolysis + KOH activation (800 °C) | 2906 | PYR13–TFSI (ionic liquid) | 178 F·g−1 at 20 °C (50 A·g−1); 182–285 F·g−1 (20–120 °C) | 84 Wh·kg−1/202 kW·kg−1 | – | [195] |
| EDLC supercapacitor | KOH activation, oxidative calcination 300 °C vs. Ar annealing 600 °C | 1789/658 | – | 205 F·g−1 vs. 82 F·g−1 | – | – | [192] |
| EDLC supercapacitor | KOH activation, ultrahigh surface area | 3600 | Ionic liquid | 131 F·g−1 at 0.5 A·g−1; 96 F·g−1 at 4 A·g−1 | 52 Wh·kg−1/871 W·kg−1 | Stable over wide voltage | [193] |
| EDLC (2D PCNs + carbon blacks) | AC2500/BP2000/Super P = 100/15/5 | – | 1 M TEABF4/PC | 226.8 F·g−1 at 0.5 A·g−1 | 56.7 Wh·kg−1/750 W·kg−1 | 98% after 50,000 cycles | [194] |
| Lithium-ion battery anode | Dry milling + carbonization 800 °C | – | Li-ion | 360 mAh·g−1 (2nd cycle, 0.1 A·g−1); 285 mAh·g−1 reversible | – | ~100 cycles, 0.23% degradation/cycle | [196] |
| ZnCl2-assisted Li-ion battery anode | ZnCl2 carbonization 550 °C | – | Li-ion | 692 mAh·g−1 | – | 86% retention after 100 cycles | [197] |
| MCDI (lithium recovery) | Pyrolytic carbonization + high-T activation | 1332.4 | – | Li recovery 41.6 mg·g−1; salt adsorption 22.8 mg·g−1 | – | Stable cycling | [198] |
| Sodium-ion battery anode | Two-step thermal: 500 + 1300 °C | – | Na-ion | 140–280 mAh·g−1 | 440–490 Wh·kg−1 (full cell) | Stable rate performance | [199] |
| Sodium-ion battery | Pre-carbonization 750 °C + annealing 1100 °C | – | Na-ion | 168 mAh·g−1 | – | Improved Coulombic efficiency | [200] |
| Li–S battery | One-step pyrolysis 900 °C | – | Li–S | 340 mAh·g−1 at 0.1 C | – | Coulombic efficiency > 98% | [201] |
| Bio-battery | HCl treatment + thermal drying | – | – | Max power 0.024 W | – | Stable 52 days | [202] |
| Flexible supercapacitor | N-doping via melamine, 600 °C | – | – | 139 F·g−1 at 0.5 A·g−1 | – | >90% after 5000 cycles | [203] |
| Humidity sensor | Pyrolyzed SCG biochar, screen-printed | – | – | Impedance 25 → 12 MΩ (20–98% RH) | – | Response < 20 s | [205] |
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Ungureanu, N.; Vlăduț, N.-V. Sustainable Valorization of Spent Coffee Grounds Within the Circular Economy: Innovative Applications in Food, Agriculture, Environmental, and Industrial Sectors. Sustainability 2026, 18, 4127. https://doi.org/10.3390/su18084127
Ungureanu N, Vlăduț N-V. Sustainable Valorization of Spent Coffee Grounds Within the Circular Economy: Innovative Applications in Food, Agriculture, Environmental, and Industrial Sectors. Sustainability. 2026; 18(8):4127. https://doi.org/10.3390/su18084127
Chicago/Turabian StyleUngureanu, Nicoleta, and Nicolae-Valentin Vlăduț. 2026. "Sustainable Valorization of Spent Coffee Grounds Within the Circular Economy: Innovative Applications in Food, Agriculture, Environmental, and Industrial Sectors" Sustainability 18, no. 8: 4127. https://doi.org/10.3390/su18084127
APA StyleUngureanu, N., & Vlăduț, N.-V. (2026). Sustainable Valorization of Spent Coffee Grounds Within the Circular Economy: Innovative Applications in Food, Agriculture, Environmental, and Industrial Sectors. Sustainability, 18(8), 4127. https://doi.org/10.3390/su18084127
