Research Trends on Valorisation of Agricultural Waste Discharged from Production of Distilled Beverages and Their Implications for a “Three-Level Valorisation System”
Abstract
:1. Introduction
2. Whisk(e)y
2.1. Bioenergy Production from Combined Draff and Pot Ale
2.2. Pretreatment to Optimise Renewable Energy Production from Draff and Pot Ale
2.3. Bioenergy Production from Draff Alone
2.4. Feed/Food
3. Tequila
3.1. Bioenergy—Pretreatment of Agave Bagasse for Increased Productivity
3.2. Optimisation of Production Systems for Renewable Energy Production from Agave Bagasse
3.3. Nanofibres and Green Composites
3.4. Chemical Production
4. Baijiu
4.1. Functional Peptides
4.2. Glutelin
4.3. Xylooligosaccharides (XOS)
4.4. Biochar
4.5. Chemical Production
5. Shochu
5.1. Bacterial Culture Medium
5.2. Electricity Generation
5.3. Functional Feed
6. Proposal of a “Three-Level Valorisation System”
7. Conclusions
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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Spirit Type | Estimated Waste Discharge | References | |
---|---|---|---|
Discharge per Litre Spirit | Annual Discharge | ||
Scotch whisky | 2.5 kg | 9 × 105 tons | [3] |
Tequila | 3.6 kg | 1 × 106 tons | [13] |
Baijiu | 3.0 kg | 2 × 107 tons | [5,6] |
Shochu | 2.0 kg | 8 × 105 tons | [14,15] |
Value-Added Products | Technologies/ Subjects | Key Findings | References |
---|---|---|---|
Bioenergy (Biomethane) | Anaerobic digestion | Four scenarios based on a whiskey plant size of 2 million L/a were assessed. The recommended scenario resulted in a biogas production containing 1.03 million m3 biomethane, corresponding to an energy yield of 10,300 MWh. It could cover 446% of the annual electricity demand and 25% of the heat demand of a traditional distillery. | [17] |
Bioenergy (Biomethane) | Anaerobic digestion | A comprehensive assessment of biogas potential was reported at nine operational distilleries. Large variation was observed from different distilleries depending on the feedstocks and the processes employed. The theoretical methane yield obtained ranged from 288 to 521 L CH4 per kg volatile solids. | [27] |
Bioenergy (Biomethane) | Anaerobic digestion | Methane production potential via anaerobic digestion was assessed, including specific methane yield, acid pretreatment and microbial analysis. The methane yield from the unprocessed by-products was 330 mL/g volatile solids from draff. | [28] |
Bioenergy (Biomethane) | Anaerobic digestion | A novel anaerobic digestion plant integrated with a pretreatment stage was designed for a whisky distillery that produces 2 million litres whiskey per annum. Compared with the conventional digesters, the proposed method achieved a 20% increase in methane yield. | [21] |
Bioenergy (Biomethane) | Anaerobic digestion | Acetoclastic methanogenesis and hydrogenotrophic methanogenesis are important pathways for biogas production under mesophilic and thermophilic anaerobic digestion plant. | [29] |
Bioenergy (biomethane) and volatile fatty acids | Anaerobic digestion | The three systems studied delivered similar methane yields which could supply up to 44% of the thermal energy demand of a distillery that produces 50 million litre of whiskey per annum. The two-phase anaerobic digestion system could provide additional valorisation opportunity due to the production of volatile fatty acid. | [30] |
Bioenergy (Biohydrogen) | Electrosynthesis | Draff and pot ale were identified as possible substrate for hydrogen production via digestion and electrolysis. | [31] |
Feed | Feasibility study | Draff and pot ale were identified as the most promising biomass to produce Insect-based salmon feed ingredients. | [32] |
Value-Added Products | Technologies/Subjects | Key Findings | References |
---|---|---|---|
Bioenergy (Biomethane and biohydrogen) | Oxidative delignification and enzymatic pretreatment | It resulted in yields 1.5 and 3.6 times (hydrogen and methane, respectively) superior to those obtained with hydrolysates of non-pretreated bagasse processed with a single enzyme. | [35] |
Bioenergy (Biohydrogen) | Detoxification pretreatment | The detoxified hydrolysate produced 33% more biohydrogen than the un-detoxified one at the optimal condition. | [36] |
Bioenergy (Biomethane) | Steam explosion pretreatment | It demonstrated steam explosion prior to anaerobic digestion could add on site output in energy recovery from agave bagasse. | [37] |
Bioenergy (Biomethane) | Comparison of pretreatment method | Biological methane potential from most hydrolysates was the same whilst difference was observed in lag phase and the methane production rates. | [38] |
Bioenergy (Biomethane) | Ionic liquid-based pretreatment | High methane generation was obtained using the hydrolysate from ionic liquid pretreated materials, 7.5 times higher when compared to that obtained without pretreatment. | [39] |
Bioenergy (Biomethane) | Hydrothermal pretreatment | The operating condition of 154 °C and 15 min achieve the maximum solubilisation of total carbohydrates. | [40] |
Bioenergy (Biomethane) | Ionic liquid pretreatment | Ionic liquid–water mixtures enhance pretreatment and anaerobic digestion of agave bagasse. | [41] |
Bioenergy (Bioethanol) | High-pressure pretreatment | It demonstrated a sustainable high pressure treatment of lignocellulosic residual biomass for ethanol production. | [42] |
Bioenergy (Biomethane) | Condition optimisation | Data reveal a acid catalyst effect, batch optimisation and stability of the semi-continuous process. | [43] |
Bioenergy (Bioethanol) | Protic ionic liquid pretreatment | Pretreatment with a biocompatible low-cost protic ionic liquid was achieved, allowing one-pot ethanol production. | [44] |
Bioenergy (Biomethane and biohydrogen) | Design of a two-stage system | The continuous hydrogen and methane production system was able to achieve equivalent to approx. 9 kJ/g bagasse, significantly increased energy recovery efficiency compared to one-stage methane production system. | [45] |
Bioenergy (Biomethane) and volatile fatty acids | Process development | Two stage continuous production was modelled and demonstrated, where maximum volatile fatty acid production in the first stage and maximum biomethane production in the second stage were defined for the first time. | [46] |
Bioenergy (Biomethane) | Continuous methane production in CSTR and UASB | The UASB reactor and the use of Cellulase 50XL can be advantageous features for future industrial application of methane production. | [47] |
Nanofibers | Organosolv treatment followed by microfluidiser | The product has high resistance to pressure, and elasticity, with a potential to be used in the elaboration of advanced materials. | [24] |
Green composites | Fibre-surface treatments | The fibre can be used as reinforcement fibres to manufacture polylactic acid-based green composites. | [48] |
Chemical | Bioconversion of lignin to PHA | Increased PHA titre was achieved by a series of biological, fermentation configuration and condition optimisation. | [49] |
Value-Added Products | Technologies/Subjects | Key Findings | References |
---|---|---|---|
Functional peptides | Extraction method development | Antioxidant peptides was obtained from Jiuzao protein hydrolysates. | [52] |
Functional peptides | Method optimisation and mechanism investigation | The optimised yield of the tetrapeptide was obtained. It could improve antioxidant capacity in vivo by activating the Nrf2/Keap1-p38/PI3K-MafK signalling pathway. | [53] |
Glutelin | Pulse electric field (PEF) assisted process | PEF can be a potential technique to extract high-quality glutelin extract from Jiuzao. | [33] |
Glutelin | Grafting of Jiuzao glutelin with pullulan | Pullulan to Jiuzao glutelin ratio was optimised. A resulting product (PJC-2) can be a potential nanostabiliser for a range of food and non-food applications. | [54] |
Glutelin | Ultrasound-stirring assisted Maillard reaction | Jiuzao glutelin conjugates was prepared and optimised between Jiuzao glutelin and carboxymethyl chitosan, leading to improved functional property of Jiuzao glutelin. | [55] |
Glutelin | Maillard reaction | Jiuzao glutelin was grafted with dextran, gum arabic, and pectin via Maillard reaction, respectively, leading to improved stability. | [56] |
Xylooligosaccharides | Autohydrolysis with a recombinant thermostable, xylanases (XynAS) | Combining autohydrolysis with the xylanases (XynAS) to produce xylooligosaccharides was achieved with maximum yield of 30.4%. | [6] |
Xylooligosaccharides | Autohydrolysis with a recombinant thermostable, xylanases, namely XynAR | A similar to above process was developed to produce xylooligosaccharides, by autohydrolysis coupled with enzymatic hydrolysis (XynAR), with a yield of 34.2%. | [57] |
Biochar | Potassium assisted pyrolysis | A novel potassium enriched biochar was developed as a controlled-release potassium fertiliser. | [8] |
Biochar | Wet-process phosphoric acid and subsequent solid-phase pyrolysis | The biochar materials displayed dual functions including sustained release of multiple nutrients and potential to remove chromium. | [58] |
Biochar | Controlled synthesis of biochar | A low-cost activated biochar was prepared from Jiuzao, used for turbidity removal in low alcoholic baijiu. | [59] |
Chemical | Anaerobic fermentation | Jiuzao was used to produce ester of caproic acid using shallow pit mud as an inoculum in anaerobic fermentation. | [5] |
Value-Added Products | Technologies/Subjects | Key Findings | References |
---|---|---|---|
Bacterial culture medium | Growing trials | Sweet potato based Shochu waste was an excellent culture medium for Escherichia coli K-12. | [62] |
Bacterial culture medium | Growing trials | Rice based shochu waste could provide culture nutrient to selected photosynthetic bacteria. The resulting Kuma PSB promoted the growth of various vegetables. | [63] |
Electricity | Cassette-electrode microbial fuel cells | Electricity generation from sweet potato based shochu waste was demonstrated. | [14] |
Electricity | Stacked microbial fuel cells | Barley based shochu waste was utilised to generate electricity. | [64] |
Electricity | Material treatment and characterisation | Shochu waste-derived activated carbon is a promising ingredient as the electrode active material of electric double-layer capacitors. | [67] |
Functional feed | Feeding trials | Barley based Shochu waste improved pork meat quality by reducing stress. | [65] |
Functional feed | Feeding trials | Sweet potato based Shochu waste could be used as a potential live feed enrichment media for larviculture of Japanese flounder. | [66] |
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Stewart, K.; Willoughby, N.; Zhuang, S. Research Trends on Valorisation of Agricultural Waste Discharged from Production of Distilled Beverages and Their Implications for a “Three-Level Valorisation System”. Sustainability 2024, 16, 6847. https://doi.org/10.3390/su16166847
Stewart K, Willoughby N, Zhuang S. Research Trends on Valorisation of Agricultural Waste Discharged from Production of Distilled Beverages and Their Implications for a “Three-Level Valorisation System”. Sustainability. 2024; 16(16):6847. https://doi.org/10.3390/su16166847
Chicago/Turabian StyleStewart, Kelly, Nik Willoughby, and Shiwen Zhuang. 2024. "Research Trends on Valorisation of Agricultural Waste Discharged from Production of Distilled Beverages and Their Implications for a “Three-Level Valorisation System”" Sustainability 16, no. 16: 6847. https://doi.org/10.3390/su16166847
APA StyleStewart, K., Willoughby, N., & Zhuang, S. (2024). Research Trends on Valorisation of Agricultural Waste Discharged from Production of Distilled Beverages and Their Implications for a “Three-Level Valorisation System”. Sustainability, 16(16), 6847. https://doi.org/10.3390/su16166847