| Literature DB >> 32875363 |
Angela Bianco1, Marilena Budroni2, Severino Zara1, Ilaria Mannazzu1, Francesco Fancello1, Giacomo Zara1.
Abstract
Brewers' spent grain (BSG) is the most abundant by-product of brewing. Due to its microbiological instability and high perishability, fresh BSG is currently disposed of as low-cost cattle feed. However, BSG is an appealing source of nutrients to obtain products with high added value through microbial-based transformation. As such, BSG could become a potential source of income for the brewery itself. While recent studies have covered the relevance of BSG chemical composition in detail, this review aims to underline the importance of microorganisms from the stabilization/contamination of fresh BSG to its biotechnological exploitation. Indeed, the evaluation of BSG-associated microorganisms, which include yeast, fungi, and bacteria, can allow their safe use and the best methods for their exploitation. This bibliographical examination is particularly focused on the role of microorganisms in BSG exploitation to (1) produce enzymes and metabolites of industrial interest, (2) supplement human and animal diets, and (3) improve soil fertility. Emerging safety issues in the use of BSG as a food and feed additive is also considered, particularly considering the presence of mycotoxins.Key points• Microorganisms are used to enhance brewers' spent grain nutritional value.• Knowledge of brewers' spent grain microbiota allows the reduction of health risks. Graphical abstract.Entities:
Keywords: Brewers’ spent grain; Microbial communities; Microbial quality; Mycotoxins; Single-cell protein; Vermicompost
Mesh:
Year: 2020 PMID: 32875363 PMCID: PMC7502439 DOI: 10.1007/s00253-020-10843-1
Source DB: PubMed Journal: Appl Microbiol Biotechnol ISSN: 0175-7598 Impact factor: 4.813
Fig. 1Scheme of the brewing process and consecutive production of brewers’ spent grain
Fig. 2Brewers’ spent grain fresh from production and after drying
Chemical composition of brewers’spent grain
| Major components | g kg−1 dry weight | Cellulose (glucan) | 3–330 |
| Hemicellulose | 192–419 | ||
| Xylan | 136–206 | ||
| Arabinan | 56–419 | ||
| Starch | 10–120 | ||
| Lignin | 115–278 | ||
| Lipids | 30–106 | ||
| Proteins | 142–310 | ||
| Ashes | 11–46 | ||
| Extractives | 58–107 | ||
| Phenolics | 7–20 | ||
| Ferulic acid | 1860–1948 | ||
| 565–794 | |||
| Minerals | mg kg−1 dry weight | Silicon | 1400–10,740 |
| Phosphorus | 4600–6000 | ||
| Calcium | 2200–3515 | ||
| Magnesium | 1900–2400 | ||
| Sulfur | 1980–2900 | ||
| Potassium | 258.1–700.0 | ||
| Sodium | 100.0–309.3 | ||
| Iron | 100.0–193.4 | ||
| Zinc | 82.1–178.0 | ||
| Aluminum | 36.0–81.2 | ||
| Manganese | 40.9–51.4 | ||
| Cobalt | 17.8 | ||
| Copper | 11.4–18.0 | ||
| Strontium | 10.4–12.7 | ||
| Iodine | 11 | ||
| Barium | 8.6–13.6 | ||
| Chromium | <0.5–5.9 | ||
| Molybdenum | 1.4 | ||
| Boron | 3.2 | ||
| Non-essential amino acids | % total protein | Histidine | 26.27 |
| Glutamic acid | 16.59 | ||
| Aspartic acid | 4.81 | ||
| Valine | 4.61 | ||
| Arginine | 4.51 | ||
| Alanine | 4.12 | ||
| Serine | 3.77 | ||
| Tyrosine | 2.57 | ||
| Glycine | 1.74 | ||
| Asparagine | 1.47 | ||
| Glutamine | 0.07 | ||
| Essential amino acids | % total protein | Lysine | 14.31 |
| Leucine | 6.12 | ||
| Phenylalanine | 4.64 | ||
| Isoleucine | 3.31 | ||
| Threonine | 0.71 | ||
| Tryptophan | 0.14 | ||
| Vitamins | ppm | Biotin | 0.1 |
| Choline | 1800 | ||
| Folic acid | 0.2 | ||
| Niacin | 44 | ||
| Phantotenic acid | 8.5 | ||
| Riboflavin | 1.5 | ||
| Thiamine | 0.7 | ||
| Pyridoxine | 0.7 |
Patents held for brewers’ spent grain
| Process for producing a filler from brewer’s spent grain (BSG), filler, use of a filler and foodstuff | US Patent Application: US-2020-0138065-A1 | A process for producing a filler from BSG. The process comprises (1) comminuting the BSG; (2) heating the BSG; (3) optionally, fermenting the BSG; (4) optionally, reducing the moisture content of the BSG; and (5) optionally, mixing the BSG with at least one flavor-modifying food additive, such as a sugar substitute(s) and/or an aroma. Also disclosed are a filler obtained or obtainable by this process, the use of such a filler, and a foodstuff comprising at least one such filler | Petry and Olwal ( | |
| Intermittent infrared drying for BSG | US Patent Application: US-105-78,358-B2 | A system for processing BSG that includes a specific intermittent infrared heating and stirring protocol designed to produce a unique dried BSG product that can be used whole or ground up and used as a quality flour suitable for human consumption | McHugh et al. ( | |
| Method for reducing moisture in BSG | US Patent Application: US-2019-0254315-A1 | A method for reducing the moisture content of BSG comprising the exposure of different BSG to infrared radiation | Willis ( | |
| Process for a prepared beverage or beverage component from BSG | US Patent Application: US-2019-0200640-A1 | A process for preparing a beverage or a component of a beverage. Enzymatic treatment of BSG with addition of one or more enzymes, with α-amylase, gluco-amylase, cellulase, xylanase, protease, and/or β-glucanase activities, and subsequent fermentation with a strain of lactic acid bacteria | Gil-Martinez and Arendt ( | |
| Spent grain fuel product and process | US Patent Application: US-10-364-400-B2 | A process of making a fuel product from BSG. After production, the dried BSG is fed into a combustion chamber of a steam boiler that is used for beer brewing, and the BSG is separated during combustion by agitation, such as spraying of the BSG in the combustion chamber | Larson et al. ( | |
| A process for microbiological stabilization of BSG, microbiologically stabilized BSG, and the use thereof | Patent Cooperation Treaty: WIPO (PCT); WO-2019-034567-A1 | A process to microbiologically stabilize the spent fresh beer beans (BSG). The process includes acidification of the BSG to a pH 4 or lower, on the basis that the BSG is acidified before reaching mycotoxin levels above the limits of reads and/or counts of colonies, not exceeding 103 CFU g−1 aerobic bacteria, fungi, yeast, mesophilic aerobic bacteria, or total anaerobic bacteria, after a week of storage at 25 °C | Gil-Martinez and Arendt ( | |
| Composition of BSG and polylactic acid | US Patent Application: US-10-285,422-B2 | A composition consisting of BSG and polylactic acid (PLA) is produced by the following steps: processing BSG; mixing BSG with PLA at a specific proportion; BSG and PLA are well mixed by a binder and then subjected to a granulation process to form plastic granules. Adding BSG to PLA can reduce the use of PLA. Furthermore, the composition of BSG and PLA and the method for making this are further used to make utensils, bottles, cans, containers, parts, and other biological plastic products, to provide added value to BSG | Chen et al. ( | |
| Composition consisting of BSG and PLA and a method for making the same | US Patent Application: US-10-201,177-B2 | This method for manufacturing a composite consisting of BSG and PLA includes the steps of: providing the raw material containing BSG; providing the raw material containing PLA; mixing the BSG with the PLA at a specific proportion; and providing a binder to enable the BSG and the PLA to be well mixed, and to maintain the desired tensile strength. A pretreatment unit includes dehydration, desiccation, drying, grinding, and sieving. The granulator includes a double screw extruder connected to a cutting machine. The double screw extruder mixes the BSG and the PLA and extrudes them into plastic bars that are then cut into plastic granules by the cutting machine | Chen et al. ( | |
| Systems and methods for making BSG dough products | US Patent Application: US-2019-0223457-A1 | The invention provides methods to produce dough and bread products made at least in part of BSG. The BSG is removed from the brewing or distilling process, dried, frozen, and then further processed into a BSG dough product. More specifically, the invention relates to the systems and methods for making frozen pizza dough balls composed at least in part of grain products from the process of brewing beer or distilling sprits, such as whiskey | Brown and Allgeier ( | |
| Process for producing protein concentrate or isolate a cellulosic thermochemical feedstock from BSG | US Patent Application: US-2018-0199593-A1 US-2018-0199594-A1 European Patent Application: WO-2018-136,235-A1, WO-2018-136,234-A1 | A process to obtain a high-value protein product and a cellulosic residue from BSG. The high-value protein product is useful as a protein supplement or as feed for livestock and poultry, and the cellulose residue has value as a raw material for a thermochemical process unit, to produce a biofuel | Mackay and Greden ( | |
| BSG-based protein powder | US Patent Application: US-2018-0014555-A1 | Production of a BSG-based protein powder and the related methods for using the powder in protein-enriched foods. The BSG-based protein powders are highly soluble and therefore easily wettable, easily dispersible, and mixable at concentrations up to 50% by weight. They can be used alone or as a protein enhancer in food for human consumption, pet food, and commercial feed | Mackay et al. ( | |
| Bio-plastic composite containing BSG and a method for making the same | US Patent Application: US-2017-0306153-A1 US-10-030-148-B2 | Method for obtaining a bioplastic composite from BSG | Chen et al. ( | |
| Integrated process for extracting proteins and arabinoxylans from BSG | Patent Cooperation Treaty: WIPO (PCT); WO-2012-069889-A1 | The present invention proposes an integrated process for extracting proteins and arabinoxylans from BSG, without the need to subject the BSG to any pre-treatment, through the use of alkaline reagents followed by selective precipitation by acidification of the medium and addition of ethanol. The present invention is applicable in the areas of re-use or exploitation of BSG, with the aim to obtain products that can be used as ingredients in the food industry, and in the production of dietetic and pharmaceutical products. The final residue obtained after extraction of the proteins and arabinoxylans can be used as a source of cellulose, as an insoluble dietetic fiber, or possibly as a fuel or raw material for the paper-making industry | Saraiva et al. ( | |
| Integrated process of filtration to dry BSG | Patent Cooperation Treaty (PCT): WO-2010-117,288-Al WO-2010-117,288-A8 | A process and the corresponding equipment, to dehydrate BSG from 85 to 15% humidity, to obtain a stabilized product with the same content of protein, fiber, and lipids. The dehydration process involves several phases, two of which are mechanical (membrane filtration, compression) and the last one of which consists of vacuum drying using hot water or low-pressure water vapor as a heat source. Energy for the process is available at no cost in the brewing industry, through the use of hot process water or low-pressure steam from cogeneration units. Dehydrated BSG is a stabilized product and can be used as food for humans and animals, ruminants, and non-ruminants, and as a raw material for biotechnological and pharmaceutical applications | De Carvalho et al. ( | |
| Process for drying BSG | US Patent Application: US-2012-0005916-A1 Patent Cooperation Treaty (PCT): WO-2010-053493-Al | A process for drying BSG, to obtain a product with a moisture content ≤ 15% by weight, biologically stable over time, with high nutritional value, commercially profitable, and environmentally safe, comprising two phases: the first is a mechanical pressing operation to reduce the initial humidity of the BSG by at least 75–80% by weight, up to a humidity < 70% by weight; the liquid obtained is transported to an effluent treatment plant; the solid obtained undergoes a second phase that consists of thermal drying, with two sub-phases: during the first, the product is transported through a stream of hot air, while during the second, it is transported by an air flow at room temperature | Lopez et al. ( |
Fig. 3Microbial exploitation of brewers’ spent grain in industrial biotechnology, agricultural processes, and human and animal diets
Worldwide mycotoxin regulations: limits and guideline for unprocessed and processed cereal in food
| Aflatoxin B1 | 2 | 10 | 10 | 5 | 15 | 0.1 | |||||||
| Aflatoxin total (B1, B2, G1, G2) | 4 | 20 | 15 | 20 | 5 | 5 | |||||||
| Ochratoxin A | 3 | 5 | 5 | 5 | 0.5 | 20 | |||||||
| Deoxynivalenol | 500 | 1000 | 1000 | 1000 | 1000 | 1000 | 1000 | 750 | |||||
| Zearalenone | 50 | 200 | 60 | 400 | |||||||||
| Fumonisins (B1, B2) | 500 | 4000 | 1000 | 1000 | 300 | ||||||||
| T-2/HT-2 | 50 | ||||||||||||
*1 μg/kg = 1 ppb (parts per billion)
Worldwide mycotoxin regulations: limits and guideline for cereal products for feed and compound feed
| Aflatoxin B1 | 10 | 10 | 20 | – | ||||||||||
| Aflatoxin total (B1, B2, G1, G2) | 5 | 20 | 20 | 50 | – | 50 | ||||||||
| Ochratoxin A | 50 | 100 | – | |||||||||||
| Deoxynivalenol | 2 | 5000 | 1000 | 1000 | – | |||||||||
| Zearalenone | 500 | 3000 | 1000 | 500 | – | |||||||||
| Fumonisin (B1 B2) | 5000 | 2000 | 5000 | 4000 | 50,000 | – | ||||||||
| T-2/HT-2 | 250 | 500 | – | |||||||||||
*1 μg/kg = 1 ppb (parts per billion)