scholarly journals Analysis of Drying of Brewers’ Spent Grain

Proceedings ◽  
2018 ◽  
Vol 2 (23) ◽  
pp. 1467 ◽  
Author(s):  
José Ignacio Arranz ◽  
María Teresa Miranda ◽  
Francisco José Sepúlveda ◽  
Irene Montero ◽  
Carmen Victoria Rojas
Keyword(s):  
Energy Use ◽  
Low Cost ◽  
Matter Content ◽  
Raw Material ◽  
Dry Matter Content ◽  
Brewing Industry ◽  
Livestock Feed ◽  
Spent Grain ◽  
Very High ◽  
Animal Consumption

Brewing industry generates a main residue, brewers’ spent grain (BSG), which has good properties both for use in animal consumption and for thermal use, but contains a very high content of moisture (20–25% dry matter content), so that its elimination or treatment should be immediate, since it can cause degeneration problems of the product. Currently, brewers often supply this material at low cost for use as livestock feed. This solution is not efficiently carried out without reporting too much benefit to the brewers more than to eliminate waste from their facilities. However, BSG is a raw material of interest for application in different areas due to its low price, availability throughout the year and a valuable chemical composition, so it seems necessary to look for an alternative use to give value to these characteristics. In this paper a drying study is carried out in order to establish the foundations for its energy use by thermal of BSG. BSG has been used from a craft brewery located at Badajoz, Spain. Drying analysis was carried out for various temperatures and inlet air flow by means a convective dryer. The properties studied show that BSG can be used for thermal utilization in large installations, being necessary heat drying processes as a pretreatment in order to obtain a biofuel with acceptable efficiency.

STUDY OF THE KINETICS OF DRYING BREWER’S SPENT GRAIN

2020 ◽  
Author(s):  
Т.Г. КОРОТКОВА ◽  
А.С. ДАНИЛЬЧЕНКО ◽  
Н.Ю. ИСТОШИНА
Keyword(s):  
Matter Content ◽  
Dry Matter Content ◽  
Drying Time ◽  
Brewer’S Spent Grain ◽  
Average Value ◽  
Free Moisture ◽  
Before And After ◽  
Spent Grain ◽  
Kinetics Of ◽  
Two Temperature

Исследована кинетика сушки сырой пивной дробины – вторичного продукта ООО «Белореченский пивоваренный завод» (Россия, Краснодарский край). Сушка проведена в двух температурных режимах – 60 и 55°С. Скорость сушильного агента при вынужденной конвекции составляла 4,5 м/с. Содержание сухого вещества определено по ГОСТ 31640–2012 в лабораторных условиях и составило 12,9%. Измерение убыли массы при сушке проведено с интервалом 5 мин. Общее время сушки навески пивной дробины в количестве 50 г – 420 мин при режиме 50°С, 360 мин – при 60°С. Среднее значение конечной влажности пивной дробины составило 11,85%. Построены кривые сушки и скорости сушки. Скорость сушки при удалении свободной влаги в первом периоде сушки, мин–1: при 60°С – 3,5, при 55°С – 3,0. Установлено, что содержание связанной влаги составляет в среднем 57% от массы влаги в навеске пивной дробины, свободной влаги – 43%. Анализ структуры навески пивной дробины под микроскопом до сушки и после нее подтвердил факт, что в исследованном материале количество связанной влаги больше, чем свободной. Наличие частиц размером 5–7 мм свидетельствует о значительном количестве клеточной влаги в неразрушенных капиллярах. Дальнейшее совершенствование технологии переработки пивной дробины должно быть направлено на разрушение клеточной структуры материала после его механического обезвоживания. The kinetics of drying of the crude brewer’s spent grain – a secondary product of LLC «Belorechensky brewery» (Russian Federation, Krasnodarregion) has been studied. Drying is carried out in two temperature modes – 60 and 55°C. The speed of the drying agent under forced convection was 4,5 m/s. The dry matter content was determined according to GOST 31640–2012 in laboratory conditions and was 12,9%. Measurement of mass loss during drying was performed at an interval of 5 min. The total drying time of the brewer’s spent grain sample in the amount of 50 gis 420 min at 50°C, 360 min – at 60°C. The average value of the final moisture content of brewer’s spent grain made up 11,85%. Curves of drying and drying speed are constructed. Drying speed when removing free moisture in the first drying period, min–1: at 60°C – 3,5, at 55°C – 3,0. It was found that the content on average of bound moisture is 57% of the mass of moisture in brewer’s spent grain, free moisture – 43%. Analysis of the structure sample of brewer’s spent grain a microscope before and after drying confirmed the fact that the amount of bound moisture in the studied material is greater than the amount of free moisture. The presence of particles of 5–7 mm in size indicates a significant amount of cellular moisture in undisturbed capillaries. Further improvement of the technology for processing brewer’s spent grain should be aimed at destroying the cellular structure of the material after its mechanical dehydration.

scholarly journals BIOGAS PRODUCTION FROM AMARANTH BIOMASS

2013 ◽  
Vol 10 (2) ◽  
pp. 59-62
Author(s):  
Vladimír Sitkey ◽  
Ján Gaduš ◽  
Ľubomír Kliský ◽  
Alexander Dudák
Keyword(s):  
Dry Matter ◽  
Large Scale ◽  
Biogas Production ◽  
Organic Fertilizer ◽  
Matter Content ◽  
Raw Material ◽  
Dry Matter Content ◽  
Optimum Conditions ◽  
Average Yield ◽  
Amaranthus Spp

Abstract Energy variety of amaranth (Amaranthus spp.) was grown in large-scale trials in order to verify the capability of its cultivation and use as a renewable energy source in a biogas plant. The possibility of biogas production using anaerobic co-fermentation of manure and amaranth silage was verified in the experimental horizontal fermentor of 5 m3 volume, working at mesophilic conditions of 38-40 °C. The goal of the work was also to identify the optimum conditions for growth, harvesting and preservation of amaranth biomass, to optimize biogas production process, and to test the residual slurry from digestion process as a high quality organic fertilizer. The average yield of green amaranth biomass was 51.66 t.ha-1 with dry matter content of 37%. Based on the reached results it can be concluded that amaranth silage, solely or together with another organic materials of agricultural origin, is a suitable raw material for biogas production.

scholarly journals Effect of Pre-hydrolysis on Simultaneous Saccharification and Fermentation of Native Rye Starch

2020 ◽  
Vol 13 (6) ◽  
pp. 923-936 ◽  
Author(s):  
Ewelina Strąk-Graczyk ◽  
Maria Balcerek
Keyword(s):  
Dry Matter ◽  
Agricultural Sector ◽  
Simultaneous Saccharification And Fermentation ◽  
Ethanol Yield ◽  
Matter Content ◽  
Raw Material ◽  
Process Efficiency ◽  
Dry Matter Content ◽  
Sem Images ◽  
Simultaneous Saccharification

Abstract The rising population and increasing demand for food place added pressure on the agricultural sector to maintain high process efficiency while implementing environmentally friendly methods. In this study, we investigate the effect of pre-hydrolysis of native rye starch and its influence on the yield of ethanol obtained by simultaneous saccharification and fermentation (SSF) from high gravity rye mashes with 25% and 28% w w−1 dry matter content. Fermentation was carried out in a 3-day system at a temperature of 35 ± 1 °C using the dry distillery yeast Ethanol Red (Saccharomyces cerevisiae). The characteristics of the tested raw material and changes in the native rye starch during enzymatic hydrolysis were analyzed using a scanning electron microscope (SEM). The SEM images revealed characteristic changes on the surface of the starch, which was found to have a layered structure, as well as interesting behavior by the yeast during SSF when the glucose concentration in the environment was lowered. Both in the mashes with 25% and 28% w w−1 dry matter, starch pre-hydrolysis did not significantly increase either the initial amounts of sugars available to the yeast or the fermentation efficiency and ethanol yield in comparison to the mashes without this pre-treatment.

Isoconversional Kinetic Analysis of Pyrolysis of Malt Waste

2017 ◽  
Vol 899 ◽  
pp. 107-112
Author(s):  
Beatriz Cristina Silvério ◽  
Pedro Ivo Brandão e Melo Franco ◽  
Carolina Moreno de Freitas ◽  
Kássia Graciele dos Santos ◽  
Nelson Roberto Antoniosi Filho
Keyword(s):  
Low Cost ◽  
Estimation Methods ◽  
Slow Heating ◽  
Brewing Industry ◽  
Heating Rates ◽  
Spent Grain ◽  
Exponential Factors ◽  
Isoconversional Kinetic Analysis ◽  
Malt Waste ◽  
Energy Activation

Locally available malt waste or brewers' spent grain, a by-product of brewing industry, was found to be a low cost and promising biomass for pyrolysis. A kinetic studied of pyrolysis of malt waste was investigated by non-isothermal thermogravimetric analyses (TG-DTG), applying slow heating rates, 10, 15, 30 and 50 K/min, and well-defined conditions. Activation energies and Arrhenius exponential factors were inferred by different estimation methods: Kissinger, Ozawa, Starink, K-A-S and. The methods presented energy activation values of 214 - 238.23 kJ/mol. The Literature studies found activations energies values similar to those found for sugarcane bagasse pyrolysis and other types of biomasses with predominance of hemicelluloses, cellulose and lignin, respectively.

Use of dry matter content as a rapid and low-cost estimate for ranking genotypic differences in water-soluble carbohydrate concentrations in the stem and leaf sheath of Triticum aestivum

2009 ◽  
Vol 60 (1) ◽  
pp. 51 ◽  
Author(s):  
Gang-Ping Xue ◽  
C. Lynne McIntyre ◽  
Allan R. Rattey ◽  
Anthony F. van Herwaarden ◽  
Ray Shorter
Keyword(s):  
Dry Matter ◽  
Field Experiments ◽  
Low Cost ◽  
Leaf Sheath ◽  
Matter Content ◽  
Water Soluble ◽  
Genotypic Differences ◽  
Dry Matter Content ◽  
Cereal Breeding ◽  
Field Samples

Stem water-soluble carbohydrates (WSC) are an important source of temporary carbohydrate reserve in cool-season cereals. Genotypic variation in stem WSC concentration in wheat at anthesis is often positively associated with grain weight and yield in water-limited environments. In this study we have examined the relationship between dry matter content (DMC, dry weight per unit of fresh weight) and WSC concentration in field-grown bread wheat. Strong correlations (r = 0.92–0.95) were observed between DMC and WSC concentration in the stem and leaf sheath from the top two or three internodes of recombinant inbred lines from a cross between Seri M82 and Babax, at anthesis or 1 week after anthesis, in several field experiments. This strong correlation was also observed in diverse genotypes grown under rainfed or irrigated conditions. DMC and WSC concentration were also positively correlated in the whole above-ground biomass of wheat at anthesis (r = 0.74–0.91). Measurement of stem and leaf sheath DMC and WSC concentration in a small number of samples would allow the rapid prediction of WSC concentrations in a large number of field samples with reasonable accuracy, as demonstrated in a small dataset in this study. These data indicate that DMC can serve cereal breeding as a rapid and low-cost selection tool for genotypic ranking of WSC concentrations in breeding populations.

Antioxidant Activities of Soluble Dietary Fiber Extracted from Brewers’ Spent Grain

2011 ◽  
Vol 233-235 ◽  
pp. 2824-2827 ◽  
Author(s):  
Quan Yi Fu ◽  
Xu Cong Yu ◽  
Lin Li ◽  
Guo Qin Liu ◽  
Bing Li
Keyword(s):  
Dietary Fiber ◽  
Superoxide Anion ◽  
Superoxide Radical ◽  
Antioxidant Activities ◽  
Raw Material ◽  
Dpph Radical ◽  
Brewing Industry ◽  
Soluble Dietary Fiber ◽  
Spent Grain

Brewers’ spent grain (BSG) is the most common by-product of the brewing industry, contains about 16.8% cellulose, 28.4% non-cellulosic polysaccharides and 27.8% lignin, which is a good raw material for industrial production of soluble dietary fiber (SDF).The antioxidant activity of crude dietary fiber (CDF) and grade dietary fiber (GDF) isolated from BSG was investigated in vitro. The scavenging hydroxyl radical capability of CDF and GDF was respectively reached to15.4% and 69.2% at the concentration of 0.1mg /mL. DF concentration from 0.02mg /mL to 0.1m g /mL was used. The scavenging capability of CDF and GDF to superoxide anion radical was increased from 10.68% and 12.33% to 35.78% and 78.39%. Both of the two DF showed some effect in scavenging superoxide radical and 2, 2-Diphenyl-1-picrylhydrazyl (DPPH) radical with the concentration increase. The result showed that BSG DF can be used as a good additive with some functionality.

scholarly journals The Influence of by-Products From Brewery Spent Grain Hydrolysis on Lactic Acid Fermentation Efficiency

2021 ◽  
Author(s):  
Magdalena Lech
Keyword(s):  
Lactic Acid ◽  
Production Efficiency ◽  
Low Cost ◽  
Lactic Acid Production ◽  
Glucose Consumption ◽  
Raw Material ◽  
Acid Fermentation ◽  
Spent Grain ◽  
Fermentable Carbohydrates ◽  
By Products

Abstract The brewery spent grain (BSG) is a lignocellulosic waste material produced in a huge amount around the world. Strict environmental protection law requires proper utilization. BSG can be transformed into easy-fermentable carbohydrates as a result of hydrolysis. This may be a low-cost raw material for biotechnological fermentation. The literature provides a lot of information that hydrolysis of lignocellulose creates by-products which can be potentially noxious to bacteria cells employed in fermentation. This research examined the influence of most of these by-products: furfural, acetic, formic, gallic, and levuilnic acid, on the LA fermentation effectiveness. These components were introduced to Lactobacillus cultures in various concentrations. The rate of cell growth, glucose consumption, and lactic acid production were measured. This components affects in various extent on LA formation in the culture. In any case, there is a critical value of them harms the fermentation, due to the reduced ability of bacteria propagation. Lower concentrations of bio-catalyst lead to an LA production efficiency drop. The LA concentrations in flasks after one day of propagation with the 2.1 [g/L] of appropriate inhibitor drop app. [%] 16 (F), 22 (GA), 8 (LevA), 40 (AA), and 100 (FA) in comparison to the flask without any inhibitor.

scholarly journals Bioactive compounds in the aboveground part of hemiephemeroid onions (Allium L.)

2021 ◽  
Vol 181 (4) ◽  
pp. 37-43
Author(s):  
T. I. Fomina ◽  
T. A. Kukushkina
Keyword(s):  
Ascorbic Acid ◽  
Secondary Metabolites ◽  
Bioactive Compounds ◽  
Dry Matter ◽  
Matter Content ◽  
Raw Material ◽  
Dry Matter Content ◽  
High Biological Activity ◽  
Constant Weight ◽  
Total Sugars

Background. Representatives of the genus Allium L. are valuable food and medicinal plants that have long been used for nutrition and human health. Modern research has proved their high biological activity. Earlier, we investigated the aboveground organs of a number of wild onion species in the consumer ripeness phase. Higher content of secondary metabolites has been observed in the hemiephemeroid species A. aflatunense B. Fedtsch., A. microdictyon Prokh., and A. rosenbachianum Regel. The aim of this work was to determine the content of bioactive compounds in the green biomass of Allium species during flowering.Materials and methods. We studied the freshly harvested raw materials – leaves and flower scapes. Dry matter content was measured by drying 1 g of raw material at 100–105°C to constant weight. The amounts of phenolic compounds, pectic substances, total sugars and carotenoids were assessed spectrophotometrically using the SF-56 (Russia) and SF Agilent 8453 (USA) instruments, and ascorbic acid was measured by the titrimetric method. The result was taken as an average of three measurements for each indicator calculated on absolute dry weight of raw material (except ascorbic acid).Results and conclusions. The green biomass of Allium species was found to contain 8,2–16,2% of dry matter; 4,5–12,0% of phenolics (catechins, flavonols and tannins); 6,9–32,4% of total sugars; 9,5–12,6% of pectic compounds (pectins and protopectins); 20,8–102,5 mg% of carotenoids, and 38,0–197,7 mg% of ascorbic acid (wet weight). A significant range of variation in the content of secondary metabolites was due to the species’ characteristics and weather conditions of the growing season. A. microdictyon had a higher content of dry matter, flavonols and tannins, whereas A. aflatunense and A. rosenbachianum were rich in ascorbic acid and sugars. The findings testify to the prospects of using Allium spp. as a source of bioactive compounds. 

scholarly journals Optimization of centrifugal separation of α-lactalbumin and β-lactoglobulin

1997 ◽  
Vol 6 (2) ◽  
pp. 193-198 ◽  
Author(s):  
Tuomo Tupasela ◽  
Petri Koskela ◽  
Eero Pahkala ◽  
Veikko Kankare
Keyword(s):  
Heat Treatment ◽  
Concentration Factor ◽  
Dry Matter ◽  
Separation Efficiency ◽  
Concentration Level ◽  
Bovine Milk ◽  
Matter Content ◽  
Raw Material ◽  
Dry Matter Content ◽  
Β Lactoglobulin

Whey proteins, which are mainly composed of β-lactoglobulin (β-lg) and α-lactalbumin (α-la), account for about 20% of the proteins of bovine milk. In this study we investigated the effect of pH, dry matter content, concentration factor, heat treatment and centrifugation on the separation of α-la from β-lg using clarified whey as raw material, α-La precipitation was highest, 23.3%, when the dry matter content ranged from 5.8% to 25.7%. The optimum pH of α-la precipitation depended on the dry matter content. The separation efficiency increased when the concentration factor and heat treatment time at 55°C increased. A longer centrifugation time and higher separation speed did not have a marked effect on the separation efficiency. Separation was more efficient with a higher centrifugation speed at concentration levels 30 X and 60 X. The separation efficiency did not improve when the temperature was raised from 55°C to 65°C but it was better at a concentration level 120 X than at 60 X and 30 X, and also at concentration level 60 X than with 30 X.

scholarly journals Kinetic patterns and optimization of the process of concentration by freezing the blood of cattle

2019 ◽  
Vol 80 (4) ◽  
pp. 12-18
Author(s):  
S. T. Antipov ◽  
V. Yu. Ovsyannikov ◽  
A. A. Korchinskij
Keyword(s):  
Heat Exchange ◽  
Boiling Point ◽  
Dry Matter ◽  
Matter Content ◽  
Raw Material ◽  
Dry Matter Content ◽  
Wide Range ◽  
Experimental Apparatus ◽  
Heat Exchange Surface ◽  
Exchange Surface

The urgency of the use of blood components as a raw material for the production of products from it that contribute to the prevention and treatment of iron deficiency states is beyond doubt. In addition, protein compounds in the blood of cattle have a high digestibility of the human body, and the complex of essential amino acids determines its attractiveness as an additive in the development of a wide range of meat products. The only possible way at present to thicken thermo labile blood compounds is cryoconcentration, carried out in a temperature range close to the cryoscopy temperature. The kinetic features of cryoconcentration of cattle blood were investigated on an experimental apparatus of cyclic action. It is shown that the conditions of cryoconcentration are determined by the boiling point of the refrigerant in the evaporator of the installation, the flow rate of the original blood washing the heat exchange surface and the content of soluble compounds in the initial liquid. Experimental data are presented in the form of growth curves of frozen ice on the heat exchange surface with an area of 0.2 m2. Using mathematical planning methods, equations are obtained that describe the amount of ice frozen for 1 hour per unit of surface area of the freezing plant, the specific energy input for freezing one kilogram of ice, and the dry matter content of the blood in the solution obtained by melting the frozen ice. The solved problem of optimizing the process of blood cryoconcentration made it possible to find rational intervals for changing the operating parameters of the freezing plant, ensuring the maximum amount of frozen ice, minimal energy costs and minimal content of soluble substances in the solution obtained by melting frozen ice. The suboptimal intervals of the indicated parameters were the following: refrigerant boiling point 256– 260 K, blood consumption (0.20–0.205)·10-3 m3/s, dry matter content 22.5–23.0 %.

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