Biogasification potential of desugarized molasses from sugarbeet processing plants.

Ioannis Martinos Polematidis, A. Koppar, P. Pullammanappallil
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This volume of methane was recovered in the biogas within a 2 day period indicating very good degradability. For every kg of raffinate fed into the anaerobic digester about 94 g COD of organic matter will be discharged with the digester effluent along with 27 g of microbial biomass (or sludge). Every metric tonne of raffinate can generate 4,300 MJ (3.7 MMBtu/US ton) of thermal energy from the combustion of the methane or about 300 kWhe of electricity can be generated (assuming 25% efficiency of converting thermal energy to electricity). Additional key words: Anaerobic digestion; biogas; raffinate; CSB; sugar beet 90 Journal of Sugar Beet Research Vol. 47 Nos. 3 & 4 N 40% of refined sugar consumed in the USA is produced from sugarbeet (Beta vulgaris L.). Beet sugar processing generates significant quantities of both solid (tailings, spent pulp) and liquid (molasses, wastewater) by-products and organic wastes. For example, American Crystal Sugar Company, East Grand Forks (EGF) plant processes 8,310 (metric) tonnes of sugar beets daily to produce 1320 tonnes of sugar. The plant also produces 3500 m3 of wastewater, 432 tonnes of tailings, 1273 tonnes of pressed spent pulp and 332 tonnes of desugarized molasses (Polematidis et al., 2008). The molasses stream from the crystallization process is usually further desugarized in chromatographic separators to recover about 70% of the sucrose. The desugarized molasses by-product stream contains water, residual sugars, raffinose, betaine, amino acids, nitrogen compounds, organic acids and inorganic salts. In some plants the betaine is recovered as another value added product. The desugarized molasses stream is concentrated (also called concentrated separated by-product, CSB raffinate) and sold as animal feed for about US$20/tonne. Sugar production from sugarbeet is an energy intensive operation due to the need for drying and evaporation, and a variety of fossil fuels including coal and natural gas are used. In this paper, we investigate the potential of converting CSB raffinate stream into biogas fuel. Biogas produced in this manner would be a renewable biofuel and could potentially displace some of the fossil fuel used in the plant. Biogasification (or anaerobic digestion) is a biochemical process in which the organic compounds (like carbohydrates, proteins and fats) are mineralized to biogas under anaerobic conditions by the concerted and syntrophic action of a mixed culture of naturally occurring microorganisms. Biogas is a mixture of methane (50 – 70%) and carbon dioxide (30-50%) and can be used as fuel in boilers or for electricity generation with very little clean up. Biogas can also be converted to renewable natural gas by removing carbon dioxide and other trace contaminants and injected into natural gas pipelines for transportation. The process of anaerobic digestion has advantages over aerobic waste treatment processes since it not only reduces the polluting potential (oxygen demand) of the waste but also produces a biofuel. The process does not reduce the nutrient (nitrogen and phosphorus) levels. Even though there have been some studies pertaining to anaerobic digestion of molasses from sugarcane refineries (Romli et al., 1994, 1995), it is not implemented in practice as molasses in itself has a high value and by converting to biogas not much value is added to the feedstock. However, the situation may be different for the desugarized molasses stream as it is a low value product. Moreover, since a major Aug. Dec. 2010 Biogasification Potential 91 fraction of the sugars have been removed, its methane production potential could have also decreased and may not produce significant methane to make its biogasification economically viable. This paper presents results from laboratory scale investigations on the biochemical methane potential of desugarized molasses from a sugarbeet processing plant. The anaerobic digestion process is analyzed in terms of extent of organic matter converted to biogas, undegraded residual organic matter and methane production rate. 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引用次数: 7

Abstract

Sugar production from sugarbeet (Beta vulgaris) generates a co-product stream called raffinate, desugarized molasses, or concentrated separated by-product (CSB). About 0.25 metric tonnes of raffinate is generated for every metric tonne of sugar produced. In this paper, the potential of biogasifying the raffinate to produce methane fuel is investigated. Several aliquots of CSB raffinate (0.1 – 0.2 kg), obtained from the American Crystal Sugar Company, MN, were biogasified in batch mode in a bench-scale anaerobic downflow stationary fixed film reactor (DSFFR) at a thermophilic temperature of 55 OC. It was found that about 0.118 m3 of methane at STP was produced per kg raffinate. This volume of methane was recovered in the biogas within a 2 day period indicating very good degradability. For every kg of raffinate fed into the anaerobic digester about 94 g COD of organic matter will be discharged with the digester effluent along with 27 g of microbial biomass (or sludge). Every metric tonne of raffinate can generate 4,300 MJ (3.7 MMBtu/US ton) of thermal energy from the combustion of the methane or about 300 kWhe of electricity can be generated (assuming 25% efficiency of converting thermal energy to electricity). Additional key words: Anaerobic digestion; biogas; raffinate; CSB; sugar beet 90 Journal of Sugar Beet Research Vol. 47 Nos. 3 & 4 N 40% of refined sugar consumed in the USA is produced from sugarbeet (Beta vulgaris L.). Beet sugar processing generates significant quantities of both solid (tailings, spent pulp) and liquid (molasses, wastewater) by-products and organic wastes. For example, American Crystal Sugar Company, East Grand Forks (EGF) plant processes 8,310 (metric) tonnes of sugar beets daily to produce 1320 tonnes of sugar. The plant also produces 3500 m3 of wastewater, 432 tonnes of tailings, 1273 tonnes of pressed spent pulp and 332 tonnes of desugarized molasses (Polematidis et al., 2008). The molasses stream from the crystallization process is usually further desugarized in chromatographic separators to recover about 70% of the sucrose. The desugarized molasses by-product stream contains water, residual sugars, raffinose, betaine, amino acids, nitrogen compounds, organic acids and inorganic salts. In some plants the betaine is recovered as another value added product. The desugarized molasses stream is concentrated (also called concentrated separated by-product, CSB raffinate) and sold as animal feed for about US$20/tonne. Sugar production from sugarbeet is an energy intensive operation due to the need for drying and evaporation, and a variety of fossil fuels including coal and natural gas are used. In this paper, we investigate the potential of converting CSB raffinate stream into biogas fuel. Biogas produced in this manner would be a renewable biofuel and could potentially displace some of the fossil fuel used in the plant. Biogasification (or anaerobic digestion) is a biochemical process in which the organic compounds (like carbohydrates, proteins and fats) are mineralized to biogas under anaerobic conditions by the concerted and syntrophic action of a mixed culture of naturally occurring microorganisms. Biogas is a mixture of methane (50 – 70%) and carbon dioxide (30-50%) and can be used as fuel in boilers or for electricity generation with very little clean up. Biogas can also be converted to renewable natural gas by removing carbon dioxide and other trace contaminants and injected into natural gas pipelines for transportation. The process of anaerobic digestion has advantages over aerobic waste treatment processes since it not only reduces the polluting potential (oxygen demand) of the waste but also produces a biofuel. The process does not reduce the nutrient (nitrogen and phosphorus) levels. Even though there have been some studies pertaining to anaerobic digestion of molasses from sugarcane refineries (Romli et al., 1994, 1995), it is not implemented in practice as molasses in itself has a high value and by converting to biogas not much value is added to the feedstock. However, the situation may be different for the desugarized molasses stream as it is a low value product. Moreover, since a major Aug. Dec. 2010 Biogasification Potential 91 fraction of the sugars have been removed, its methane production potential could have also decreased and may not produce significant methane to make its biogasification economically viable. This paper presents results from laboratory scale investigations on the biochemical methane potential of desugarized molasses from a sugarbeet processing plant. The anaerobic digestion process is analyzed in terms of extent of organic matter converted to biogas, undegraded residual organic matter and methane production rate. Based on the results a simple analysis was carried out to determine energy potential of the raffinate.
甜菜加工厂脱糖糖蜜的生物气化潜力。
从甜菜(Beta vulgaris)中生产糖会产生一种副产物流,称为萃余液、去糖糖蜜或浓缩分离副产物(CSB)。每生产一吨糖,就会产生大约0.25公吨的萃余液。本文研究了废液生物气化生产甲烷燃料的潜力。从美国冰糖公司(MN)获得若干等分的CSB余液(0.1 - 0.2 kg),在一个实验规模的厌氧下流固定膜反应器(DSFFR)中,在55℃的嗜热温度下,以间歇式模式进行了生物气化。结果表明,在STP下,每千克萃余液产生约0.118 m3的甲烷。在2天的时间内,沼气中的甲烷量被回收,这表明沼气的可降解性非常好。每千克排入厌氧消化池的尾液中,约94克COD有机物将随消化池出水排出,同时排出27克微生物生物量(或污泥)。每公吨的尾液可以从甲烷燃烧中产生4300兆焦耳(370万英热单位/美吨)的热能,或产生约300千瓦时的电力(假设热能转化为电能的效率为25%)。关键词:厌氧消化;沼气;萃余液;CSB;《甜菜研究杂志》第47卷第3期和第4期N在美国消费的精制糖中有40%是由甜菜(Beta vulgaris L.)生产的。甜菜糖加工产生大量固体(尾矿、废纸浆)和液体(糖蜜、废水)副产品和有机废物。例如,美国水晶糖公司东大福克斯(EGF)工厂每天处理8310吨甜菜,生产1320吨糖。该工厂还生产3500立方米废水、432吨尾矿、1273吨压榨废纸浆和332吨脱糖糖蜜(Polematidis et al., 2008)。结晶过程中的糖蜜流通常在色谱分离器中进一步解糖,以回收约70%的蔗糖。脱糖糖蜜副产品流含有水、残糖、棉子糖、甜菜碱、氨基酸、氮化合物、有机酸和无机盐。在一些植物中,甜菜碱作为另一种增值产品被回收。经浓缩的糖蜜流(也称为浓缩分离副产品,CSB萃余液)作为动物饲料出售,价格约为每吨20美元。由于需要干燥和蒸发,从甜菜中生产糖是一种能源密集型操作,并且使用多种化石燃料,包括煤和天然气。在本文中,我们研究了将CSB尾液流转化为沼气燃料的潜力。以这种方式产生的沼气将是一种可再生生物燃料,并有可能取代工厂中使用的一些化石燃料。生物气化(或厌氧消化)是一种生化过程,其中有机化合物(如碳水化合物,蛋白质和脂肪)在厌氧条件下通过自然存在的微生物混合培养的协同作用被矿化成沼气。沼气是甲烷(50 - 70%)和二氧化碳(30-50%)的混合物,可以用作锅炉的燃料或用于发电,几乎不需要清理。沼气也可以通过去除二氧化碳和其他微量污染物转化为可再生天然气,注入天然气管道进行运输。厌氧消化过程比好氧废物处理过程具有优势,因为它不仅降低了废物的污染潜力(需氧量),而且还产生了生物燃料。这个过程不会降低营养物(氮和磷)的含量。尽管已经有一些关于甘蔗精炼厂糖蜜厌氧消化的研究(Romli等人,1994,1995),但由于糖蜜本身具有很高的价值,并且通过转化为沼气并没有给原料增加多少价值,因此没有在实践中实施。然而,由于糖蜜是一种低价值产品,因此情况可能有所不同。此外,由于2010年8月至12月的主要生物气化潜力91部分的糖已被去除,其甲烷生产潜力也可能下降,可能不会产生显著的甲烷,使其生物气化在经济上可行。本文介绍了实验室规模对甜菜加工厂脱糖糖蜜生化甲烷势的研究结果。从有机物转化为沼气的程度、未降解残余有机物和甲烷产率等方面分析厌氧消化过程。在此基础上进行了简单的分析,确定了萃余液的能势。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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