Abstract:Sugar derived from lignocellulosic biomass is an important intermediate product, often used for the production of biofuels and value‐added chemicals. It is therefore essential to understand and reduce the production costs of sugar derived from lignocellulosic biomass. This study evaluates the economic feasibility of a biorefinery producing sugar from lignocellulosic biomass using a combination of autohydrolysis and mechanical refining pretreatment. This biorefinery is self‐sufficient in energy, producing exces… Show more
“…Giuliano et al 23 determined the selling price to be US$3.5/kg, and concluded that co-production of ethanol and xylitol was desirable. Ou et al 24 performed TEA of a sugarcane production facility co-producing xylitol and polyols, and determined variation in sugar price with production of xylitol and polyols. For a feedstock processing capacity of 1500 MT/day, the selling price of xylitol was US$2/kg.…”
A detailed techno-economic analysis and life cycle assessment (LCA) of a novel bio-refinery that produces xylitol from sugarcane bagasse are provided. The proposed process includes dilute acid pretreatment in pressurized conditions followed by fermentation (upstream section). The fermentation broth is then sent for separation and purification to the downstream section. Calculations are performed for a plant with 4 t/h of dry bagasse throughput. With a fermentation yield of 0.54 g xylitol per g of xylose, the plant produced 437.4 kg/h of xylitol. Upstream data are adapted from experimental studies, while ASPEN PLUS ® flowsheet simulation is used to obtain data for the downstream section. The xylitol production facility is assumed to be annexed to an existing sugar mill in India. The total utility requirement in the process is reduced using heat integration strategies. Cradle-to-gate scope is considered for the LCA and 1 kg of xylitol is taken as the functional unit. The product cost of xylitol is calculated to be 230 INR/kg (US$3.17/kg). For a 4 year payback period, the selling price of xylitol must be 450 INR/kg (US$6.2/ kg). The fermentation and pretreatment sections are the major components of the product cost. The LCA results show that the life cycle greenhouse gas emissions are 2.759 kg CO 2 eq. per kg xylitol. The electricity requirement within the plant is identified as the major source of greenhouse gas emissions, and reduction of fermentation duration is identified as a key factor. The results identify opportunities to improve the process from an economic as well as an environmental standpoint.
“…Giuliano et al 23 determined the selling price to be US$3.5/kg, and concluded that co-production of ethanol and xylitol was desirable. Ou et al 24 performed TEA of a sugarcane production facility co-producing xylitol and polyols, and determined variation in sugar price with production of xylitol and polyols. For a feedstock processing capacity of 1500 MT/day, the selling price of xylitol was US$2/kg.…”
A detailed techno-economic analysis and life cycle assessment (LCA) of a novel bio-refinery that produces xylitol from sugarcane bagasse are provided. The proposed process includes dilute acid pretreatment in pressurized conditions followed by fermentation (upstream section). The fermentation broth is then sent for separation and purification to the downstream section. Calculations are performed for a plant with 4 t/h of dry bagasse throughput. With a fermentation yield of 0.54 g xylitol per g of xylose, the plant produced 437.4 kg/h of xylitol. Upstream data are adapted from experimental studies, while ASPEN PLUS ® flowsheet simulation is used to obtain data for the downstream section. The xylitol production facility is assumed to be annexed to an existing sugar mill in India. The total utility requirement in the process is reduced using heat integration strategies. Cradle-to-gate scope is considered for the LCA and 1 kg of xylitol is taken as the functional unit. The product cost of xylitol is calculated to be 230 INR/kg (US$3.17/kg). For a 4 year payback period, the selling price of xylitol must be 450 INR/kg (US$6.2/ kg). The fermentation and pretreatment sections are the major components of the product cost. The LCA results show that the life cycle greenhouse gas emissions are 2.759 kg CO 2 eq. per kg xylitol. The electricity requirement within the plant is identified as the major source of greenhouse gas emissions, and reduction of fermentation duration is identified as a key factor. The results identify opportunities to improve the process from an economic as well as an environmental standpoint.
“…The expected production cost in the NSM was $0.43/kg (dry sugar mixture) in 2020 US dollar equivalents for the concentrated sugar stream for an expected plant lifetime of 30 years and an internal rate of return of 10%. The cost is conservatively high compared to other analyses of sugar production from lignocellulosic biomass, not only in terms of production cost, but also in terms of capital cost per unit of installed production capacity (Michels, 2014;Moncada et al, 2018;Ou et al, 2021), These are generally higher than the historical sugar spot prices in the last five years, ranging between $0.22-0.50/kg (Macrotrends, 2021).…”
Section: Cost Of and Speed Of Sugar Productionmentioning
“…Particularly, in the last five years the researchers have attempted to integrate the developed process modules with the technoeconomics to understand the benefits associated with holistic utilization of all biomass components. For instance, Ou et al (2021) showed that if 1500 tonnes of miscanthus was processed for sugar production per day, the minimum sugar selling price (MSSP) was $446/tonnes. 178 However, when the xylose stream obtained when fed-batch strategy fermentation was adopted.…”
Section: E Coli Strain Was Engineered To Hydrolyse Xylan Fraction Of Hemicellulose By Heterologous Overexpression Of β-mentioning
confidence: 99%
“…For instance, Ou et al (2021) showed that if 1500 tonnes of miscanthus was processed for sugar production per day, the minimum sugar selling price (MSSP) was $446/tonnes. 178 However, when the xylose stream obtained when fed-batch strategy fermentation was adopted. 180 Lately Ranganathan (2020) showed that when glucose derived from rice straw was used for ethanol production, but xylose was kept intact, the cost of ethanol was $0.627/L.…”
Section: E Coli Strain Was Engineered To Hydrolyse Xylan Fraction Of Hemicellulose By Heterologous Overexpression Of β-mentioning
confidence: 99%
“…For instance, Ou et al (2021) showed that if 1500 tonnes of miscanthus were processed for sugar production per day, the minimum sugar selling price (MSSP) would be $446 per tonne. 178 However, when the xylose stream obtained after auto-hydrolysis was diverted for xylitol production, the MSSP was reduced to $347 per tonne. Similar observations were made by Giuliano et al (2018), who found that if only cellulosic ethanol was targeted from steam exploded corn stover, the payback ethanol price was €1.62 per kg.…”
Section: Xylose As An Alternative Carbon Source For Microbial Growth and Product Developmentmentioning
Biologists and engineers are making tremendous efforts in contributing to a sustainable and green society. To this end, there is an increase in interest towards waste management cum valorisation. Lignocellulosic...
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