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This report presents the economics of bio-based Acrylic Acid production from glucose syrup in Germany using a fermentation process similar to Cargill process. Initially, raw sugar is hydrolyzed into invert sugars, which are fermented to produce 3-hydroxypropionic acid (3-HPA), which is then dehydrated to produce Acrylic Acid.
This report shows a feasibility study of Bio-Adipic Acid production from glucose syrup in a plant located in the United States. The route examined is a two-step catalytic process similar to Rennovia process. In this process, glucose is first oxidized to produce glucaric acid, which is then hydrogenated to produce Adipic Acid.
This report assesses the economics of production of bio-based Adipic Acid. The process examined in this report is a fermentation process similar to BioAmber process, in which glucose is fermented to adipic acid. The process under analysis assumes a plant located in the United States.
This report assesses the economics of production of bio-based Adipic Acid. The process examined in this report is a fermentation process similar to BioAmber process, in which raw sugar is fermented to adipic acid. The process under analysis assumes a plant located in Germany.
It presents the economics of bio-based 1,3-Butadiene (BD) production from glucose syrup in the United States using a direct aerobic fermentation process similar to the one proposed by Global Bioenergies.
It presents the economics of bio-based 1,3-Butadiene (BD) production from glucose syrup in the United States using an anaerobic fermentation process.
It presents the economics of bio-based 1,3-Butadiene (BD) production from raw sugar in Germany using a direct aerobic fermentation process similar to the one proposed by Global Bioenergies. Raw sugar is hydrolyzed into invert sugars, which are fermented to Butadiene.
This study refers to bio-based 1,3-Butadiene production from raw sugar in Germany via an anaerobic fermentation process. Raw sugar is first hydrolyzed into invert sugars, which are then fermented to Butadiene.
This report concerns the bio-based BDO production in the United States from glucose. In this report, BDO is produced using a two-step process similar to Myriant/JM Davy technology. In this process, glucose is fermented to succinic acid, which is then hydrogenated to BDO. Ammonium sulfate and tetrahydrofuran (THF) are generated as by-products.
This report examines the costs related to Butanediol production from glucose syrup. Initially, glucose is fermented to produce succinic acid, which is then hydrogenated to produce butanediol. The economic analysis is based on a plant constructed in the United States.
This report presents the economics of bio-based 1,4-Butanediol production from raw sugar in Germany. Initially, raw sugar (sucrose) is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are fermented to produce succinic acid, which is then hydrogenated to produce BDO.
This report presents the economics of bio-based 1,4-Butanediol (BDO) production from glucose syrup in a plant located in the United States. This process, similar to the one proposed by Genomatica, consists in a direct fermentation of glucose syrup, producing BDO, which is then submitted to purifying steps.
It examines bio-based BDO production using a fermentation process similar to the one proposed by Genomatica. This report presents an economic analysis for a plant constructed in Germany using raw sugar as feedstock in the fermentation.
This report presents the economics of bio-based Butanol production from corn in the United States. The process under analysis is a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. Initially, corn undergoes wet milling to separate starch, which is hydrolyzed in two steps. Glucose is fermented to produce butanol, acetone and ethanol.
This report examines a conventional Acetone-Butanol-Ethanol (ABE) fermentation process. This economic analysis assumes a plant located in Germany using raw sugar as feedstock, which is fermented to Butanol, acetone and ethanol by a novel strain of Clostridium. Each product is separated.
This report provides the economics of bio-based Isobutanol production from corn in the USA using a typical fermentation process. In this process, distiller's dried grains with solubles (DDGS) are generated as by-product.
This study presents a techno-economic analysis of cellulosic Isobutanol production from corn stover in the United States using a biochemical process. Initially, corn stover is treated with dilute acid and undergoes ammonia conditioning. Then, the cellulose is enzimatically hydrolyzed to glucose and xylose, which are then fermented to produce Isobutanol.
This report provides the economics of bio-based Isobutanol production from raw sugar in Germany using a typical fermentation process. Initially, raw sugar is hydrolyzed into invert sugars, which are then fermented to produce Isobutanol.
This feasibility study approaches an economic analysis of Bio-Isoprene production from glucose syrup in the United States using an aerobic fermentation process.
This report provides a techno-economic study of a fermentation process for Isoprene production from glucose in the United States. In the process examined in this report, glucose syrup undergoes anaerobic fermentation for isoprene production.
This feasibility study approaches an economic analysis of Bio-Isoprene production from raw sugar in Germany using an aerobic fermentation process. Raw sugar is initially hydrolyzed into glucose and fructose (invert sugars), which are then fermented to Isoprene product.
This report provides a techno-economic study of a fermentation process for Isoprene production from raw sugar in the Germany. In the process examined in this report, raw sugar is initially hydrolyzed into glucose and fructose (invert sugars), which are then anaerobically fermented to Isoprene product.
This report presents the economics of L-Methionine production from glucose syrup in the United States using a process similar to the technology developed by Metabolic Explorer. In this process, glucose is fermented in an aerobic environment to produce L-Methionine.
This report presents the economics of L-Methionine production from raw sugar (sucrose) in Germany using a process similar to the technology developed by Metabolic Explorer. In this process, sucrose is diluted and sucrose is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are then fermented in an aerobic environment to produce L-Methionine.
This report examines the costs of p-Xylene production from glucose syrup in the United States. Initially, glucose is converted to hydroxymethylfurfural (HMF), which reacts with hydrogen to produce dimethylfuran (DMF). Finally, DMF reacts with ethylene using hexane as a solvent, yielding paraxylene.
This study approaches an economic analysis of p-Xylene production from glucose syrup in the United States. In this process, glucose is fermented to isobutanol intermediate, which is then converted to p-Xylene through dehydration, dimerization and dehydrocyclization.
This report provides an economics of p-Xylene production from raw sugar (sucrose) considering a plant located in Germany. Initially, sucrose is hydrolyzed into glucose and fructose, which are converted to sorbitol. Sorbitol is then reacted in condensation section forming p-Xylene.
This report analyses the economics of an integrated plant producing Polybutadiene from glucose in the United States. In this process, glucose is converted to butadiene via a direct aerobic fermentation process similar to the one proposed by Global Bioenergies. Then, the butadiene is polymerized to polybutadiene via a typical solution process.
This report analyses the economics of an integrated plant producing Polybutadiene from raw sugar in Germany. In this process, raw sugar is hydrolyzed to glucose and fructose (invert sugars), which are fermented to butadiene via a direct aerobic fermentation process similar to the one proposed by Global Bioenergies. Then, the butadiene is polymerized to polybutadiene via a typical solution process.
This report presents the economics of 1,3-Propanediol (PDO) production from glucose syrup using a fermentation process similar to the one developed by DuPont. The economic assessment assumes a plant located in the United States.
This report presents the economics of the production of 1,3-Propanediol (PDO) production from crude glycerol using a fermentation process in the United States. The microorganism used is Klebsiella pneumoniae.
This study approaches the economics of 1,3-Propanediol (PDO) production from raw sugar using a fermentation process similar to the one developed by DuPont. Raw sugar is used as the feedstock, being first hydrolyzed to glucose and fructose (invert sugars), which are then fermentated to produce PDO.
This report analyses the economics of bio-based Succinic Acid production from glucose syrup in the United States, using a fermentation process similar to Myriant process.
This report examines the costs related to bio-based Succinic Acid production from glucose syrup in the United States. The process examined in this report is similar to Reverdia fermentation process.
It presents the economics of bio-based Succinic Acid production from glucose syrup in the United States using a process similar to BioAmber fermentation process.
This report examines the costs related to bio-based Succinic Acid production from glucose syrup in the United States, using a fermentation process similar to Michigan Biotechnology Institute (MBI) process. In this process, glucose is initially fermented to produce Succinic Acid, which is recovered by electrodialysis from the fermentation broth.
This study presents the economics of bio-based Succinic Acid production from raw sugar in Germany using a fermentation process similar to Reverdia process. Raw sugar (sucrose) is hydrolyzed to glucose and fructose (invert sugars), which are fermented to Succinic Acid.
This report presents the economics of bio-based Succinic Acid production from raw sugar in Germany, using a fermentation process similar to Myriant process. Raw sugar (sucrose) is hydrolyzed to glucose and fructose (invert sugars), which are fermented to Succinic Acid. The product is obtained via crystallization. Ammonium sulfate is generated as by-product.
This study presents the economics of bio-based Succinic Acid production from raw sugar in Germany, using a fermentation process similar to BioAmber process. Raw sugar (sucrose) is hydrolyzed to glucose and fructose (invert sugars), which are fermented to Succinic Acid. The product is obtained via crystallization.
This study presents the economics of bio-based Succinic Acid production from raw sugar in Germany, using a fermentation process similar to Michigan Biotechnology Institute (MBI) process. Initially, raw sugar is hydrolyzed into invert sugars. The invert sugars are then fermented to produce Succinic Acid, which is recovered from the fermentation broth by electrodialysis.