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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.
It presents the economics of 1,3-Butadiene extraction from a crude C4s stream in the United States. The process examined in this report is similar to Nippon Zeon. In this process, dimethyl-formamide is used as a solvent in order to extract twice 1,3-Butadiene from the crude C4 stream.
This report analyses the economics of 1,3-Butadiene production from a crude C4s stream in the United States using an extraction process that uses N-methyl-2-pyrrolidinone (NMP) similar to BASF NMP. Raffinate-1 is generated as by-product in the process.
This study presents the economics of 1,3-Butadiene (BD) production from mixed butenes in a plant assumed to be erected in the United States. In this process, which is similar to TPC/UOP Oxo-D, butenes are catalytically dehydrogenated to produce the Butadiene product. Raffinate is obtained as by-product.
This report presents the costs associated with 1,3-Butadiene production from carbon monoxide in the United States using a process similar to LanzaTech/Invista. First, carbon monoxide (CO) is fermented forming 2,3-butanediol (BDO). Then, BDO is catalytically dehydrogenated to 1,3-Butadiene (BD).
This report examines the costs related to 1,3-Butadiene (BD) production from hydrous ethanol in the United States. This process consists of a two-stage reaction process. First, ethanol is converted to acetaldehyde, which is then reacted with ethanol to produce 1,3-Butadiene. Raffinate is generated as by-product in the process.
This report presents the economics of 1,3-Butadiene (BD) production from n-butane. In the process, n-butane undergoes a dehydrogenation reaction process similar to Lummus Catadiene, generating a C4s stream which is purified to obtain 1,3-Butadiene. The economic analysis is based on a plant located in the United States.