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It presents the economics of bio-based Succinic Acid production from crude glycerol in the United States, using a fermentation process similar to Succinity process. In this process, crude glycerol (at 85 wt% purity) obtained as by-product of biodiesel plants is used as raw material. After purification, glycerol is fermented to produce Succinic Acid.
This report presents the economics of Biodiesel production from soybean oil in the United States using a typical alkaline catalysis process. In this process, the triglycerides in the oil are reacted with methanol to make methyl esters. Crude glycerol is also obtained and purified, generating pharmaceutical grade glycerol as by-product.
This report presents the economics of Biodiesel production from soybean oil in the United States using a typical alkaline catalysis process. In this process, the triglycerides in the oil are reacted with methanol to make methyl esters. Crude glycerol is also generated as by-product.
This report provides an economic analysis of Biodiesel production from soybean oil in the United States via transesterification using a catalytic distillation technology.
This feasibility study assesses the economics of Biodiesel production from soybean oil considering a plant located in the United States. This process is a heterogeneous catalysis process similar to Axens Esterfip-H process. Crude glycerol is also produced in this process, being purified to generate pharmaceutical grade glycerol as by-product.
This feasibility study assesses the economics of Biodiesel production from soybean oil considering a plant located in the United States. This process is a heterogeneous catalysis process similar to Axens Esterfip-H process. Crude glycerol is generated as by-product.
This study presents a techno-economic analysis of Biodiesel production from soybean oil in the United States via transesterification using a supercritical fluid technology.
Economics of Biodiesel production from algae in the USA. The process examined comprises three main steps: algae cultivation; lipids extraction; and transesterification of lipids. Crude glycerol is generated as by-product.
This report presents the economics of Bisphenol A (BPA) production in the United States via a condensation reaction of acetone with phenol catalyzed by hydrogen chloride.
This report presents a techno-economic analysis of Bisphenol A (BPA) production in the United States, via a process similar to Dow's QBIS technology. In this process, BPA is produced by the reaction of acetone with phenol catalyzed by a cation-exchange resin.
This report presents the economics of a typical Bronopol production process from sodium hydroxide, calcium chloride, nitromethane, and liquid bromine in the United States.
In this study, the process reviewed is a typical aromatization process producing a mixture of Benzene, Toluene and Xylenes (BTX) from ethane. In this analysis, ethane is first dehydrogenated to ethylene, which is oligomerized. The oligomers then cyclize to form naphthenes. They are finally dehydrogenated, yielding aromatics. The economic assessment assumes a plant located in the United States.
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.
This report concerns the bio-based BDO production in the Germany from raw sugar. In this report, BDO is produced using a two-step process similar to Myriant/JM Davy technology. In this process, raw sugar is hydrolyzed into glucose and fructose (invert sugars). The invert sugars are fermented to produce to succinic acid, that is then hydrogenated to BDO. Ammonium sulfate and tetrahydrofuran (THF) are generated as by-products.
This report presents the economics of an 1,4-Butanediol (BDO) production process from acetylene and formaldehyde in the United States. In this process, acetylene initially reacts with formaldehyde by addition, forming 1,4-butynediol. The butynediol is then hydrogenated to produce BDO. It is a typical acetylene-based Reppe process.
This assessment examines a technology similar to the process proposed by Mitsubishi Chemical for 1,4-Butanediol (BDO) production from butadiene (BD) in the United States. In this process, BDO is produced from BD via acetoxylation.
This report presents an economic analysis of 1,4-Butanediol (BDO) production from maleic anhydride in the United States using a process similar to the one proposed by JM Davy. Initially, maleic anhydride is reacted with methanol to produce dimethyl maleate (DMM). The DMM is then hydrogenated to BDO.
This feasibility analysis is about 1,4-Butanediol (BDO) production from propylene in the United States using an allyl alcohol process. Initially, propylene is reacted with acetic acid and oxygen, producing allyl acetate. The allyl acetate is then hydrolyzed, yielding allyl alcohol. Finally, the allyl alcohol is converted by hydroformylation and hydrogenation to BDO.
This report shows a techno-economic analysis related to the construction of a plant in the United States for 1,4-Butanediol (BDO) production from propylene oxide using a process similar to LyondellBasell. Initially, propylene oxide is isomerized to allyl alcohol. The allyl alcohol then reacts with syngas, generating 4-hydroxybutyraldehyde, which is finally hydrogenated to BDO.
This feasibility study examines 1,4-Butanediol (BDO) production from succinic acid in the United States using a hydrogenation process similar to the one proposed by BioAmber.
This study analyzes the costs for n-Butanol production from butyraldehyde. In this process, n-butyraldehyde is hydrogenated generating n-Butanol. The economic analysis is based on a plant constructed in the United States.
The report shows an economic analysis of the construction of an industrial plant in the United States for n-Butanol production. In the process reviewed ethanol is dimerized into n-Butanol via the Guerbet reaction. This reaction is composed by dehydrogenation, aldol condensation and hydrogenation.
This report presents an economic analysis of n-Butanol production from propylene and syngas, assuming a plant located in the United States. The process under analysis is similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. This process comprises hydroformylation of propylene and n-butyraldehyde hydrogenation.
This report presents the economics of Butenes production from ethylene using a dimerization process similar to Lummus process. In the process under analysis, gasoline and fuel oil are generated as by-products. The economic analysis assumes a plant constructed in the United States.
This report shows the economics of Butenes production from propylene via a metathesis process. In the process examined, propylene is converted to butenes and ethylene is generated as by-product. The economic assessment assumes a plant located in the United States.
This report approaches the production of n-Butyl Acrylate from acrylic acid and n-butanol. The process examined is similar to the Synthomer's Butyl Acrylate Process. In this process acrylic acid and n-butanol are directly converted to Butyl Acrylate via an esterification reaction catalyzed by p-Toluene Sulfonic Acid. The economic analysis performed assumes a plant located in the United States.
This study concerns the production of n-Butyl Acrylate, starting from propylene and n-butanol. Chemical grade propylene is oxidized to acrolein and then to acrylic acid, which is then fed to an esterification reaction, along with n-butanol to generate Butyl Acrylate. The economic analysis performed is based on a plant located in the United States.
This feasibility study approaches n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly developed by JM Davy and Union Carbide, employing Selector 10 catalyst. The production ratio of n- to iso-butyraldehyde is about 10.
This report presents an economic analysis of n-Butyraldehyde production from propylene and syngas, assuming a plant located in the United States. The process under analysis is a propylene hydroformylation similar to the LP OXO technology jointly licensed by JM Davy and Dow, employing Selector 30 catalyst. The production ratio of n- to iso-butyraldehyde is about 30.
This report concerns the costs associated with the production of n-Butyraldehyde from propylene and syngas. The process under analysis is a propylene hydroformylation similar to the technology jointly developed by Rhodia (former Rhône-Poulenc) and Ruhrchemie. The economic analysis presented assumes a plant located in the United States.
This report approaches an economic analysis of LAO production from ethylene in the United States. The process examined in this report produces C4 to C12+ linear alpha-olefins via ethylene oligomerization, following a process similar to DuPont Versipol process.
This report presents the economics of LAO production from ethylene in the United States. In this case, C4 to C12+ linear alpha-olefins are obtained via a process similar to Alpha-SABLIN process (jointly developed by SABIC and Linde). This process employs a bubble-column type reactor in which a homogenous catalyst system is introduced together with a solvent.
This study presents a techno-economic analysis of LAO production from ethylene in the United States. In this report, a process similar to INEOS process is analyzed, producing linear alpha-olefins ranging from C4 to C16+, mainly C6 to C10. Ethylene oligomerization is carried out in a reaction with triethylaluminum produced on site, increasing the chain of the alkyls bonded aluminum.
This feasibility study presents an economic analysis of Linear Alpha Olefins (LAO) production from ethylene in the United States. The process presented is similar to Shell Higher Olefins Process (SHOP) in which LAOs ranging from C4 to C18 are obtained. This process comprises three steps: oligomerization, isomerization and disproportionation.
This report provides the economics of Linear Alpha Olefins (LAO) production from ethylene in the United States. The process examined in this report produces LAOs ranging from C4 to C30+ using a process similar to Chevron Phillips process. Ethylene is initially submitted to oligomerization, and this reaction effluent is subjected to a transalkylation reaction.