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This report presents the economics of Acrylic Acid production from 3-hydroxypropionic acid (3-HP). 3-HP is submitted to a dehydration reaction to generate Glacial Acrylic Acid. The reaction is carried out in vapor phase in a reactor column. The economic analysis approaches a plant located in the United States.
This study reviews the economics of a process for Ester-Grade Acrylic Acid (EAA) production from acetylene. The process examined involves a catalytic carbonylation of acetylene to produce Acrylic Acid similar to BASF. The economic analysis performed is based on a plant constructed in the United States.
This study presents the economic analysis of Ester-Grade Acrylic Acid (EAA) production from ethylene oxide in the United States using a carbonylation process similar to Novomer process. In this process, ethylene oxide is catalytically carbonylated to beta-propiolactone intermediate, which is then converted to Acrylic Acid.
It presents the economics of Ester-Grade Acrylic Acid (EAA) production from crude glycerol in the USA using a two-step process similar to Arkema technology. In the process examined, crude glycerol, obtained from biodiesel plants, is dehydrated to acrolein, which is subsequently oxidized to Acrylic Acid.
This report presents the economics of Ester-Grade Acrylic Acid (EAA) production from natural gas in the United States. Initially, methane in the natural gas feed is cracked to acetylene which is reacted carbon monoxide generated by feed combustion, yielding Acrylic Acid.
This report presents the economics of Ester-Grade Acrylic Acid (EAA) production from propane in the United States. Initially, propane undergoes oxydehydrogenation in the presence of steam to form propylene, which is then oxidized in vapor phase to generate acrylic acid.
This report presents the economics of Ester-Grade Acrylic Acid (EAA) production from chemical grade (CG) propylene in a plant located in the United States. The process consists in a two stage vapor-phase oxidation of propylene, yieding Acrylic Acid, which is then purified to obtain the Ester-Grade product.
This report shows a feasibility study of bio-based Acrylic Acid production from glucose syrup in a plant assumed to be located in the United States. The process is based on the fermentation route of glucose, yielding Acrylic Acid, similar to the speculative process proposed by the Delft University of Technology.
This report presents the economics of bio-based Acrylic Acid production from glucose syrup in the United States using a fermentation process similar to Cargill process. Initially, glucose is fermented to produce 3-hydroxypropionic acid (3-HPA), which is then dehydrated to produce Acrylic Acid.
This report shows a feasibility study of bio-based Acrylic Acid production from glucose syrup in a plant assumed to be located in Germany. The process is based on the fermentation route of raw sugar, yielding Acrylic Acid, similar to the speculative process proposed by the Delft University of Technology.
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 presents the costs associated with the construction of an industrial plant, in the United States, for crude acrylic acid purification to produce Glacial Acrylic Acid. The purification process examined is based on crude acrylic acid crystallization.
This analysis presents the costs associated with the construction of an industrial plant in the United States, for crude acrylic acid purification via distillation to produce Glacial Acrylic Acid.