Search for a Commodity and Check Solutions Offered
Refine Results
Results 1 - 4 of 4
In this report, it is approached the economics of Isopropyl Alcohol production from acetone in a typical acetone hydrogenation process, also assuming an industrial plant located in the United States. The reaction is carried out in liquid phase, in two fixed bed reactors in series, catalyzed by a Raney nickel catalyst.
This report approaches the economics of Isopropyl Alcohol production from Polymer Grade (PG) Propylene. This study is based on a plant located in the United States. Isopropyl Alcohol is obtained via a typical direct propylene hydration process which is carried out in the vapour phase using phosphoric acid on silica as catalyst.
This report presents an economic analysis of an integrated unit for producing Isopropyl Alcohol from propane in the United States. In a first unit, propane is converted to propylene via propane dehydrogenation. The propylene obtained is then converted to Isopropyl Alcohol via vapor phase hydration over a catalytic bed of phosphoric acid on silica.
This report presents the economics of Isopropyl Alcohol production from refinery grade (RG) propylene via a typical indirect propylene hydration process. In this process, RG propylene reacts with sulfuric acid to form isopropyl alcohol sulfates. Those sulfates are then reacted with water to form Isopropanol. The study assumes a plant located in the United States.