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Methanol synthesis via methyl formate in the liquid phase

Thesis/Dissertation ·
OSTI ID:7035152

An alternative route of synthesizing methanol from hydrogen and carbon monoxide, methanol synthesis via methyl formate, was studied. This synthesis route basically involves two reactions, carbonylation of methanol to methyl formate and hydrogenolysis of methyl formate to methanol. These two reactions are studied separately and jointly in the liquid phase. A carbonylation rate equation using potassium methoxide as the catalyst and a hydrogenolysis rate equation using a manganese promoted copper chromite (Cu/Cr/Mn) catalyst are developed. The effect of operating conditions and some chemicals on these reactions are investigated. The two-step reaction route to produce MeOH is not superior to the current industrial route-direct synthesis of H{sub 2} and CO to MeOH. Thermodynamic and kinetic studies are made for carrying out the two reactions concurrently in a single slurry reactor using both catalysts. The concurrent methanol synthesis has many advantages over the current industrial gas phase methanol synthesis; among them are high synthesis rate, low reaction temperature, little or no synthesis gas recycle and high rate of heat removal from the reactor. The concurrent synthesis has advantages over the two-stage process (carrying out the two reactions separately): it uses less equipment, the carbonylation catalyst is more tolerable to CO{sub 2} and H{sub 2}O; the hydrogenolysis catalyst is more tolerable to CO and CO{sub 2}. An interaction between the two catalysts is founded. A major problem using Cu/Cr/Mn catalyst in the concurrent synthesis is a slow decrease in activity with time. A barium promoted copper chromite catalyst (Cu/Cr/Ba) was found to have similar activity and was more stable than the Cu/Cr/Mn catalyst.

Research Organization:
Pittsburgh Univ., PA (USA)
OSTI ID:
7035152
Country of Publication:
United States
Language:
English