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Propylene oxidation to acrolein example

After several years and millions of dollars were spent to develop a homogenous gas-phase oxidation process to produce propylene oxide, the development was terminated. This was a reaction classified as a [Pg.124]

Skipping the pilot-plant saved 1 to 2 million dollars and made it possible for the company to enter the acrylic market a full year ahead of the competition. It was assumed that the savings would be enough to pay for any changes in the production unit that might be needed. [Pg.125]

By this time, the construction of the production unit was underway, and in a great hurry a pilot-plant was constructed, the size of a single tube of the 4000 tube commercial reactor. Interestingly, when the glowing discharge [Pg.125]

Efficiency means component 1 made per component 3 converted, all in molar units. Data show that 89.7% of the converted propylene was accounted for by the formed acrolein. An additional 9.8% efficiency is indicated for acrylic acid. Efficiency to total useftil product was 99.5% as long as ignition of homogeneous reaction could be avoided [Pg.126]

The catalyst used for these studies was one that had been rejected by laboratory short tubular reactor experiments as a hotspot-type catalyst. This same type was recommended by another corporate lab with experience in catalyst formulations. The hotspot-type catalyst gave 3- [Pg.128]


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