Dehydrogenation of alkylene glycol ethers to ether detones and aldehydes
A technology of alkylene glycol ether and propylene glycol methyl ether, which is used in the field of catalytic dehydrogenation of alkylene glycol ether to prepare ether ketone and ether aldehyde, and can solve problems such as inconvenience
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Embodiment 1
[0021] The hydrogenation reaction is carried out in a stainless steel fixed bed reactor. A copper chromite catalyst (4.1 kg, Cu-0203-T, product of Engelhard Company) was charged into the reactor. The catalyst is activated with a mixture of hydrogen and nitrogen. To drive off moisture and air, the catalyst bed was heated to 150°C and maintained at this temperature for 5-8 hours under a nitrogen flow at a rate of 500 L / hr. Hydrogen is then added to the reactor. The reaction is exothermic so hydrogen addition is slow initially at a rate of 1.0-1.5% of the nitrogen flow rate. As the reaction continued, the concentration of hydrogen was gradually increased so as to control the temperature not to exceed 170°C. The hydrogen concentration reached 100% at the end of the reaction.
[0022] A mixture of 40% by weight water and 60% by weight propylene glycol methyl ether was fed into the reactor at a weight hourly space velocity (WHSV) of 1.1. The temperature of the reactor was maint...
Embodiment 2
[0024] Example 1 was repeated, but using a mixture of 20% by weight water and 80% by weight propylene glycol methyl ether. At this steady state, the conversion of propylene glycol methyl ether was 37.5%, and the selectivity to methoxyacetone was 85.4 mol%.
Embodiment 3
[0026] Example 1 was repeated, but using a mixture of 10% by weight water and 90% by weight propylene glycol methyl ether. At this steady state, the conversion of propylene glycol methyl ether was 34%, and the selectivity to methoxyacetone was 75.2 mol%.
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