Start-up process for the production of glycols
A diol and catalyst technology, applied in the field of start-up procedures, can solve problems such as reducing catalyst performance, reducing product yield, and operating confusion
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Embodiment 3
[0059] Example 3: Stabilization of Tungsten in Solution
[0060]0.5 grams of 1.2 wt% Ru / C (RX3-extra) (3-80 mesh) hydrogenation catalyst was loaded into the reactor. The catalyst was reduced in a reactor at 300° C. for 1 hour under H2 flow (3 NL / min) at atmospheric pressure (absence of liquid). After catalyst reduction was complete, the temperature was lowered to 230°C and the pressure was raised to 100 bar. Water was fed into the reactor at a rate of 60 g / L until steady state operation was obtained. Without changing the feed rate of liquid or gas, the water feed was switched to a mixture containing 1 wt. Reactive aqueous solution. These conditions were similar to the experiments described in Comparative Examples 1 and 2 (except glucose and buffer in the feed).
[0061] The reaction was carried out for 115 hours. When the water wash was complete, the pH stabilized at ~5. After switching to the aqueous reaction solution, a drop in pH was observed. The pH stabilized at a ...
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