Failure of the level sensor in the catalytic stabilization absorber led to water contamination in the stabilized gasoline, thereby deactivating the hydrogenation catalyst
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The failure of the level gauge in the catalytic stabilization absorber during winter leads to water contamination in the stabilized gasoline, which in turn causes deactivation of the hydrogenation catalysts; please be aware of this
Haven’t heard of it! Please explain in more detail; it seems impossible!
Is it the level sensor 301 in front of the absorption tower that has failed? Question: What is the difference between gasoline hydrogenation and diesel/hydrocarbon hydrogenation? I would like to learn about it*; thank you!
Does your catalytic gasoline reactor still require hydrogenation? I really can’t understand it. Is it about the stability of absorption in coking? If it’s catalytic gasoline, then your processing costs will increase. Is there a limit level for the absorption tower as well?
Capacity 301 unit; stable gasoline with 800 PPM sulfur – undergo hydrogenation
Wow, what kind of manufacturing process do you use for your devices? How is it possible to still have so much sulfur in stable gasoline? If the sulfur content in the raw material is too high, a sulfur transfer agent can be added. It’s expensive to hydrogenate catalytically stabilized gasoline
I still don’t understand. Under normal circumstances, there is a gas-liquid equilibrium tank in front of the absorber – at the outlet of the compressor. This tank contains condensed oil, which needs to be pumped into the stripping tower, not gasoline. Is your condensed oil sent for hydrogenation first?