Operation of diesel stripping tower
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What operating temperature, pressure, and steam volume (feed rate) should be used in the diesel stripping tower to ensure that copper corrosion in the naphtha is within acceptable limits? ?
Copper sheet corrosion isn’t caused by this operation, right? Our system is unable to control copper sheet corrosion; the stripping tower merely removes hydrogen sulfide from the oil products. Of course, that also plays a role, but it’s not the ultimate determining factor.
It seems that this parameter is not a fixed value, but rather is optimized based on your test results and the calculation of your yield
The key issue is that the hydrotreated naphtha produced via diesel hydrogenation fails the copper corrosion test
The key issue is that the hydrotreated naphtha produced via diesel hydrogenation fails the copper corrosion test
It’s still the case that your response isn’t thorough enough
The sulfur content is not high, so it’s probably not due to incomplete reaction
The sulfur content is not high, so it’s probably not due to incomplete reaction
The sulfur content is not high, so it’s probably not due to incomplete reaction
The product from the top of the distillation column in the hydrogenation unit suffers from unacceptable corrosion.