Let's talk about #Syngas plants and #sulfurpoisoning (with a focus on the #primaryreformer or #SMR) with Anton Kariagin, one of Clariant's syngas subject matter experts. To avoid sulfur breakthrough in the first place: 🌟 Monitor your desulf. section - check sulfur in/out, track sulfur pick-up compared to the maximum amount your bed can handle 🌟 If you're using Clariant's service portal CLARITY®, consider using this tool to help you monitor your bed But, we all do everything we can and inevitably sulfur breakthrough downstream may occur. What happens if you have sulfur coming in to your plant? This is configuration dependent but the main reactors to worry about are: 🌟 Pre-reformer and/or the primary reformer 🌟 Low temperature shift (LTS) On the primary reformer #catalyst, sulfur lays down on the catalyst which blocks active sites. When this happens, the heat is not pulled away from the tube walls (as it normally is from the endothermic reaction of reforming) and you may visually see hot banding or hot spots on the tubes (these visually look like brighter spots on your tubes). On the LTS catalyst, sulfur is a permanent poison. So what can we do? For the primary reformer you can: 🌟 Monitor tube wall temperatures - operating too hot or above design severely impacts tube life. 🌟 Consider a steam-out to help regenerate the catalyst and remove the carbon formation. Excessive steaming can negatively impact catalyst activity so you want to balance steam and carbon removal but not do it too long or too frequently. 🌟 For severe poisoning, you can consider a steam/air regeneration. Has anyone had success regaining primary reformer catalyst activity after a sulfur poisoning event? What method did you use to regain activity? What reasons did you see sulfur poisoning in your plant? #neverstoplearning #ammonia #hydrogen #methanol #Clariant
Thanks for sharing
Good point! Anton Kariagin Karen Braden, PE
Thanks for sharing. Actually the catalyst absorptive capacity is known and hence the catalyst supplier can predict the life time of the batch, considering the average sulfer concentration in feed gas and the gas flow rate to Desulfurizer at full plant rate. However, I have seen catalyst bed replacement because of high DP. This could happen if desulfurizer bed temperature exceeds 400 - 410 oC for long durations especially at start up conditions, leading to long-chain carbon formation. One question I would like to ask please, Is sulfur poisoning of primary reformer catalyst is reversible ! I would like to hear from Mr. Anton. Thank you
What went wrong,why sulphur breakthrough ? Please share Root Cause ?
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