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Solutions - Advanced Process Licensing Solutions
Is there a route for post-treating gasoline with minimal octane loss?
For the post-treatment of FCC gasoline, fixed-bed HDT is by far the most trusted solution because of its low capex, its ease of operation, and its flexibility.
Hydrogen consumption is higher than we would like in our raw diesel hydrotreater. Can we lower it without loss of throughput?
Hydrogen consumption in a hydrotreater comes from hydrotreatment reactions but also from losses within the process.
Solids in the feed are causing corrosion and erosion problems in our amine system. How do we remove them effectively and economically?
In order to ensure that there are no solids in the amine system, Axens recommends an amine filtration package which filters a slipstream of the lean amine to remove solid particles. The amine filtration package also includes an activated carbon filter for hydrocarbon elimination and a polishing filter to remove any charcoal fines.
What steps do we need to take to keep our sour water stripper at peak performance following a shutdown?
Shutdown operations of the sour water stripper unit should maximise the removal of H2S and NH3 from water, especially for long duration shutdowns, to minimise the safety concerns and corrosion issues during maintenance. If the sulphur recovery unit is not available, the sour gas should be routed to flare, then start the shutdown by decreasing the sour water feed to the unit manually and slowly.
How can we minimise gas and coke make with heavy feed to our FCC?
Catalytic systems towards better coke and/or dry gas selectivities will certainly help, especially to face contaminant metals which catalyse side reactions. If not limited by catalyst circulation, low delta coke catalysts will increase cat/oil but coke yield should stay constant.