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Hello everyone. Our unit is a heavy oil catalytic cracking plant with a capacity of 2 million tons per year, featuring a coaxial reactor and regenerator. It was originally designed with a single lift pipe for heavy oil, but an additional lift pipe for light oil was added to the reactor as part of later modifications. Recently, due to the light nature of the raw materials, low bed temperature, and low air volume, a bias in the bed has also occurred. To increase the main lift volume, oil slurry reprocessing is put into use (a process was designed for this purpose but has never been utilized before); this process involves mixing the oil slurry with the feed oil in the main lift pipe before it enters the feed oil nozzle. Our slurry solid content is 6–9 g/l, and the reprocessing ratio of the recycled oil is 7–9% (with a solid content of 2–3%). I would like to know what the advantages and disadvantages are of feeding this slurry back into the feed oil nozzle of the main lift pipe What issues should be considered in process adjustments?
There are actually quite a few similar discussions on this topic in the forum; for example: Can oil sludge be reprocessed? The functions and negative effects of re-smelting: https://bbs.hcbbs.com/forum.php?mod=viewthread&tid=915738&shareuid=398787. The poster should also learn to utilize the forum’s search function and search for relevant keywords. For example: https://bbs.hcbbs.com/search.php?mod=forum&searchid=1171&orderby=lastpost&ascdesc=desc&searchsubmit=yes&kw=%BB%D8%C1%B6%D3%CD%BD%AC
Once again, make good use of search – it will get you twice the result with half the effort!
We have already started using mixed feeding; it’s not clear what impact this will have on the nozzles. After its implementation, the amount of charring has increased, and the distribution within the bed layer has improved somewhat.