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This post was last edited by akzo2008 on 2009-9-9 at 11:24. Let’s exchange ideas. We use a parallel high-low configuration with a processing capacity of 1.4 million tons; in terms of operation, the slide valve often needs to be kept at a wide opening. For dealing with accidents, it seems that the regenerator’s bed clogging issue is less of a problem in this configuration compared to the coaxial type. However, one technician said that the coaxial type is easier to operate, especially since switching and adjusting the plug valves is simpler. Could everyone share how they feel? I would really like to exchange ideas with those who have experience in both types of operations. Hehe, I’m only experienced with one of them, so I’m eager to hear everyone’s opinions :) Some devices are introduced here for reference; it can be seen that parallel and coaxial types are more common, while others are less so: http://bbs.hcbbs.com/thread-530675-1-1.html
The forum has discussed this before; all 3 types of catalytic cracking have been encountered. It seems that from an operational perspective, the coaxial design is simpler, while the side-by-side arrangement is relatively more complex; In terms of processing capacity (operational flexibility), being at the same level high or low has certain advantages ; In terms of equipment usage, the faults and problematic operating conditions of plug valves represent the weaknesses of the coaxial design ; In terms of investment costs, coaxial investments require relatively less land.
This post was last edited by chengkang on 2009-9-9 22:12. With coaxial plug valves, they tend to become eccentric over time and thus fail to close properly; in an emergency situation, it is not possible to disconnect the two components. In terms of the charring effect, having both high and low settings gives better results, with lower carbon content. For our two catalytic systems, the liquid yield at the high and low settings is somewhat higher. Normal operation; it’s simple for coaxial connections. (Our two regenerators at different heights are connected in series, involving coking distribution and level control)
Changing a U-shaped tube into a straight one is presumably a very well-established process; I don’t see why anyone would still use U-shaped tubes
Each has its advantages. Which specific format to choose depends largely on the preferences of the design and production teams.
I think, from a safety perspective, the stacked design is safer than the coaxial design, but in terms of operation, the coaxial design is easier to control!
This post was last edited by chengkang on 2009-9-9 22:14. Once you’re proficient in both coaxial and parallel operations, it makes no difference as long as the instruments work well. 1# akzo2008