Shell gasification
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I am working on my graduation project related to coal-to-methanol production. The gasification technology used is Shell’s pulverized coal gasification method, and what needs to be done now is the calculation for Shell’s coal gasification process, primarily focusing on material balance. How should I proceed with this? ? No relevant information available: (
There is too much information available on this topic; it would be useful to list the data needed for material balance, so that everyone can provide some helpful suggestions
It seems there’s a graduation thesis on gasification for methanol production by that swordsman; give it a look
At present, there is only 1 million tons of coal powder, and this figure can change depending on the circumstances during the production process. In short, there is only one piece of data now: the amount of coal powder
For other unknown data, one can either provide them themselves or refer to the standards: (
Is the swordswoman Baba Ma of the Taoists? I don’t understand what you mean:o
Actually, I also recommend that you refer to relevant papers; the data I can provide here might not be suitable. For example, for a shell furnace with an annual methanol production capacity of 500,000 tons, the coal consumption is around 2,000 tons per day. Information related to this type of furnace has been discussed many times by experienced users on this forum, so you should take a look there
Most of the information about this thing is classified! Many of the experts on this forum work with SHELL, and I do the same! {:3_47:}The calculations for SHELL can be done using existing methods; it mainly depends on what your design requirements are!
Some information on the material balance for Shell gasification has been found; now it’s necessary to use CAD to draw the structural diagram (or assembly diagram) of the Shell gasifier. All that’s required is to create the diagrams based on the existing ones, and mastering that process will suffice. From the information I’ve seen, the coal feed rates for Shell gasifiers in China are 1,000 t/d and 2,000 t/d; it’s sufficient to illustrate just one of these values. Of course, some design-related information for the Shell gasifier is also needed; there must be one’s own design calculation process. The current task is the selection and design of a Shell gasification furnace; I’m not sure how to proceed at the moment. : ( Can I add you on Penguin? My 1371989278