How to design the gas distributor in a Klaus reactor? I hope you will kindly offer your guidance
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How should the gas distributor in a horizontal Claus reactor be designed? Moreover, when calculating the empty-bed gas velocity in a horizontal reactor, it involves dividing the process gas flow rate by the cross-sectional area; how should this cross-sectional area be determined? The cross-sectional areas of the Klaus horizontal reactor vary at different heights; I would be grateful for any guidance you could provide. Thank you very much!
This post was last edited by letitbe on 2017-6-19 10:37. Isn’t this the patent documentation for the European process package? Ask the patent holder directly, but I don’t think they’ll provide it to you
Are there any basic materials on this topic? No such materials could be found; instead, an image of a distributor was found, which is in the form of a semi-cylinder
Are there any basic materials on this topic? No such materials could be found; instead, an image of a distributor was found, which is in the form of a semi-cylinder
Are there any basic materials on this topic? No such materials could be found; instead, an image of a distributor was found, which is in the form of a semi-cylinder
Are there any basic materials on this topic? No information on this topic was found; instead, an image of a distributor was found, which is in the form of a semi-cylinder
Ask the technical supplier; the company used European technology before as well. The person who came to train us on driving is very strict regarding technical details – they refuse to answer questions that relate to aspects not covered in the technical documentation. Try communicating more with them; maybe they will tell you
Basic information? Regarding patented items, don’t assume that foreigners’ understanding of IP is the same as that of locals