Thread Content
This post was last edited by *amingteda on 2017-8-24 at 23:04. Dear fellow users, in order to help everyone learn the *ProII process simulation software better – so that beginners can gain knowledge and experienced users can refresh their skills – we are launching a series of activities titled “Making Progress Every Day” for learning the basics of ProII. Since I use Aspen Plus/Hysys on a regular basis and have not studied ProII software systematically, the knowledge I offer might be quite basic. I hope fellow users will provide valuable suggestions and opinions, and actively participate in the discussions. I have been working on revising my paper lately and don’t have time to post “Making Progress Every Day”; I am truly sorry to all my fellow netizens. I submitted the revised version today, and I can interact with all of you sea friends again on a daily basis. Multiple-choice question: 6. Which of the following statements about the shortcut distillation module is correct? A. The Fenske-Underwood-Gilliland shortcut method is used for the design of distillation columns. B. Calculate the minimum reflux ratio, the minimum number of theoretical plates, the number of theoretical plates at a given reflux ratio, and the location of the feed plate based on the specified feeding conditions and separation requirements. C. It is useful to first carry out a simplified distillation calculation before proceeding with rigorous, board-by-board calculations, as the preliminary calculation can provide you with a basic idea of what is reasonable. D. Model parameters include: condenser/reboiler, minimum reflux ratio, specifications for separation requirements, Fenske estimates, and product estimates.