کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
687285 | 1460114 | 2013 | 7 صفحه PDF | دانلود رایگان |

Multi-component separation by distillation is known as a conventional method in chemical processes. In this study the effects of feed splitting on three classical arrangements (with and without heat integration) were investigated in order to reduce the total annual cost (TAC). Ternery mixture separation (propane, butane and pentane) by distillation was selected as a case study. An optimization problem was defined based on the effective parameters affecting the total annual cost. Optimum values for decision variables were calculated by applying the genetic algorithm. Calculation results showed that the heat integration procedure in the feed splitting method reduced the TAC significantly. It was also indicated that the prefractionator arrangement with heat integration resulted in the greatest decrease in the total annual cost.
► Effect of the feed splitting and heat integration in the ternary mixture were investigated.
► Three classical arrangements were considered and analyzed.
► Feed splitting prefractionator with heat integration was selected as best arrangement.
Journal: Chemical Engineering and Processing: Process Intensification - Volume 63, January 2013, Pages 37–43