Revamp of heat-integrated crude oil distillation systems for energy reduction and new product demands
Lu Chen, Megan Jobson, Robin Smith
Abstract
Lu Chen, Megan Jobson, Robin Smith
Abstract
An optimization-based design methodology for the retrofit design and analysis of heat-integrated crude oil distillation systems was proposed. The approach considers the distillation column and preheat train in a single framework and aims to improve the overall performance of the system. In the approach, distillation units were simulated using simplified models that allow the specification of the products, and the heat exchanger network was studied in terms of its detailed structure. The hydraulic constraints of the existing distillation column design were accounted for, and the existing numbers of stages in each section were considered. Simulated annealing was employed as the optimization algorithm because of its ability to optimize both structural and operational process variables. Case studies addressing the reduction of energy consumption in an existing heat-integrated atmospheric distillation column, and for improving profit by adjusting product yields according to market value were presented. This is an abstract of a paper presented at the AIChE Spring National Meeting (New Orleans, LA 4/6-10/2008).
OpenAlex reports 2 citations for this work. Citation counts describe recorded attention and do not establish research quality.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
An optimization-based design methodology for the retrofit design and analysis of heat-integrated crude oil distillation systems was proposed. The approach considers the distillation column and preheat train in a single framework and aims to improve the overall performance of the system. In the approach, distillation units were simulated using simplified models that allow the specification of the products, and the heat exchanger network was studied in terms of its detailed structure. The hydraulic constraints of the existing distillation column design were accounted for, and the existing numbers of stages in each section were considered. Simulated annealing was employed as the optimization algorithm because of its ability to optimize both structural and operational process variables. Case studies addressing the reduction of energy consumption in an existing heat-integrated atmospheric distillation column, and for improving profit by adjusting product yields according to market value were presented. This is an abstract of a paper presented at the AIChE Spring National Meeting (New Orleans, LA 4/6-10/2008).
Key concepts: Distillation, Heat exchanger, Process engineering, Fractionating column, Heat recovery ventilation, Computer science, Engineering, Mechanical engineering