سال انتشار: ۱۳۸۶
محل انتشار: پنجمین کنگره بین المللی مهندسی شیمی
تعداد صفحات: ۴
Mohammad Mehdi shanazari – Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran
Farhad Shahraki – Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran
Mohammad Khorram – Department of Chemical Engineering, University of Sistan and Baluchestan, Zahedan, Iran
Distilation unit is used as a case study in this work. three units of this plant, atmospheric and vacuum units and S.R.G. unit, were focused to reduce energy consumption. Data and information are collected from Esfahan refinery and commercial simulation software, Aspen Tech provision is used to simulate unmeasured data and determine thermodynamic properties. Grand composite curve are used as tools to study the energy integration. Distillation unit consists of seven distillation columns, 21 hot and 10 cold streams. For this unit the optimum ∆Tmin determine 33◦C. According to process integration, the modification of Distillation unit can be achieved by adding new heat exchanger. Four heat exchanger were chosen to be used for unit. The maximum heat recovery can save about 9.2464% of overall energy consumption in furnace and cold utility consumption reduce.