شماره مدرك :
8608
شماره راهنما :
7989
پديد آورنده :
صفري، فاطمه
عنوان :

مدلسازي، شبيه سازي و بهينه سازي حرارتي برج هاي تقطير مزدوج حرارتي

مقطع تحصيلي :
كارشناسي ارشد
گرايش تحصيلي :
فرايندهاي جداسازي
محل تحصيل :
اصفهان: دانشگاه صنعتي اصفهان، دانشكده مهندسي شيمي
سال دفاع :
1392
صفحه شمار :
يازده،66ص.: مصور،جدول،نمودار
يادداشت :
ص.ع.به فارسي و انگليسي
استاد راهنما :
ارجمند مهرباني
استاد مشاور :
محسن نصر اصفهاني
توصيفگر ها :
مصرف انرژي , انتگراسيون حرارتي
تاريخ نمايه سازي :
18/12/92
استاد داور :
احمد محب، مسعود حق شناس فرد
دانشكده :
مهندسي شيمي
كد ايرانداك :
ID7989
چكيده فارسي :
به فارسي و انگليسي: قابل رويت در نسخه ديجيتالي
چكيده انگليسي :
Modeling Simulation and Thermal Optimization of Thermally Coupled Distillation Columns Fatemeh Safari f safari@ce iut ac ir Date of Submission 2014 01 20 Department of Chemical Engineering IsfahanUniversity of Technology Isfahan 84156 83111 Iran Degree M Sc Language Farsi Supervisor Arjomand Mehrabani Arjomand@cc iut ac ir Abstract Distillation is one of the most important and common operations in chemical and petrochemical industries Despite all of its advantages distillation units are responsible for a price of energy make scientists try to find solutions to reduce energy consumption of distillation Heat integration of thermally coupled distillation column is one of the best methods Two columns with different pressures are used in this construction columns are integrated such that the condensing duty of high pressure column is used to boil the low pressure column This work provides a comparison between two simple columns with direct configuration and thermally coupled distillation column with direct sequence backward integration arrangement for separation of a water methanol and dimethyl ether mixture based on energy consumption and cost The influence of changing numbers of first and second column trays on heating and cooling rate of each column are investigated based on a developed mathematical model using conservation law of mass and energy and bubble point method The average relative error between calculated and industrial temperatures in some trays is about 0 996 According to simulation the thermally coupled construction saves energy about 50 more than two simple columns but increase about 6 capital cost Since steam is not used in high pressure columns in thermally coupled distillation operating cost decrease about 20 too Keywords Distillation Energy consumption Heat integration Thermally Coupled distillation
استاد راهنما :
ارجمند مهرباني
استاد مشاور :
محسن نصر اصفهاني
استاد داور :
احمد محب، مسعود حق شناس فرد
لينک به اين مدرک :

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