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رسائل ماجيستير الانجليزية 2014 0e1947fd-0e66-437e-a81e-9d94a9359e12

Determination of the Optimum Heat Recovery Approach Temperature for an Existing Heat Exchanger Network of Crude Distillation Unit

Salih Mohamed Ahmed, Abdelbagi Osman Elsiddig , Kawther Abdelgader Ahmed Ebnoff

كلية الهندسة والتكنولوجيا-جامعة الجزيرة · السودان

الموضوعات

علوم تطبيقية وتكنولوجية

الملخص

Energy conservation and optimization is an important method in chemical process industry. From industrial industry facts, the calculation of minimum heating and cooling requirements reveal significant energy savings. This studyaddressesthedetermination of optimum process to process heat exchange at minimumHeat Recovery Approach Temperature (HRAT) for an existing heat exchanger network. The study is applied according to the Pinch Technology concepts on the most common heat exchanger network (HEN) which isthe crude preheat train unit. Minimum heating and cooling requirements were determined for such HEN after excessive heat load shifting using five utility paths combination options at different HRAT values.A minimum HRATcorresponds to the optimum total cost has been determined for each paths combination and found to range between 8oC to 14oC.Then a complete economical analysis was conducted for each option to decide and pick up the most optimum. Such economical evaluation involved the determination of capital investment for the minor retrofit of HEN and the expected energy savings. From investment and savings, the payback period has also been calculated for each option and found to range between 0.5 to2.5 years. Two options were found to be the best but having critical argument and trade-offto choose the optimum from them. Both of them are showing great energy savings and moderate investment with little time of payback spam. However, the optimum readings of one of these options was at 8oCHRAT which considered to be small and might restrict the process of heat transfer. Based on this study, it is recommended to consider HEN streams and exchangers pressure dropfor further study.

التعريف والنوع

رقم الوثيقة
0e1947fd-0e66-437e-a81e-9d94a9359e12
رقم العقد
0
نوع الوسائط
Crawler
نوع المحتوى
الرسائل العلمية
صيغة المصدر
رسائل ماجيستير
نوع الملف
pdf text
أسماء الملفات
71774_1.pdf

بيانات النشر

ألقاب المؤلفين
[{"name_ar":" Salih Mohamed Ahmed","title_ar":"اشراف","title_en":"Supervision"},{"name_ar":"Abdelbagi Osman Elsiddig ","title_ar":"اشراف","title_en":"Supervision"},{"name_ar":"Kawther Abdelgader Ahmed Ebnoff ","title_ar":"اعداد","title_en":"Preparation"}]
اللغة
English

المصدر والدورية

اسم المصدر
Determination of the Optimum Heat Recovery Approach Temperature for an Existing Heat Exchanger Network of Crude Distillation Unit

المحتوى والصفحات

عدد الصفحات
0

إشراف وإعداد

الإشراف
Salih Mohamed Ahmed, Abdelbagi Osman Elsiddig
الإعداد
Kawther Abdelgader Ahmed Ebnoff

الاقتباسات الببليوغرافية

APA

Salih Mohamed Ahmed،Abdelbagi Osman Elsiddig و Kawther Abdelgader Ahmed Ebnoff . (2014). Determination of the Optimum Heat Recovery Approach Temperature for an Existing Heat Exchanger Network of Crude Distillation Unit. أطروحة(رسائل ماجيستير). كلية الهندسة والتكنولوجيا-جامعة الجزيرة. السودان.

MLA

Salih Mohamed Ahmed،Abdelbagi Osman Elsiddig و Kawther Abdelgader Ahmed Ebnoff . Determination of the Optimum Heat Recovery Approach Temperature for an Existing Heat Exchanger Network of Crude Distillation Unit. 2014. كلية الهندسة والتكنولوجيا-جامعة الجزيرة، رسائل ماجيستير.