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Regeneration of catalyst

Author name: عبد الباسط حسن مهدي
Supervisor name: Eman J. Taha | Thamer J. Mohammed
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

EFFECT OF PROMOTERS ON CATALYTIC ACTIVITY

Author name: علي نزار فائق
Supervisor name: SHAHRAZAD RIFAT RAOUF
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

Computer Model for Optimization of RDC Extraction Column Design

Author name: احمد صالح مهدي
Supervisor name: SARMAD ABBASS ALI
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

CATALYST DECAY IN A CSTR

Author name: محمد جاسم عبد الحسين
Supervisor name: Essam Halabia
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:

STUDY ON GALVANIC CORROSION OF HEAT EXCHANGER AND VALVES IN OIL REFINERIES

Author name: احمد سعدون خيون
Supervisor name: Jamal M. Ali
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

دراسة استخدام الكاربون المنشط المعدل لازالة الزئبق من الغاز الطبيعي == Studying The Use Of modified Activated Carbon To Remove Mercury From Natural Gas

Author name: عمار حسام الدين عبد الرزاق
Supervisor name: محمد ابراهيم محمد
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

A Study On Genetic Diversity Of Chickens Using Micro Satellite Markers

Author name: Al - Shammary . Aemen Ali Kudayr
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Baghdad - College Of Engineering - Department Of Chemical Engineering
University location: Baghdad
Key words:
  • Genetic engineering

معالجة المياه الصناعية الملوثة من المصافي النفطية (ازالة المعادن الثقيلة) == Removal of Heavy Metals from Industrial Wastewater in Petroleum Refinery

Author name: علي حاتم احمد
Supervisor name: ثامر جاسم محمد
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

الخواص الفيزيائية وميكانيكية سلوكية نفط خام البصرة == Rheological and Behavior of AL-Basrah Crude Oil

Author name: محمد علاوي حسن
Supervisor name: عامر عزيز عبد الرحمن
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

انتاج وقود الديزل ذو محتوى كبريتي واطئ باستخدام طريقة المعالجة بالهدرجة والاكسدة == Production of Low Sulfur Diesel by Combined Hydro-Oxidative Desulfurization

Author name: احمد محمد جودي
Supervisor name: نيران خليل ابراهيم
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:

تقييم نفط خام البصرة == EVALUATION OF BASRA CRUDE OIL

Author name: حيدر توماز حسين
Supervisor name: عدنان عبد الجبار
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

خزن الغاز السائل باستخدام افضل البدائل لترشيد الطاقة == LPG Storage Using Best Alternative Of Energy Conservation

Author name: غسان علي احمد سندال
Supervisor name: جمال مانع عل
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

عمليات التحميض للطبقات المنتجة للنفط الخام في ابار الانتاج البترولية == Acidification of Crude Petroleum Bearing Strata In Production Wells

Author name: سيف عبد الحق عبد الستار
Supervisor name: نجاة جمعة صالح
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:
Abstract: تم في هذا البحث دراسة عملية التحميض بصورة عامة وتحميض طبقتي ( التنومة والخصيب) المنتجة ) ضمن حقول EB - 91 للنفط والواقعة ضمن حقول شرقي بغداد بصورة خاصة. وتم اعتماد البئر (.(Case Study ) شرق بغداد كـ نموذج تعتبر عملية تحميض الابار النفطية من العمليات ا | In this work, acidification process in general and in particular at Al - Tanuma and Khasib layers is studied. Al - Tanuma and Khasib layer's in well (EB - 91)are located in east of Baghdad oil field. That well was taken as a case study.Acidification process is important to increase productivity of old oil well, and new one. Before acidification a test was carried out with water. During the test water is injected in these two layers under high pressure. If the test is successful that means the two layers are able to absorbed the dilute acid. - At first acid concentration must be diluted for 30 % to 15 % by using water as dilutent. - Additives are added to the acid, these additives are : • Anti - corrosion (A1 - 48) 0.5%.• Anti - emulsifier (NE - 50) 0.5%.• Emulsifier (WFT - 9256) 0.5%.• Solvent (WMS - 121) 1%. - Acid and the additives were injected inside Al - Tanuma and Khasib layers under high pressure. - Displacement liquid (gas oil) was injected inside the two layers to remove the acid and let it enter the formation. - The well was closed for minimum (1) hour to complete the reaction of acid with well formations. - The well was opened.The crude oil, gas oil and remaining acid will elute from the well by the action of pressure. - The crude oil eluted from the well was transferred by fire pipes to burning hole, where it was burned for about (3 - 4) hours. - After burning process is completed the well is ready for production.

التصميم الابتدائي لمحطة معالجة المياه الملوثة نفطيا في مصفى ميسان == Preliminary Design of Wastewater Treatment Plant In Missan Refinery

Author name: محمد خليل ابراهيم
Supervisor name: رياض صادق محمد صالح المختار
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:
Abstract: هذا البحث يتضمن كيفية دراسة معالجة المياه الملوثة بالمشتقات النفطية الناتجة من مصفى ميسان , ان قسم مصفى ميسان هو احد المصافي المهمة بالعراق، حيث انه يستهلك الماء من نهر المشرح التابع للمحافظة بكميات كبيرة لغرض العمليات التشغيلية التي تجري في المصفى.في | This research involves study of water treatment contaminated by Oil products in Missan Refinery, where the Department of Missan Refinery represents one of the important refineries in Iraq, which consumed water from Al - msherh River in large quantities for the purposes of the oil refinement.In the Missan refinery, The discharge of industrial wastewater from the operational units (three refining units) is about (1500 m3 / month), representing a sufficient amount of contamination of agricultural land or swamp water that discharge to it, Therefore, this study aims to find economical ways to treat these industrial wastewater that contaminated with oil. Several ways to treat contaminated water are suggested in present study (physical - mechanical and chemical treatment). The suggested treatments based on laboratory tests of contaminated Oily wastewater to find a specification of contaminated water, such as : - Turbidity, (pH), total salts and dissolved solids TDS, COD, BOD, suspended solids (S.S), oil content and phenol.

اختيار الافضل للمفاعل النازل لوحدة التكسير بالعامل المساعد == Optimization Technique of Fcc Downer Reactor

Author name: علي محسن غضبان
Supervisor name: Safa A. Al | Naimi
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:
Abstract: يشتمل البحث على عمل نموذج رياضي لمفاعل النازلdowner) ) في وحدة التكسير المحفز بالعامل المساعد وان التفاعل يشمل اربع مكونات هي التغذية Gas oil)) والغازات الخفيفة (Light gases) والكازولين (Gasoline) والفحم (Coke) اوما يسمى ب Four lumps model لوصف حركة تفاعل | In this work, mathematical model for downer reactor have been developed, in which a four - lump model is used to characterize the feed and the products, where gas oil cracks to give lighter fractions and coke. The integrated reactor steady state model makes gross assumption about the hydrodynamics, using 4th. order Runga Kutta method. Polymath version 5.1 and Aspen version 7.3 programs are used to solve the simulation model. This model can predict the mixing temperature and pressure profiles at mixer (MxR) chamber; also shows the physical performance and productivity all over the downer height. An interactive excel worksheet is constructed and used as a powerful tool for solving the model equations and studying the effect of any change in operating variables on the unit performance. Also observed the simulated results by using two programs (Polymath and Aspen) and the difference between them especially in temperature , pressure and product yield profile plotted along the reactor length and shows that the results from Aspen are better than Polymath because the first is more advanced and accurate. The operation of downer reactor for catalytic cracking is associated with several important objectives such as feed rate and height, diameter of reactor and amount of catalyst rate as well as the production requirements, all of which need to be optimized simultaneously. In this study, a validated mathematical model was used to perform the single - objective optimization of the FCC system at the design stage. In the optimization study, four operating parameters were used as decision variables. These variables were chosen based onsystematic sensitivity analysis of the system which showed complex interplay of the decision variables over the system performance indicators. Elitist Polymath version 5.1 enhanced with Excel flow sheet 2007 were used to solve a number of objective function optimization problems. The objective functions used are maximization of the gasoline yield, and minimization of the catalyst flow rate. The optimal results obtained here provide physical insights that can help in the design stage of the downer reactor.

الاضافات على زيوت التزيت لتحسين خواصها == Additives For Lubricantion Oil To Improve Its Properties

Author name: وسام عدنان حيدر العبيدي
Supervisor name: عدنان عبد الجبار عبد الرزاق السالم
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:
Abstract: معامل اللزوجة ونقطة الانسكاب من العوامل الاكثر اهمية التي يجب دراستها لتحسين اداء زيوت التزيت. في هذه الدراسة اضافة البوليمر مثل Polymethacrylate بنسب وزنية %(2,4,6,8,10) الى قاعدة الزيت الاساس SN500 وSN150 معامل اللزوجة ونقطة الانسكاب تقاس حسب المواصفه | Viscosity index and pour point are the most important factors that should be study to improve the performance of lubrication oil. In this study an polymer additive such as polymethacrylate (2,4,6,8,10)wt% were added to lubrication basic oil SN 500 and SN150.Viscosity index and pour point were measured according to ASTM 445 and ASTM D2270 respectively The results show that as an increasing in additive ratio, viscosity index and pour point increase.

تحسين مواصفات / ازالة الكبريت من النفوط العراقية الثقيلة باستخدام طريقة الاكسدة المعانة بالموجات فوق الصوتية == Upgrading / Desulfurazation of Iraq Heavy Crude Oils Using Oxidation Assisted By Ultrasound

Author name: شيماء كاظم محيسن
Supervisor name: نيران خليل ابراهيم
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:
Abstract: وجودالكبريت في النفط الخام يشكل تحديات هائلة فيما يتعلق بالاثار البيئية والاقتصادية السلبية.وعلى هذا النحو ايضا سلامة المعدات معرضة لمخاطر عالية اثناء معالجة نفط خام الاحدب(3,55? كبريت) بسبب طبيعته الحامضية.وبالتالي فان هذا البحث يهدف الى تقليل محتوى الك | The presence of sulfur in crude oil posses enormous challenges as regards its negative environmental and economic impact. As such, the safety of the equipment is at high risk during the processing of Al - Ahdab crude oil because of its sour nature (3.55wt% sulfur). The present work is aimed at reduce the sulfur content of Al - Ahdab crude oil prior to processing by oxidative desulfurization treatment method using ultrasonic irradiation probe and high speed homogenizer for the enhancement of oxidizing the sulfur compounds and converting them into sulfones. The oxidation step was then followed by solvent extraction to extract the sulfones.An ultrasound - assisted oxidative desulfurization (UAOD) with hydrogen peroxide in the presence of acetic acid and subsequent solvent extraction using a polar solvent (acetonitrile ) has been applied for the desulfurization of Al - Ahdab crude oil in a bench scale unit. The results indicate that the desulfurization efficiency is dependent on the sonication rate. The measured sulfur content of the crude oil, obtained after 10 minutes contact time indicated that the highest efficiency obtained is 81.86%, corresponding to reductionin sulfur content up to 0.664wt.%, when sonication energy of 21139J was used. The second mixing scheme examined was that of using a high speed homogenizer. The results indicate that the desulfurization efficiency increases with increasing mixing speed from5000 to 26000rpm, and reaction time from 15 to 60min. The highest desulfurization efficiency obtained was 72.6% at 26000rpm and 60min reaction time. The above results indicate that UAOD is a successful process to upgrade Al - Ahdab crude oil. However, oxidative desulfurization assisted by high speed agitation also gave reasonable desulfurization efficiency. The sulfur content was reduced to about 1.2% which is less than that of Kirkuk crude (2.8%) and that of AL - Basrah crude (3.16%).

دراسة حركية التفاعل لوحدة التهديب بالعامل المساعد في مصفى الدورة == Kinetics Study of Catalytic Reforming Process In Daura Refinery

Author name: حيدر مجيد خضير
Supervisor name: محمد فاضل عبد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:
Abstract: Catalytic naphtha reforming is one of the key processes in petroleum refining, converting gasoline boiling range low - octane hydrocarbons to high - octane compounds which can be blended into gasoline. Other valuable by products include hydrogen and cracked light gases. Modeling of a typical semi - regenerative catalytic reformer of Duara refinery has been carried out involving most its key constituent units. Kinetic modeling of the reactions occurring in the fixed bed reactors connected in series formed the most significant part of the overall simulation effort. A reaction scheme involving (15 pseudo components) connected to gether by a network of 30 reactions for components in the C5 - C10 range has been modeled. The Hougen - Watson Langmuir - Hinshelwood type reaction rate expressions are used to represent rate of each reaction. Deactivation of the catalyst was modeled by including the corresponding equations for coking kinetics. It was found that Paraffines and Naphthenes undergo a continuous reduction through the three reactors while the rate of formation of aromatics is becoming slower as the reactants proceed to the third reactor. The reactor of naphtha reforming could be considered as a hydrogen production.

تخمين حركية تفاعل ازالة الكبريت للنفثا الثقيلة العراقية == Prediction of Kinetic Reaction of Iragi Heavy Naphtha Desulferization

Author name: سها سامي قاسم
Supervisor name: زيدون محسن شكور
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:
Abstract: واحدة من التحديات في مصافي تكرير النفط الخام في الاونة الاخيرة هو الحد من محتوى الكبريت من النفثا الثقيلة الى الحدود الدنيا. في هذا البحث تم اخذ مواصفات محتوى الكبريت للنفثا الثقيلة بمعدل 632 جزء في المليون الى 2.5 جزء في المليون، في درجات حرارة التفاعل ( | One of the recent challenges in the petroleum refineries is the reduction of sulfur content of heavy naphtha to the new lower limits. In this reaserch, was taken the specification of the sulfur content of heavy naphtha at arrange 632 ppm to 2.5 ppm, The range of reaction temperatures is (35 - 175) oC and liquid hourly space velocity (LHSV) at range of (1.3 - 1.4) hr - 1 and hydrogen pressure is 35 bars.The simulators are useful tools to manage operation and to improve the profitability of the process. In this study, excel and Matlab program were developed to simulate hydrodesulferization process (HDS) in vapor phase reactor of heavy naphtha hydrotreating unit of Daura refinery, the comparison between the plan results with HDS reactor model results was made.. Based on the model results the optimum operating conditions were determined. Acomputer program MATLAB (Matrix Laborator) it is software for developed code of kinetic parameter estimation problem using the estimation method and least square as objective function and new GA as solving method. The code was implemented on personal computer (intel (R) Core (TM) i3 CPU, 2.39 GHz processor, 2 GB RAM). The function to be minimized was the sum of squares of the differences between calculated and measured concentration.Genetic optimization method was used to define the parameters of desulfurization reaction kinetic. This hydrotreating reaction kinetic model for desulfurization of Daura heavy naphtha was determined for heavy naphtha boiling point range of (35 - 175) C and using a commercial (HDS) catalyst cobalt - molybdenum (Co - Mo) supported of alumina.The result showed that the order of kinetic reaction was first order for heavy naphtha hydrotreating with (Co - Mo) supported of alumina, and the graphically method is more suitable and less error than optimization method for represent the kinetic reaction for heavy naphtha hydrotreating in Daura refinery.

مقارنة بين الطرق المختلفة لتحلية وقود الديزل == A Comparison Between The Different Methods Used For Diesel Fuel Sweetening

Author name: ابو ذر حمد الله حسين
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

تاثير تاكل الغلفاني على المعادن تحت ظروف الجريان المختلفة == Effect Of Galvanic Corrosion On The Metals Under Flow Conditions

Author name: محمد شرباز كريش
Supervisor name: Jamal Mane Ali
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:

Design Of Shell And Tube Heat Exchanger Computer Program By Visual Basic

Author name: مؤيد مشعان طلال
Supervisor name: ظافر حسين رشيد
General topic: Chemical Engineering
Specific topic: Biochemistry Engineering
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering
Language: English
University location: Baghdad
First pages:

تحسين مواصفات متبقي التقطير الجوي لنفط الخام شرق بغداد بواسطة الهكسان الاعتيادي == Upgrading Of East Baghdad Resid By N - Hexane

Author name: علي جاسم راضي
Supervisor name: عادل شريف حمادي
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

الحماية الكاثودية للخزانات == Cathodic Protection Of Storage Tank

Author name: رنا مهند حسين
Supervisor name: شذى احمد سامح
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:

النمذجة والمحاكاة الرياضية لوحدة التكسير المحفز بالعامل المساعد == Modeling And Simulation Of FCC Risers

Author name: وليد خالد فاضل
Supervisor name: شاكر محمود احمد
General topic: Chemical Engineering
Specific topic: Oil Refining and Gas Technology
Degree: Higher Diploma
University: University of Technology - Department Of Chemical Engineering - Chemical Engineering and Oil Refining Branch
Language: English
University location: Baghdad
First pages:
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