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حماية سبائك الالمنيوم من التاكل في محلول ملحي باستخدام تقنية ليزر Nd:YAG == PROTECTION OF ALUMINUME ALLOY FROM CORROSION IN NACL SOLUTION USING ND:YAG LASER TECHNIQUE

Author name: احمد ياسين علي الجنابي
Supervisor name: شذى احمد سامح
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

Study The Performance Of Low Cost Material ( Peanut Hulls) For Dye Adsorption Using Inverse Fluidized Bed

Author name: Shaimaa Abood Alwan
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • Fluidization

تقييم نفط خام البصرة == EVALUATION OF BASRA CRUDE OIL

Author name: حيدر توماز حسين
Supervisor name: عدنان عبد الجبار
General topic: Chemical Engineering
Degree: Higher Diploma
Language: English
University location: Baghdad
First pages:

The Removal Of So2 Over Modified Activated Carbon Calalyst In Fixed Bed Reactor

Author name: Zainab Adnan Nasir
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • Sulphur dioxide

تحسين انتقال المادة باستخدام اسطوانة دوارة معززة == ENHANCEMENT OF MASS TRANSFER USING ROTATING CYLINDER PROMOTERS

Author name: براق شهاب احمد
Supervisor name: قاسم جبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

Shell And Double Concentric Tubes Heat Exchanger Calculations And Analysis

Author name: fadhic abid allawi
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • heat - transfer media

Study Of Corrosion Of Electrical Submersible Pumps Esp In South Rumaila Oil Field

Author name: layla sideea mohamed
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • corrosion contral industry

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
Degree: Higher Diploma
Language: English
University location: Baghdad
First pages:

اداء ونمذجة عملية التحويل الى الغاز في مفاعل ذو الطبقة المتميعة == PERFORMANCE AND MODELING OF GASIFICATION PROCESS IN A FLUIDIZED BED GASIFIER

Author name: اسراء كرم عبد
Supervisor name: باسم عبيد حسن
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

Potential Of Rice Husk For Methylene Blue Dye Removal From Waste Water

Author name: Hamsa Natia Fadhil
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • chemical engineering

Disinfection By Product Removal By Activated Carbon Using Batch Mode

Author name: nabeel ibrahim hasan
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University location: Baghdad
Key words:
  • filters and filtration

تصنيع وتشخيص المضافات النانوية الى الديزل الحاوي على الفناديوم == Synthesis and Characteristics of Nano-additives to Vanadium Containing Diesel-Oil

Author name: علياء حمزة حمادي جودي
Supervisor name: تحسين علي الحطاب | فلاح كيفي مطلوب
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

مثبطات التاكل لحديد تسليح الخرسانة باستخدام مثبطات دوائية == Corrosion Inhibition of Mild Steel in Concrete Using Drug Inhibitors

Author name: هدى عادل محمد عبد الجليل
Supervisor name: عبد الرسول صالح البوهات
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

دراسة العوامل المؤثرة في عملية استخلاص النحاس == Studying the Effective Parameters in Copper Electro Winning

Author name: سارة علي عبد الحسين محمد
Supervisor name: شاكر صالح بحر | حسن عبد الزهرة الفتلاوي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

المحاكاة على الديناميكية والسيطرة لبرج التقطير == SIMULATION ON DYNAMIC AND CONTROL OF DISTILLATION COLUMN

Author name: سامر عطا قاسم
Supervisor name: خالد مخلف موسى
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تخفيض المقاومة الاحتكاكية بسبب الاضافات المفردة والمشتركة == REDUCTION OF FRICTIONAL RESISTANCE CAUSED BY SINGLE AND COMBINED ADDITIVES

Author name: عمر جلاء يحيى
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تحليل انتقال الحرارة والزخم لجريان حلقي ثنائي الطور ماء - هواء في انبوب افقي == MOMENTUM AND HEAT TRANSFER ANALYSIS OF ANNULAR AIR-WATER TWO PHASE FLOW IN A HORIZONTAL PIPE

Author name: اسيل قيس رشيد
Supervisor name: باسم عبيد حسن | خالد مخلف موسى
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

التحليل النظري للتاكل المعدني الغلفاني الخارصين الحديد والنحاس تحت السيطرة طاقة التنشيط == THE THEORETICAL ANALYSIS OF GALVANIC CORROSION (Zn, Fe and Cu) UNDER ACTIVATION CONTROL

Author name: اسيل فاضل خضير عباس
Supervisor name: باسم عبيد حسن
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة اللزوجة الجوهرية وطاقة تنشيط الجريان لبعض البوليمرات في مختلف المذيبات == STUDY OF INTRINSIC VISCOSITY AND FLOW ACTIVATION ENERGY OF SOME POLYMERS IN DIFFERENT SOLVENTS

Author name: رباب عماد احمد الجبوري
Supervisor name: طالب بهجت كشمولة
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة تاثير عوامل التشغيل في معالجة المياه باستخدام التنافذ العكسي == STUDYING THE EFFECT OF OPERATING CONDITIONS ON WATER TREATMENT USING RO

Author name: مروة اسد صالح
Supervisor name: نصير عبود الحبوبي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة انتقال المادة للغشاء الساقط في الانابيب اللولبية باستخدام نظام ماء غاز ثاني اوكسيد الكاربون == A STUDY OF MASS TRANSFER INTO A LIQUID FALLING FILM IN SPIRAL TUBES USING CO2 – WATER SYSTEM

Author name: امال قحطان عبد الله
Supervisor name: زيد عدنان عبد الرحمن
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير بعض المضافات على اللزوجة الجوهرية لزيوت التزييت الاساس == INFLUENCE OF SOME ADDITIVES ON INTRINSIC VISCOSITY OF BASE LUBRICATING OILS

Author name: خالد عمران علي
Supervisor name: طالب بهجت كشمولة
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تثبيط التاكل الكلفاني في محلول كلوريد الصوديوم == INHIBITION OF GALVANIC CORROSION IN SODIUM CHLORIDE SOLUTIONS

Author name: زينب علي زغيلي
Supervisor name: قاسم عبد الجبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

المحاكاة النظرية لدراسة تاكل الحديد في الحوامض الحاوية على الاوكسجين == SIMULATION OF IRON CORROSION IN AERATED ACID SOLUTIONS

Author name: ايثار مقصود جسار
Supervisor name: قاسم جابر محمد | باسم عبيد حسن
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تقليل الاحتكاك بواسطة المحسنات المضافة في الجريان المضطرب == FRICTION REDUCTION CAUSED BY THE ADDITION OF ADDITIVES INTO A TURBUIENT FLOW

Author name: اسماء حسن ضياء
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تحليل نظري لافضل سمك حشوة لمفاعل كهروكيمياوي == THEORETICAL ANALYSIS OF THE OPTIMUM BED THICKNESS OF AN ELECTROCHEMICAL REACTOR

Author name: اوس عبد المهدي صادق
Supervisor name: قاسم جبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

السيطرة بالوقت الحقيقي لمبادل الحراري المضغوط == REAL TIME CONTROL OF COMPACT HEAT EXCHANGER

Author name: شفاء عبيد كاظم الجبوري
Supervisor name: نصير عبود الحبوبي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تجريبية وحركية للاسترداد الفناديوم من مخلفات المحفز المستهلك استعمال الصودا الحارقة == Experimental and Kinetics of Vanadium Recovery from Spent Catalyst Using Caustic Soda

Author name: صفا كاظم حسين
Supervisor name: خالد مخلف موسى
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

التنبؤ بايجاد علاقات الحجم المولي للسائل المشبع في اي درجة حرارة بظمنها درجة الغليان للمركبات النقية والخ?ئط == PREDICTION AND CORRELATIONS OF SATURATED LIQUID MOLAR VOLUME AT ANY TEMPERATURE (INCLUDING NORMAL BOILING POINT) FOR PURE COMPONENTS AND MIXTURES

Author name: الاء حسين علي الربيعي
Supervisor name: محمود عمر عبد الله
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير الاضافات المشتركة على مقاومة الانحلال لمحاليل البوليمر المخففة تحت تاثير الجريان المضطرب == EFFECT OF COMBINED ADDITIVES ON DEGRADATION RESISTANCE OF DILUTE POLYMER SOLUTIONS UNDER TURBULENT FLOW

Author name: لبنى عبد الكريم نعيم الغزي
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة بعض العوامل المؤثرة على اداء المفاعل الحيوي ذي الخلط المستمر باستخدام برنامج مختبر المصفوفات Matla == INVESTIGATION OF SOME FACTORS AFFECTING THE PERFORMANCE OF BIOCHEMICAL REACTOR USING MATLAB

Author name: رائد عبد اسماعيل
Supervisor name: باسم عبيد حسن | خالد مخلف موسى
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

المحاكاة نظريا وعمليا لانتاج الاثيل ثلاثي بيوتيل الايثر باستخدام التقطير التفاعلي == SIMULATION AND EXPERIMENTAL INVESTIGATION TO PRODUCE ETHYL TERT-BUTYL ETHER USING REACTIVE DISTILLATION

Author name: نادين خالد محمد الجنابي
Supervisor name: ندى بهجت النقاش
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

افضل سمك طبقة وطبقتين من عازل انبوبي لمنع تسرب الحرارة تحت ظروف انتقال الحرارة بالحمل الطبيعي == OPTIMUM SINGLE AND LAYERED PIPE INSULATION FOR A GIVEN HEAT LOAD UNDER NATURAL CONVECTION HEAT TRANSFER

Author name: سمر سعدي حسين
Supervisor name: قاسم جبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير المؤثرات الميكانيكية على تحلل عوامل تقليل الاعاقة == THE INFLUENCE OF MECHANICAL EFFECTS ON DEGRADATION OF DRAG REDUCING AGENTS

Author name: مروة فائق عبد الجبار
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير مضافات تقليل الاعاقة في الجريان الاضطرابي ثنائي الطور == THE EFFECTIVENESS OF DRAG REDUCER AGENTS IN TURBULENT TWO PHASE FLOW

Author name: نعيم عبد المحسن اسماعيل حسين الحلو
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

حساب معامل انتقال الكتلة للعمود الفقاعي لنظام ماء - هواء باستخدام معالجة الصور == DETERMINATION OF MASS TRANSFER COEFFICIENT FOR BUBBLE COLUMN (AIRWATER SYSTEM) USING IMAGE PROCESSING

Author name: الاء عبد العزيز تركي
Supervisor name: نصير عبود الحبوبي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير بعض الاضافات على خصائص الشحوم == INFLUENCE OF SOME ADDITIVES ON PROPERTIES OF GREASES

Author name: زينب حيدر عبود الموسوي
Supervisor name: مهند عبد الرزاق
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة الامتصاص على عمود الامتصاص == STUDYING THE CONTROL OF ABSORPTION COLUMN

Author name: داليا سمير مكي
Supervisor name: خالد مخلف
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

محاكاة عن التقطير المستمر للتفاعل الكيمياوي == SIMULATION OF CONTINUOUS REACTIVE DISTILLATION COLUMN

Author name: نور قيس رشيد
Supervisor name: ندى بهجت النقاش
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

الحساب النظري لمعاملات التصحيح لمعامل السحب وسرعة الاستقرار النهائية == THE THEORETICAL INVESTIGATION OF DRAG COEFFICIENT AND SETTLING VELOCITY CORRELATIONS

Author name: هناء كامل خلف
Supervisor name: مهند عبد الرزاق
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تنبؤ وعلاقات عامة لقيمة الانتروبي المتبقي المحمص للمركبات النقية == PREDICTION AND CORRELATIONS OF RESIDUAL ENTROPY OF SUPERHEATED VAPOR FOR PURE COMPOUNDS

Author name: شهد زهير النجار
Supervisor name: محمود عمر عبد الله
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة تاثير قواعد الخلط المختلفة على علاقات التوازن الطوري للبخار مع السائل == INVESTIGATION THE EFFECT OF DIFFERENT MIXING RULES ON VLE PREDICTION

Author name: مها علي حسين
Supervisor name: محمود عمر عبد الله | فينوس مجيد حميد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

التحول الهايدروجيني للهكسان الطبيعي بوجود الاطيان المحملة بالبلاتين كعامل مساعد والمحضرة باستخدام تقنية الغاز المسال فوق الظروف الحرجة == HYDROCONVERSION OF N-HEXANE OVER PLATINUM SUPPORTED ZEOLITE CATALYSTS PREPARED BY SUPERCRITICAL TECHNIQUE

Author name: اسامة اكرم سعيد الراوي
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:

دراسة الخواص الريولوجية لمحاليل البولمرات والعوائق == STUDY THE RHEOLOGICAL PROPERTIES OF NON-NEWTONIAN POLYMER SOLUTIONS AND SOLID SUSPENSIONS

Author name: منار طاهر ناصر
Supervisor name: قاسم جبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة عملية لاداء بعض مثبطات التاكل المعدني في محاليل حامضية مشبعة بالهواء == INVESTIGATION OF THE PERFORMANCE OF SOME CORROSION INHIBITORS IN AERATED ACID SOLUTIONS

Author name: حيدر محمد تركي
Supervisor name: قاسم جبار سليمان | باسم عبيد حسن
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

محاكاة لسيطرة مبادل حراري المزدوج == SIMULATION OF CONTROLLED SHELL AND TUBE HEAT EXCHANGER

Author name: سارة سمير حسن ليلو
Supervisor name: نصير هبود الحبوبي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

الازالة الكهروكيمياوية لايونات المواد الثقيلة من المخلفات الصناعية المقلدة == Electrochemical Removal of Heavy Metal Ions from Simulated Industrial Effluents

دراسة مفاعل كهروكيمياوي يعمل تحت تاثير انتقال الكتلة لازالة ايونات المعادن == Electrochemical Reactor Simulation for Metal Ion Removal under Mass Transport Controlled Conditions

Author name: اسن قصي ناجي
Supervisor name: Qasim J. Slaiman | Kamal Shakir Abd
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

القيم والتنبؤ من الحرارة الكامنة للتبخر في درجات الحرارة المختلفة للمركبات النقية والمخاليط الثنائية == Evaluation and Prediction of Latent Heat of Vaporization at Various Temperatures for Pure Components and Binary Mixtures

Author name: محمد جبار عجرش
Supervisor name: محمود عمر عبد الله
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير تركيز البوليمرات في المحاليل المائية على الخواص الريولوجية == EFFECT OF CONCENTRATION OF WATER-SOLUBLE POLYMER SOLUTIONS ON RHEOLOGICAL PROPERTIES

Author name: اريج جاسم محمد
Supervisor name: مهند عبد الرزاق
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تاثير قطر الانبوب على تقليل الاعاقة في الجريان المضطرب == EFFECT OF PIPE DIAMETER ON TURBULENT DRAG REDUCTION

Author name: وسام هادي رضا الصفار
Supervisor name: جابر شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

تقييم اداء نظام التحلية الشمسية نسبة الى مناخ البصرة == Evaluation of the Performance of Solar Desalination System Relative to Basrah Climate

Author name: هبة صباح جعفر
Supervisor name: علاء عبد الرزاق جاسم | جاسم محمد مهدي الاسدي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Basrah
First pages:

الخواص الهيدروديناميكية وانتقال المادة في الملامس ذي القرص الدوار == Study of Hydrodynamics and Mass Transfer Characteristics in Rotating Disc Contactor

Author name: وسام عبد الرحمن فيروز القمبر
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Basrah
First pages:

التحلل للاصباغ النسيجية في المياه الملوثة بالاكسدة الانودية المتقدمة == Degradation of Textile Dyes Wastewater by Advanced Anodic Oxidation

Author name: زينب ناجي نعمه جاسم
Supervisor name: فلاح كيفي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

تقييم عمليات الاكسدة الكهروكيمياوية المتقدمة لمعالجة المياه الفينولية المحضرة == Evaluation of Electrochemical Advanced Oxidation Processes for the Treatment of Phenolic Wastewater

Author name: زهراء محمد جودة فيروز
Supervisor name: علاء نور غانم الموسوي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

ازالة ايونات الرصاص من مخلفات المياه باستخدام التخثير الكهروكيمياوي كعملية مستمرة == REMOVAL OF LEAD IONS FROM WASTEWATER USING ELECTROCOAGULATION AS CONTINUOUS PROCESSES

Author name: افنان مشكور عبيد عزيز
Supervisor name: ساطع كاظم احمد
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

ازالة ايونات الزنك من مياه المخلفات الصناعية باستخدام قطب ذو حشوة متميعة == Removal of Zinc Ions from Industrial Wastewater by Using Fluidized Bed Electrode

Author name: نسرين حسين جاسم
Supervisor name: شاكر صالح بحر
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

العوامل المؤثرة في خلية الوقود الميكروبية عند توليد الكهرباء من المياه الملوثة == Effect of Microbial Fuel Cell Parameters on Electricity Generation from Wastewater

Author name: علي منير هادي قدوري
Supervisor name: حسن عبد الزهرة الفتلاوي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

اقتران خليه الوقود المايكروبي بالمحفز الضوئي لتوليد الطاقه النظيفة == Coupling microbial fuel cell with photo catalytic as renewable power generation

Author name: سارة كريم غافل
Supervisor name: واثق ناصر حسين
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

تاكل الكاربون الصلب في حامض الستريك باستخدام مستخلص اوراق الجنكة بيلوبا == Corrosion Inhibition of Carbon Steel in Citric Acid Using Ginkgo Biloba Leaves Extract

Author name: سرى ابراهيم موسى
Supervisor name: فلاح كيفي مطلوب
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

دراسة تثبيط تاكل الخارصين في انواع مختلفة من المحاليل والمثبطات == Study for Zinc Corrosion Inhibition in Different Types of Inhibitors and Solutions

Author name: زينب عبد الكريم فرحان
Supervisor name: شاكر صالح بحر
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

ازالة ايونات الرصاص من مياه الصرف الصناعي بطريقة التخثير الكهروكيمياوي == Removal of Lead Ions from a Synthetic Waste Water by a Batch Electrocoagulation Process

Author name: رواء زاهد جفات
Supervisor name: ساطع كاظم عجام
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

استرجاع الفضة من محلول نفايات الاشعة السينية بواسطة استخدام مفاعل ذو حشوه ثابته == Recovery of Silver from Waste X - Ray Films by Using Fixed Bed Reactor

Author name: منتظر احمد عيسى محيسن
Supervisor name: شاكر صالح بحر
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

الترسيب الكهروكيميائي للكادميوم من مياه الصرف == Electrochemical deposition of Cadmium from Wastewater

Author name: زينب جابر حمزة
Supervisor name: فلاح كيفي مطلوب
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

تاثير المثبطات (بيردين و نترات الصوديوم) على تاكل الفولاذ الكاربوني في اسطوانة دوارة في درجات حرارة مختلفة في الوسط الحامضي / الملحي == The Effect of Inhibitors (Pyridine and NaNO3) on Carbon Steel Corrosion in Rotating Cylinder at Different Temperatures in a Salty / Acidic Medium

Author name: شهد حسن علاوي
Supervisor name: شاكر صالح بحر
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

معالجة المياه الصناعية من المعادن السامة باستعمال مادة امتزاز محلية جديدة == A new Local Adsorbent for The Treatment of an Industrial Wastewater from Toxic Metals

Author name: سحر فاضل عبد الرزاق الجمعة
Supervisor name: الهام هاشم شمخي | مصطفى محمد رضا الفائز
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Basrah
First pages:

تاثير خصائص القطب على اداء خلية الوقود الميكروبية == Influence of Electrodes Characteristics on the performance of a Microbial Fuel Cell

Author name: محمد هادي راضي الطائي
Supervisor name: حسن عبد الزهرة الفتلاوي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:

معالجة مياه الصرف الصناعي لمصافي النفط بالاكسدة الانودية المباشرة == Treatment Of Petroleum Refinery Wastewater By Direct Anodic Oxidation

Author name: انغام سامي حمزة
Supervisor name: علاء نور غانم الموسوي
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:
Abstract: مياه الصرف الصناعي لمصافي النفط الناتجة بصورة رئيسية من عمليات تكرير النفط الخام والصناعات التحويلية، مواد التشحيم والبتروكيماويات الوسيطة. هذه السوائل هي المصدر الرئيسي للتلوث البيئي المائي. تتكون مياه الصرف الصناعي من الزيوت والشحوم والمركبات العضوية ا | Petroleum refinery wastewater originating from petroleum industries primarily resulted in refining crude oil and manufacturing fuels, lubricants and petrochemical intermediates. These effluents are a major source of aquatic environmental pollution. The wastewaters are composed of oil and grease, toxic organic compounds along with many other minerals. In this study, wastewater of Al - Najaf petroleum refinery was used as electrolyte solution in the experiments, and the effect of some variables on the removal of organic material as a pollutant in term of COD were studied. The performance of anodic oxidation represented by COD removal was studied using 1 liter batch - mode parallel plate electrochemical reactor at constant initial COD concentration and fixed agitation speed of 250 rpm with the variation of operating conditions that were expected to have a major effect on process. These variables were : electrodes material (platinum, stainless steel, graphite, PbO2, and carbon felt), current densities (5, 15, 25) mA cm - 2 for carbon felt electrode and (10, 30, 50) mAcm - 2 for other electrodes, pH (4, 7, 10), temperatures (25, 40, and 55)?C and with electrolysis time up to 120 minutes. The results show that the direct anodic oxidation process gave the best COD removal percent of 84.88% and 86.27% at 50 and 25 mA cm - 2 current densities for PbO2 and carbon felt anode materials, respectively. The highest COD removal was predicted at pH 4 and the best temperature at 55?C for all electrode types. The reaction was followed by pseudo first - order kinetics rate. As well, it was studied the effect of current density on the current efficiency, instantaneous current efficiency, energy consumption, charge load with the time and calculated activation energy.

تحسين الاداء الحراري للمائع النانوي في المبادلات الحرارية == Enhancement Of Thermal Performance Of Nanofluids In Heat Exchangers

Author name: شهد فالح حسن
Supervisor name: تحسين علي الحطاب
General topic: Chemical Engineering
Specific topic: Electrochemical Engineering
Degree: Master
Language: English
University location: Babylon
First pages:
Abstract: التقنية الواعدة التي تستخدم لتعزيز عملية الانتقال الحراري هي باستخدام الموائع النانوية كخيار جيد واستبدالها محل السوائل التقليدية الشائعة. والمبادلات الحرارية هي معدات واسعة التطبيق في كثير من التطبيقات الصناعية المختلفة وبالتالي يكون سلوك وخصائص المائع | The most promising technique that is used to enhance the thermal performance for the heat transfer processes is using the nanofluids as a good choice to replace the conventional fluids. The heat exchangers are the wide range application equipment that is used for different industrial applications and therefore, the properties and the behavior of the fluid media are the main control parameters in equipment design of the heat exchangers. In this work an attempt was made to investigate experimentally the thermal performance of nanofluid which consists of deionized water (DI) as a base fluid and Aluminum oxide (Al2O3) as solid nanoparticles. The investigation includes two parts, the first one is studying the effect of addition of solid nanoparticles to the base fluid on the thermo - physical properties such as density, viscosity and thermal conductivity for different values of the volume fraction of nanoparticles. The second part includes the experimental work studying the effect of the nanoparticles (Al2O3) volume fraction (0.05, 0.1 with base fluid ), heat flux (With three values 7.4W,11W,16.8W) and angle (With two values 90?,45?) with four models (four different type from wicks in heat pipe) to enhance the heat transfer in heat pipe with two cases of transient temperature distribution and steady state. One model is different from the other by using different wicks in a heat pipe in all models. The general results referred to the enhancement of heat transfer rate are represented by increasing the concentration of nanoparticles (Al2O3) volume fraction such as (?=0.1) is better than (?=0, ?=0.05), increasing heat flux such as (16.8W) is better than (7.4W,11W) and an inclination angle such as( 45?) is better than (90?).At the transient state the time to reach to the steady state decreases when the concentration of the nanoparticles (Al2O3) volume fraction increases, the heat flux increases and the angle incline. In model 4 the heat transfer enhancement is better than that of model 3 and model 3 is better than that of model 2 and model 2 is better than that of model 1.The time to reach the steady state decreases in model 4 more than model 3, model 2 and model 1. The temperature decreases in the heat pipe when we gradually sidle from heater. The time to reach to steady state found in model 4 at concentration of nanofluid (?=0.1) and heat flux (16.8W) in angle (45?) is (19 min). In the steady state when we increase the concentration of the nanoparticles (Al2O3) volume fraction at the same distance (z) the temperature increases ,The increase in the heat flux of the hot part of the heat pipe will always increase the temperature in the heat pipe and the temperatures distribution in the heat pipe will be improved. The thermal performance of the heat pipe is enhanced by increasing the concentration of the nanofluid , the heat flux and by inclining the heat pipe from 90? angle to 45? angle such as in result of model 4.

ازالة ايونات عدد من المعادن السامة الثقيلة كهروكيميائية وتحت ظروف ديناميكية == Removal Of Multi Toxic Metal Ions Electrochemically Under Dynamic Conditions

Author name: سهى اكرم محمد
Supervisor name: قاسم جبار سليمان | سيسيليا خوشابا
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: Electrochemical process is supplying unquestionable amelioration to treat the wastewater pollution, which is a major issue and particularly if the pollutants concerned of multi heavy metal ions. Therefore, two different configurations of electrochemical cells rotating cylinder electrode, RCE and fixed bed flow - by porous electrode, FBPE, in which electrolyte flow is perpendicular to the current flow. They are used to study their effect on the removal of four heavy metal ions being examined, which are : copper Cu(II), cobalt Co(II), cadmium Cd(II), and lead Pb(II)). As single, double, triple, and quaternary ions that were mixed, at different applied currents (150, 180, 250, and 300 mA) by using RCE and (50, 90, 150, 180, and 250 mA) by using FBPE. In addition, different dynamic conditions are examined, which are represented as different rotation speeds in RCE (100, 150, 200, 250, and 300 rpm) and different flow rates in FBPE (100,200,300,400, and 500 l/h). At different deposition times with constant initial concentration of the four metals ions as 125 ppm, the samples have been taken. The supporting electrolyte that is used in all experiments is 0.5 M NaCl at pH 3.5. Where a porous highly conductive material for both electrodes design stainless steel 316 of 60 mesh no.(60 60 pore in inch2) is chosen, to ensure the removal of heavy metals be effective and also the recovery of the deposited metal can be removed without damage the electrodes.The effect of the variation in the initial concentrations on the deposition process has been investigated. The range of initial concentration is from 50 to 200 ppm for Cu(II), Co(II), and Pb(II) ions with different applied currents (120, 180, 250, and 300 mA) and rotation speeds (100, 150, and 200 rpm) at constant time of deposition. Box - Wilson, central composite design, is chosen to carry out investigation and thirty - six response equations are found.The metals deposited on the electrode were recovered, which can be tested by X ray diffraction to characterize the composition of the recovered powder.The scope of the research mainly revealed the followings : The experimental results of the removal rate of the four metal ions : individually and as co - deposition as : binary, ternary, and quaternary metal ions, and at different conditions are presented. Mass transfer coefficients are found, and correlated with applied current and electrolyte velocity, which being more by applied current to increase. The performances of the two configurations are deduced based on the figures of merit for an initial concentration of 125 ppm.as shown in the followed table, Table Abstract - 1 The Maximum values of figures of merit for the two configurations reactor Reactor Design RCE FBPE Heavy metal ions A Applied current 300mA Cu(II) Co(II) Cd(II) Pb(II) At applied current 250 mA Cu(II Co(II) Cd(II) Pb(II) Fraction conversion, % 99.94 80 77.7 99.5 100 98.9 95 100 Mean value of the Space time yield (Kg m - 3 s - 1) 58.6 36.7 35.6 47.6 34.5 25.2 20.3 32.5 Specific energy consumptions Es (KWh/Kg) 1.75 2.03 3.9 5.75 7.2 6.7 13.4 23.5 Normalized space velocity sn (s - 1) *10 - 5 44.8 18.1 17.3 27.9 6.19 1.6 1.1 3.3 Current efficiency % At 150 mA 55.6 38.7 19.4 15.1 At 50 mA30.7 19.32 8.45 8.7 Fraction conversion, % At rotation speed 300rpm 99.5 76 75.4 97.5 At flow rate 300l/h100 97.6 90.4 100 Mean value of the Space time yield (Kg m - 3 s - 1) 27.1 15.7 15 19.4 34.3 25 23.6 33.8 Normalized space velocitysn (s - 1) *10 - 5 36.7 At 300 rpm 38.7 At 100 rpm 19.4 At 100 rpm 15.1 At 100 rpm 5.3 At 400 l/h 1.5 At 300 l/h 1.4 At 300 l/h 4.4 At 300 l/h It is found that copper and lead ions have a catalyzed effect on the deposition of cobalt and cadmium, as they reduced the hydrogen evolution reaction especially at higher applied current and electrolyte velocity. Furthermore, the characteristics of the deposited metal that recovered from the RCE, were examined by X ray diffraction which show high purity metal and binary metal alloys with little amount of impurities as lead oxides where the presence of lead oxides had the effect on producing binary alloys. Copper metal exhibited strongly then secondly lead, which appeared in three different phases and the weekly existence, was for cobalt. Experimental results, analysis and correlations showed good performance of the cell on removal multi metal ions from simulated effluents. Although the FBPE configuration had the magnificent performance by comparing with RCE, RCE had acceptable performance also with comparison with previous workers.

تقليل الاعاقة في الجريان المضطرب باستخدام البولي اكريل امايد وصمغ الزانثان : دراسة عملية ونظرية == Turbulent Drag Reduction By Polyacryl Amide And Xanthan Gum, Experimental And Theoretical Investigation

Author name: احمد عدنان عطشان
Supervisor name: جبار شنشول جمالي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: This work presents an experimental study of the drag - reduction performance of two water - soluble polymers, Polyacrylamide(PAAM) as flexible, linear synthetic polymer and Xanthan Gum(XG) as a rigid polysaccharide from natural resources. The flow loop used consisted of 0.5 O.D. inch straight pipe with a test section of 3 m length. A 0.5 inch O.D. vertical tubing with elbows was also included to compare the drag - reduction behavior between both tubing configurations. Various concentrations of polymeric additive and water flow rates were tested. The results show that the drag - reduction in vertical piping are significantly lower than in straight type for both polymer type. The dragreduction efficiency of Xanthan Gum agent is much lower than polyacrylamide. Higher concentrations of XG about 150 ppm is required to get exactable drag - reduction performance about 12.84% in the straight pipe. While about 40.3% drag - reduction was achieved with about 50 ppm Polyacrylamide with the same conditions. Moreover, the drag - reduction efficiency of XG can be improved by mixing with Polyacrylamide agent at a given conditions.Part of the experimental work was devoted to study the performance of Polyacrylamide as drag - reducing agent with the existence of small amounts of sodium chloride acts as an inhibitor to the ability of the additive, resulting in lower drag - reduction probably due to collapse of PAAM at more compact structure with the addition of sodium chloride as strong ionic salt.Polyacrylamide and Xanthan Gum additive undergo undesirable mechanical degradation with increasing of circulation time, leading to lower drag - reduction performance. The molecular degradation is likely to occur at low additive concentrations and low turbulence flow, in vertical piping, since the polymeric additives are exposed to shear stresses.Further attempt was done in present investigation to find correlations for accurately predicting drag - reduction characteristics of drag - reducing agents, used in published works. A published time scale hypothesis for prediction of drag - reduction values, the friction factor data as a function of the polymer concentration, shear stress, Reynolds number, pipe diameter. The experimental friction factor results were taken from a published work for gas oil with polyisobutylenes. Good agreement between measured and predicted friction factor. Further attempt was made to correlate the mechanical degradation ability by modifying the Kouraush, Williams and Watt (KWW) equation. The experimental data were taken from a published work for Polyethylene Oxide. The modified equation was found to fit experimental data better than the original KWW equation.

تحضير عامل مساعد زيوت Y من قشور الرز العراقية لتطبيقات تكسير الهكسان == Preparation Of Zeolite Y Catalyst From Iraqi Rice Husk For Cracking Of n - Hexane

Author name: زينب محمد صبار
Supervisor name: نجاة جمعة صالح | بشير يوسف شرهان
General topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: Silica nano particles were prepared from Iraqi rice husk (al - Najaf province) by precipitation method. Rice husk (RH) was treated with two different concentrations of inorganic acid (i.e. 1 & 3 N HCl) then burning at 700 °C under two heating rates. Chemical composition of rice husk ash (RHA) determined by X - Ray fluorescence (XRF) was contained about 89.5 wt% and 95.2 wt% SiO2 by treatment with 1N HCl at 10 and 5 °C/min heating rates for 3 hrs, respectively. While, XRF analysis was given 97.5 wt% SiO2content in RHA by treatment with 3 N HCl at 5 °C/min heating rates for 2 hrs. 3N HCl and heating rate at 5°C/min seems to be the best method to reduce the metallic ingredients and to obtain highly purified nanosilica powder at a purity of 98.9 wt%.The prepared nanosilica was also characterized by X - ray diffraction (XRD), BET surface, Fourier transform infrared spectroscopy (FTIR) and Atomic Force Microscope (AFM), in order to investigate its properties.X - ray results revealed a strong single beak of 2? at about 22° with an amorphous phase. Surface area was measured for nano silica to be 298 m2/g. The average diameter of prepared nanosilica is 89.58 nm as obtained by AFM analysis. Rice husk is seen to be a frugal waste material, high silica content, and it will be able to apply as a natural source of silica for preparation the zeolite - Y catalysts rather than burnt or dumped it as waste, causing environmental and health problems. On the other hand, the commercial source of silica (i.e. Ludox As - 40) is industrially used with other materials for synthesizing the zeolite type - Y catalyst and economically it has an expensive cost. Hence, it is essential to find out another pathway for silica source.This work deals with the replacing of costly commercial precursors of silica by a cheap natural nano - source silica from Iraqi RH. As such this study focuses on the optimization of percentages of natural and/or commercial silica applied within either seed gel or feed stock gel in the zeolite - Y synthesis process in order to investigate the effect of the nature of the silica used on both the structural properties of produced of Y - catalyst as well as on the catalytic performance of these catalysts in hydrocarbon cracking reactions forimproving the production catalytic activity and selectivity. Commercial zeolite - Y catalyst was laboratory prepared by means of commercial silica source and named as “A” sample, whereas other four samples of zeolite catalysts were successfully synthesized with a desired zeolite - Y phase and so - called “B, C, D and E” using different percentages of natural silica source. All the achieved samples are investigated by characterization techniques (i.e. XRD, BET - surface area, Pore volume, FTIR SEM, AAS, and EDX). The synthesized HY - catalyst samples were catalytically tested in the cracking of Hexane (C6H14) through an experimental cracking rig, and the reaction products were analyzed by GC. The performance of Iraqi RH zeolite type - Y catalysts was compared with the commercial lab HY - catalyst. Catalyst B prepares from only natural nanosilicasource and in comparison with other synthesized Y - catalysts; it gives the best catalytic behavior with 98 - 95 mol% conversion together with the selectivity domination of isomer and normal paraffin within the reaction products during more than 2 hrs at 450 °C. This result confirms that the use of natural silica source can be enhanced the catalytic properties of zeolite type - Y catalyst.

دراسة تاكل الصلب الكربوني في محلول ملحي والمنتجات البترولية بوجود غاز ثاني اوكسيد الكربون == Studying of Carbon Steel Corrosion In Salt Solution And Petroleum Products In Presence of CO2

Author name: نضال احمد شاكر
Supervisor name: شذى احمد سامح | شروق طالب الحميري
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: يتضمن البحث دراسة سلوك التاكل للصلب الكربوني في محلول ملحي من (3.5wt%NaCl) ومشبع طبيعيا بالهواء بوجود غاز CO2 المستخدم في انابيب النفط. وتم تصميم منظومة القطب الاسطواني الدوار (RCE) لانجاز الدراسة.واجريت تجارب الاستقطاب في ظروف الجريان المضطرب باستخدام | The present work is to study the corrosion behaveior of carbon steel, in naturally aerated 3.5wt% NaCl (brine solution) and petroleum products in presence of CO2. A rotating cylinder electrode (RCE) system were used to study the potentiostatic polarization experiments, under turbulent flow conditions, using 3.5wt% brine solution as electrolyte at different temperatures (298, 308, 318 and 328)K and rotating speed of (0, 100, 200, 300 and 400)r.p.m. at each temperature.Similar experiments were carried out in 3.5wt% brine solution using CO2 gas at (32 ml/sec) flow rate.Corresponding experiments by weight loss were carried out in 3.5wt% brine solution with compunds of : - 1. Kerosene + 10V% brine solution.2. Gas oil + 10V% brine solution. At 328Kand flow rates of (0 and 400) r.p.m.3. Similar experiments were carried out in kerosene + 10V% brine solution at (298, 308 and 318)K and static condition speed of (0) r.p.m at each temperature.4. Experiments were carried out in pure kerosene at a temperature of (298 and 318) K and speed of (0) r.p.m.All above experiments were carried out with and without CO2 gas.The results indicated that the corrosion rate of carbon steel was increased in presence of CO2 gas.The anodic dissolution kinetics were activation control processes affected by temperature.The activation energy of carbon steel with CO2 gas system (2.87 - 1.8) Kcal/mol at different r.p.m. was lower than that without CO2 gas system of (11.4 - 1.7) Kcal/mol at different r.p.m.The corrosion potentials without CO2 gas were shifted to the noble direction with increasing flow rate at a constant temperature, whereas such potential were shifted to the less noble direction with increasing temperatures at a constant speed. However, the corrosion potential with CO2 gas was more noble than that obtained without CO2 gas.The corrosion rate is increased with increasing temperature and velocity. The results indicated that the corrosion rates of ( gas oil +10V% brine solution ) are higher than that of (kerosene +10 V % brine solution) with and with out CO2 gas, and the corrosion rate of pure kerosene is lower than that of (kerosene+10V% brine solution) with and without CO2 gas.In the presence of CO2 gas the results indicated that corrosion rate increases due to continuous dissoultion of iron ion and formation of weak carbonic acid. The carbonic acid accelarteed corrosion rate and affected carbonate and hydrogen ion, which increased the cathodic reactions on the metal surface.

دراسة تاثير بعض متغيرات عملية الترسيب الكهروكيمياوي للنحاس على كفاءة العملية وخواص المسحوق المنتج == The Study of The Effect of Some Variables In Electrochemical Deposition of Copper Powder On The Efficiency of Process And Powder Properties

Author name: ميادة نوار نصيف
Supervisor name: فاروق منصور مهدي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Salahaddin
First pages:
Abstract: يهدف البحث الى اجراء دراسة عملية لانتاج مسحوق النحاس باستعمال طريقة الترسيب الكهروكيمياوية مع دراسة تاثير عدد من المتغيرات التي تؤثر في كفاءة العملية والوقوف على طبيعة تاثير كل منها. تمت دراسة تاثير كل من كثافة التيار وزمن الترسيب ودرجة حرارة وسط الترسيب | The present study aims to produce copper powder by the electrochemical deposition method. In this work, the effect of current density, deposition period, electrolyte temperature, distance between electrodes, ratio of anode to cathode surface area and cathode rotation on the current efficiency and powder properties such as apparent density, grain size, grain size distribution and grain morphology on powder properties and current efficiency are studied. A deposition system composed of Perspex cell, two copper electrodes ( 96.8% purity), electrolyte composed of 90g/l CuSO4 and 120g/l H2SO4 as well as the electrical connections. Betts method was followed by this study.The automatic sieve shaker was used to determine the grain size, while the atomic spectroscopy was used to determine copper purity. Moreover, both optical microscope and SEM were used to estimate powder morphology. It is found that current efficiency is increased with increasing deposition time and electrolyte temperature. It is also found to be decreased with increasing current density, distance between the electrodes, ratio of anode to cathode surface area and rotation of cathode electrode. The results showed also that particle size is increased with increasing the distance between the electrodes and increased with increasing the ratio of anode to cathode surface area and cathode rotation. Further more, the obtained data indicated that the maximum and minimum achieved fine grain percent (

تاثير الجزيئات وحجم الندف على معالجة المياه بواسطة العمليات الفيزيائية - الكيمياوية لمياه النهر == Effect of Particle Floc Size On Water Treatment By Physico - Chemical Process

Author name: مهند ابراهيم فرحان
Supervisor name: ثامر جاسم محمد
General topic: Chemical Engineering
Specific topic: Chemical Processes
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: يتضمن هذا العمل دراسة تاثير حجم الجزئيات وحجم الفلوك المتكون على عملية التخثر - التلبيد عن اضافة المخثرات واجريت التجارب باستخدام عينة من الماء الطبيعي التي اخذت من نهر دجلة، مع في مستوى ( 55 NTU ) التعكر. واستخدمت ( Jar - test ) لتحديد الظروف المثلى لازا | This work includes the study of the effect of particle size and floc size formed on the process of coagulation - flocculation by the addition of coagulants.Experiments were conducted using a sample of natural water which was taken from Tigris River, within the level of (55) NTU turbidity. Jar - test was used to determine the optimal conditions for the removal of turbidity through coagulation - flocculation and sedimentation.Several experiments were carried out to investigate the effect of flocculation time 1,6 and 20 min, coagulants dose and camp No. on the residual turbidity or removal efficiency ,floc size or floc formed that have greater Intensity, floc strength and recovery factor, largest volume, greater surface area and the most number and properties of electrical particle such as (zeta potential ,mobility , frequency). The floc growth, breakage floc size and regrowth of different type of coagulant were investigated by a laser diffraction particle sizing device (zeta plus).The coagulants used were alum, FeCl3, polyelectrolyte (PE), alone or in combination of them.

اداء المبادل الحراري الارضي الاحادي المسار باستخدام موائع تشغيلية مختلفة == Peformance of A Single Pass Earth - Tube Heat Exchanger Using Different Working Fluids

Author name: مصطفى جواد نعمة
Supervisor name: غزوان احمد محمد | عباس خلف محمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: العديد من التقنيات استخدمت لتحسين معدل الانتقال الحراري لاختزال حجم المبادلات الحرارية وتشغيلها باقل كلفة0المبادلات الحرارية الارضية استخدمت وبشكل واسع وذلك لتحسين تقنيات التبادل الحراري في العديد من التطبيقات الصناعية0المبادل الحراري الارضي هو اداة تسمح | Several techniques have been applied to enhance heat transfer rate in order to reduce the size of heat transfer devices and also operating cost. Earth tubes have been used as one of the most widely used heat transfer enhancement techniques in several industrial applications. Earth tube heat exchanger is a device which permits transfer of heat from fluid to deeper layers of soil and vice versa.The results of the heat transfer characteristics in earth tube heat exchanger are presented. The experimental test section is made of 50 m carbon steel pipe of 19.05 mm inner diameters and 25.95 mm outer diameters. The pipe was buried 2 m deep below ground surface. Water and gasoil were used as working fluids in the experimental runs. Experiments were performed under conditions of volumetric flow rates ranging from 0.5 to 2 m3/h and inlet working fluids temperature is between 35 to 70?C at winter season and between 50 to 70?C at summer season. Working fluids temperatures were measured at five points with equal length by thermocouples placed inside the pipe. Also, soil temperatures were measured at these points by thermocouples placed 0.5 m apart from pipe. The effects of working fluid flow rate, inlet temperature, pipe length on the overall performance of the earth tube heat exchanger was investigated at winter and summer seasons, respectively.It was shown that the heat transfer rate of the working fluid increases as the pipe length and inlet temperature increase, or volumetric flow rate decreases. Furthermore, the heat transfer rate in the first half of the pipe represents (33.3 to 87.5%) from the total heat transfer rate, depending on working fluid operating conditions. Also, it was noticed that the heat transfer rate in summer days is less than in winter days. Coefficient of performance (COP) analysis was also carried out to characterize the system performance at different operating conditions. The experimental earth tube heat exchanger (ETHE) system was attained a maximum COP of 45.589 at winter tests and 17.818 at summer tests for water as working fluid. But, the maximum COP was reached only 28.52 for gasoil as working fluid at summer.

تحسين اداء مفاعل الطبقة الوشله المشغل بالحالة الغير مستقرة لمعالجة المياه من ملوثات الفينول == Performance Enhancement In Unsteady State Operated Trickle Bed Reactor of Phenolic Wastewater Treatment

Author name: غيداء ضياء الدين نجيب
Supervisor name: صفاء الدين عبد الله النعيمي | فرح طالب السوادني
General topic: Chemical Engineering
Specific topic: Chemical Processes
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تضمن البحث دراسة عملية ونظرية لاكسدة محلول الفينول بطريقتي (CWAO & PP - CWAO) باستخدام عمود الطبقة الوشله Trickle Bed Reactor لكل من التشغيل المستقروالتشغيل الدوري (Unsteady Periodic Operation) والمتضمن التقطيع الدوري لمعدل جريان السائل (Liquid Flow Mod | Catalyst Wet Air Oxidation (CWAO) and Hydrogen Peroxide Promoted Catalytic Wet Air Oxidation (PP - CWAO) of phenol in aqueous phase are studied experimentally and theoretically in this work using a trickle bed reactor operating in both steady state and periodic operation; liquid flow and hybrid modulation. A laboratory unit was constructed for this purpose, where a versatile reactor setup required "high pressure stainless steel reactor of 0.018 m i.d.×0.76 m height", in which experiments could be carried out under different modes of operation. The effect of key parameters that influence on the performance of trickle bed reactor (TBR) for CWAO and PP - CWAO is studied in a steady - state operation to provide a basis for comparison with periodic experiments and kinetic measurements in TBR under constant operating pressure (0.1 MPa) throughout Initial phenol concentration (0.84 - 1.5 g/L), liquid hourly space velocity (1.16 - 19.87 h - 1), superficial gas velocity (0.163 - 0.655 m/s), and bed temperature (30 - 80oC) for CWAO. Hydrogen peroxide concentration (5 - 40%) and feed rate (0.0499 - 0.1465 L/h) for PP - CWAO at constant liquid hourly space velocity (1.16 h - 1), initial phenol concentration (1.35 g/L), superficial gas velocity (0.163 m/s), and bed temperature (80oC).In periodic operation, the effect of cyclic parameters is investigated in a broader range of cycle period (5 - 180 sec) and split (0.2, 0.5 and 0.7) for both liquid flow and hybrid modulation under some of the conditions chosen on the basis of the steady state results for PP - CWAO.The results showed that the CWAO and PP - CWAO of phenol are kinetically controlled. In CWAO, LHSV and air flow rate have a slight effect on the phenol conversion, whilst they have a positive effect on the rate of reaction. The conversion and reaction rate of phenol increase with increasing initial phenol concentration and bed temperature, but they have a little pronounced effect in the range of temperature. The highest phenol conversion (75.26%) was obtained over Pt/? - Al2O3 at LHSV=1.16 h - 1, bed temperature=80°C, air flow rate=10 L/min and initial phenol concentration=1500 ppm.For PP - CWAO, the promoting effect of hydrogen peroxide was less marked in the range (5 to 25) %H2O2 concentration while at (35 - 40) %H2O2 concentration, the removal efficiency became more pronounced where the phenol conversion enhanced from 73.26% conversion at 25% H2O2 to 88.88% conversion at 40% H2O2. Hydrogen peroxide flow rate has a negligible effect on the removal of phenol. According to the kinetic results, the reaction kinetic was pseudo first order with respect to phenol concentration, (0.3) order with respect to oxygen, and the apparent activation energy equals to (19.8247) kJ/mol. The rate expression for CWO is - r_ph= C_ph^ For periodic operation, the time average conversion enhancement is indeed quite considerable in liquid flow modulation as split is lowered from steady state (? =1) to a value of (? =0.5) and reached as much as 6.66 % over the steady state at cycle period (?_p)= 15 sec; which is close to the hybrid modulation, where enhancement reached to 6.91% at ? =0.2 and (?_p)=5 sec.Intermediate compounds were analyzed for CWAO and PP - CWAO in steady state operation. Four intermediate compounds were indicated, namely oxalic acid, acetic acid, formic acid and maleic acid (carboxylic acid). Acetic acid being the main refractory intermediate in the catalytic oxidation of phenol at the operating conditions employed for CWAO process in steady state operation. The PP - CWAO of phenol in steady state and periodic operation has a positive impact on the intermediate compound mineralization as compared with the CWAO in steady state operation. In the modeling part, a suitable reactor scale model is evaluated and extended to predict the performance of TBR under the employed conditions. The model was solved numerically by finite difference approach with a semi implicit solution of the differential equations. The simulated results for steady - state and periodic operation (liquid flow modulation) performance showed that the expected trends in performance enhancements as experimental results. The experimental data results showed the relative error for the conversion (1.22 - 8.9%) in the broad range of experimental.

معالجة الماء الحاوي على النفط في حقول نفط العراق الجنوبية == Oily Water Treatments For Southern Iraqi Oil Fields

Author name: عقيل شيخة عرفات
Supervisor name: خالد مخلف موسى
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: عمليات الحفر تنتج كميات كبيرة من الماء الملوث يعرف بالماء المنتج او الماء المنتج من البئر. مختبريا تم التحقق باستخدام Autoclave بحجم لتر واحد مصنوع من مادة الصلب stainless steel لمعالجة الماء المنتج من حقول الرميلة الشمالية والزبير الخطوة الاولى استخدمت م | The oil drilling operations create large quantities of contaminated water known as “Produced Water” (PW), or water that is produced from the well. An experimental investigation was conducted using 1litter stainless steel autoclave to treat the oily water produced from North Rumaila and Zubair oil fields. The first approach was a pretreatment to remove solid particles using sedimentation with and without flocculation. The second approach included studied the effect of pH, pressure, temperature, salinity, operation time, outlet time and RPM. The third approach was investigate the effect of the surfactants (detergents and alcohol) to reduce surface tension, finally, was addition of some sorbents like polypropylene, polyethylene, used plastic and sawdust.The ranges of salinity, pH, pressure and temperature were selected according to the PW conditions which out from dehydrator and desalter (80000 ppm, 6, 3bar and 60°C respectively), the RPM of mixer was selected to satisfy laminar flow, while the time of operation and outlet product represented the minimum residence time in batch reactor and its discharge to choose the minimum design cost. The results showed that the best conditions were : - Pressure =1 bar, temperature =45°C, mixer speed =300 RPM, treating time =15 min and skim time starting =5 minutes. Best additives to reduce surface tension : ethanol volume = 0.05vol %, powder detergent = 400 mg/litter and liquid detergent volume = 0.03vol%. Best sorbents : Sawdust amount addition = 2.5 gm, polypropylene = 4 gm, polyethylene = 3 gm and used plastic = 2.5 gm The results showed that using polymers made a great change in the oil recovery percent (all the oil was recovered).

اكسدة ايون الحديدوز الى ايون الحديديك باستخدام المضافات في العمود ذو الفقاعة == Oxidation of Ferrous To Ferric Ion By Additives In Bubble Column

Author name: صباح محمد حسن الجبوري
Supervisor name: رافع جمال يعقوب
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Salahaddin
First pages:
Abstract: تم دراسة اكسدة كبريتات الحديدوز الى كبريتات الحديديك من خلال التركيز على اختبار تاثير الظروف التشغيلية للمنظومة على عملية اكسدة كبريتات الحديدوز بالهواء ومن ثم دراسة تاثير المضافات في اتمام عملية الاكسدة باستخدام الاوكسجين في العمود الفقاعي. تم استخدام ا | This study was discussion converting of ferrous sulfate to ferric sulfate by oxidation with using the bubble column and concentrates by using air and then studied the effect of additives to complete the oxidation with oxygen. Air is used as an oxidation agent in the first step to study the oxidation reaction in bubble column with(5 cm inside diameter ,120 cm tall ), in this part of process, studying the operation condition on the oxidation and determining the rate of conversion. Temperature ( 50,60 and 70 )°C ,air flow rate (100,150,200 and 250)L/h and initial concentration of ferrous (0.5 , 0.25 , 0.1 and 0.05 )M with fixing the pressure slightly up to 1 atmosphere are used to study the performance of the parameters (initial concentration ,temperature and air flow rate on oxidation ferrous sulfate.The effect of these conditions are studied throughout the experimental work to increase the conversion rate of ferrous sulfate.The results are shown that the maximum conversion rate is 53.5% at the temperature 70 °C ,air flow rate 150 L/h and initial concentration of ferrous is 0.1M.The results of the optimum conditions are depended on the second part of this work by using oxygen gas and additive material, (CuSO4, KMnO4, H2O2 and HNO3) at the different concentration (100 , 200 , 300 , 400 , 500 ) ppm, the effect of each material is studied to show the conversion rate of ferrous to ferric sulfate.The test of these material gave different results for each material and gave different result for each concentration of additive on the conversion rate of ferrous.The best result is that the conversion rate is 81.1 % by using CuSO4 at additive concentration 400ppm, the conversion rate is 78.9% by using HNO3 at concentration of additive 200 ppm , the conversion rate is 73.1% by using KMnO4 at concentration of additive 400 ppm and the conversion rate is 70% by using H2O2 at concentration of additive 200 ppm.Mathematical correlation for each additive and the main operating variables on oxidation of ferrous to ferric sulfate are solved by using (Excel) program are illustrated : - (d[?Fe?^(+2)])/dt=0.612067 t+0.011378 Cadd ? 2.86622.

ازالة الكبريت ودراسة الحركية لوقود الديزل بعملية الامتزاز ذو الوجبة باستخدام الكاربون المنشط == Desulfurization And Kinetic Study of Diesel Fuel By Batch Adsorption On Activated Carbon

Author name: سمر خالد الجنابي
Supervisor name: نيران خليل ابراهيم
General topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: منتجات التقطير في المصافي , وخاصة قطفة زيت الغاز تحتوي على كميات كبيرة من مركبات الالكيل - بنزوثيوفين والتي هي الاكثر تمردا لازالة الكبريت عن طريق السلفرة الهيدروجينية التقليدية. وتستمر لوائح الوقود في جميع انحاء العالم في التشديد استجابة للحاجة الملحة | Refinery distillates, especially gas oil fractions contain considerable amounts of alkylated benzo - thiophene which are the most recalcitrant to desulfurization via conventional hydrodesulfurization. Fuel regulations continue to tighten worldwide in response to the need to cleaner air and refiners meet these regulations at a very significant cost. The need to cut the operational and capital costs has necessitated a renewed look to the non - hydrogen, low temperature and pressure processes for producing ultra low sulfur fuels.Non - conventional approaches for ultra low - sulfur fuels belong either to oxidative or a selective adsorption routes. The present research focuses on a batch adsorption desulfurization process for diesel fuel containing 580ppm sulfur, based on physical adsorption of refractory sulfur compounds on activated carbon (AC). The effects of time (0 - 3.5 hr), temperature (30 - 70 °C), diesel to AC ratio (2 - 10 ml/gm), AC particle size (0.2 - 1.44 mm), mixing velocity(100 - 1000 rpm), and initial sulfur concentration (280 - 580ppm) in commercial diesel fuel on the desulfurization efficiency were studied. The residual sulfur concentration in diesel fuel was decreased from 580 to 247 ppm, corresponding to a desulfurization efficiency of 57 %, at best conditions of 2.5 hr contact time, 50 ?, 2ml diesel/gm AC, 0.8 mm AC particle size, and 1000rpm mixing rate. The sulfur adsorption dependency on contact time and initial sulfur concentration in commercial diesel fuel (280 - 580ppm) were studied. Different kinetic models : Pseudo - first order (PFO), pseudo - second order (PSO) and intraparticle diffusion models were applied to fit the experimental data. The results of the kinetic analysis showed that the pseudo - first order model underestimates the equilibrium sorption capacity by about 33%. However the pseudo - second order model has succeeded in predicting the equilibrium sorption capacity with correlation coefficient, R2 = 0.995. The experimental adsorption isotherms were correlated by Langmuir and Freundlich models. The results indicated that Freundlich isotherm exhibits the best fits for the adsorptive desulfurization of diesel fuel with correlation coefficient (R2) of 0.989 as compared with the Langmuir model ( ). The adsorption intensity as estimated from the Freundlich isotherm is larger than one which is indicative of physical adsorption.

ازالة المحتوى الكبريتي بالاكسدة العميقة باستخدام الكاربون المنشط المحفز == Deep Oxidative Desulfurization Using Catalyze Activated Carbon

Author name: ياسمين منذر جاعد
Supervisor name: ودود طاهر محمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: ازالة المحتوى الكبريتي من الوقود هي قضية بيئية حاسمة على نحو متزايد. عملية الهدرجة(HDS) تزيل المركبات الكبريتية مثل المركبتان والكبريتيد من الهيدروكربونات، ولكن بعض الكبريت - يحتوي على مركبات (مثل dibenzothiophene) من الصعب جدا ازالتها وتحتاج عمليات عميقة | Removal of sulfur species from fuels is an increasingly critical environmental issue. Hydrodesulfurization (HDS) removes sulfur compounds, such as mercaptans and sulfides from hydrocarbons; however, some sulfur - containing compounds (such as dibenzothiophene) are very difficult to remove and need deep desulfurization processes.This work was applied to the desulfurization diesel fuel produced from the conventional HDS process or ultra - desulfurization. The used fuel types were either real diesel fuel or simulated diesel fuel, where sulfur - containing compound (dibenzothiophene) converted to its corresponding sulfone by oxidation using hydroperoxide as an oxidant and formic acid as cocatalyst with activated carbon (AC), in addition to its adsorbent virtue. Simulated diesel fuel according to British Petroleum 200B doped with dibenzothiophene was prepared.The experimental study was divided into two parts, preliminary study, that include thermally (activated carbon with heat treatment (ACH)) and chemically treatments (i.e. activated carbon impregnated with copper (Cu/AC), activated carbon impregnated with nickel(Ni/AC), activated carbon impregnated with copper and nickel (Cu - Ni/AC) and activated carbon with nitric acid treatment (ACN) ) to the parent activated carbon, these types were tested at different operating conditions (i.e. temperature = 25 and 60 ?C, pH=2, H2O2/diesel fuel ratio=3/100 and activated carbon doses = 0.7 and 1.0 g) to achieve the best one that gives higher desulfurization efficiency. ACM that is a mixture of ACH and ACN (equal percentage) gives 80% sulfur removed at operating conditions of temperature= 60 ?C, pH=2, H2O2/diesel fuel ratio=3/100 and ACM doses = 0.7 g. In general, the activity of activated carbons as follows ACM >ACN > ACH > Ni/AC > Cu/AC > Cu - Ni/AC > parent AC While, the second part represents the main study, that deals with the desulfurization process in details, using ACM with operating conditions of temperature of 60 - 80 ?C, pH of 0 - 4, H2O2/diesel fuel ratio of 3/100 to 7/100 and ACM doses of 0.5 to 1.0 g Maximum desulfurization efficiency achieved was 92.3% at operating conditions of temperature= 80 ?C, pH =0, H2O2/diesel fuel ratio= 5/100 and ACM dose =1.0 g.Finally, two experiments with the best conditions above were done on the real diesel fuel. Maximum desulfurization efficiency was 25% at temperature= 80 ?C, pH =0, H2O2/diesel fuel ratio= 5/100 and ACM dose =1.0 g.

معالجة مياه المصب العام للحقن في حقل الناصرية النفطي == Water Treatment of Main Outfall Drain For Injection In Nasiriyah Oil Field

Author name: جعفر جبار مدلول
Supervisor name: احمد فائق العلوي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: يهدف العمل الحالي لانتاج مياه ملائمة للحقن في حقل الناصرية النفطي من المصب العام يتكون الجزء العملي من هذا البحث من ثلاثة مراحل(1) التخثير/ التلبد , (2) مرشح ماء الجاذبية الطبيعية او غشاء دقيق و(3) تقنية اغشية النانو. المرحلة الاولى, تخلص عملية التخثير/ | The aim of the present work is to produce water appropriate for injection in Nasiriyah oil field from Main Outfall Drain (MOD). The experimental work in this research consists from three stages (1) coagulation/ flocculation, (2) natural gravity water filter or microfiltration membrane (MF) and (3) nanofiltration membrane (NF) technology. The first stage, coagulation/flocculation process removed the suspended solids from MOD and reduced the turbidity to the demand limits. The variables studied were initial turbidity (11.8 - 100 NTU), coagulant dosage (0 - 55 ppm), speed of the slow mixing step in the jartest apparatus (2nd step) (20 - 40 rpm), time of 2nd step (20 - 40 min), and settling time (10 - 50 min). Turbidity increases by increasing initial turbidity and decreases by increasing the coagulant dosage, speed and time of 2nd step and settling time until the reaching to the optimum for them at the minimum turbidity, then any increasing of the coagulant dosage, speed and time of 2nd step will increase the turbidity, while any increasing of settling time will do no effect on turbidity. The optimum dosage for alum was 35, 40 and 50 ppm. While, for ferric chloride it was 15, 20 and 30 ppm and for polyelectrolyte 4, 8 and 10 ppm for 11.8, 30 and 100 NTU initial turbidity respectively. The optimum speed of 2nd step was 25 rpm for each of alum (35 ppm), ferric chloride (15 ppm) and polyelectrolyte (4 ppm). While the optimum time of 2nd step was 30 min for each of alum (35 ppm), ferric chloride (15 ppm) and polyelectrolyte (4 ppm) and settling time was 30 min for each of alum (35 ppm), ferric chloride (15 ppm) and polyelectrolyte (4 ppm). The second stage, natural gravity water filter or microfiltration MF was used to ensure that the particle size was in the demand limits (less than 10 ?m) and reduce the turbidity and the total suspended solids (TSS) to the demand limits (5 NTU and 3 - 3.5 mg/l). It was found that turbidity and TSS increases by increasing the inlet turbidity and TSS and the results was arranged progressively as the following : Natural gravity water filter ? 5 ?m MF ? 1 ?m MF. The final stage, nanofiltration NF membrane technology was used to remove sulphate from MOD. The variables studied were feed concentration (1800 - 9630 mg/l) and operating temperature (27 - 37 oC). Also concentrate recirculation was used to obtain high recovery percentage of water can be inject. It was found that product flow rate increases by increasing temperature and decreases by increasing salts concentration in feed. Also it was found that salts concentration in product increases by increasing feed concentration and temperature. Rejection percentages were (94.475 - 95.631 %), (88.088 - 90.714 %), (83.33 - 93.2 %), (85.116 - 92.727 %) and (65.385 - 72.727 %) for sulphate, total hardness (TH), Ca2+, Mg2+ and Cl - respectively and recovery percentage of product water was (11.429 - 38.143 %) for polyamide membrane (TFC). In the case of concentrate recirculation, feed concentration, permeate concentration and volume of permeate increases with increasing in operating time and 12.69 liter of water valid for injection in oil field was recovered from 25 liter feed after 180 minute.

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
Degree: Higher Diploma
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.

السلوك التاكلي للحديد الكاربوني في نواتج المياه للصناعات النفطية المحتوية على غاز CO2 == Corrosion Behavior of Carbon Steel In CO2 - Containing Oilfield Produced Water

Author name: خالد حامد رشيد عبد الخالق
Supervisor name: ابرائيل سركيس يارو
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: ان وجود غاز ثاني اوكسيد الكاربون ( (CO2في طبقة الماء المالح بشكل غاز مذاب تحت ضغوط عالية والمصاحبة للنفط الخام يكون حامض الكاربونيك. الحديد المطاوع يشغل المادة الاساسية في تركيب خطوط الانابيب الناقلة في الصناعة النفطية والغازية , بسبب رخص ثمنها , مقاومته | Carbon dioxide is present in water as a dissolved gas under the high pressures common in underground oil and gas reservoirs. In the dissolved state it forms carbonic acid. The primary material of construction for pipelines in the oil and gas industry is mild steel, because of its price, strength and availability. However, carbon steel corrodes in the presence of carbonic and organic acids such as acetic acid (HAc). It is therefore important to investigate the conditions in which HAc causes corrosion damage to mild steel. The extent of HAc/CO2 corrosion depends on many other variables such as : temperature, CO2 partial pressure, pH, flow regime, etc.The corrosion rates of API X65 mild steel alloy have been studied by three different techniques : i. Weight Loss Technique.ii. Potentiodynamic Polarization Technique.iii. Characterization of the Corroded Surface Techniques.i. Weight Loss Technique : A series of experiments were performed to study the effect of simulated brines solutions on the corrosion rate of mild steel with and without acetic acid. The corrosion rates of mild steel were found to be similar in simulated brines solutions and 3.5 wt % NaCl solutions. The corrosion experiments were planned to form a second - order mathematical expression using Full Factorial Experimental Design (FFED) : a - Four variables experiments (influence of temperature, solution pH, acetic acid (HAc) concentration and speed of rotation). b - Three variables experiments (influence of temperature, solution pH and speed of rotation).The results of this investigation are summarized as follows : The second - order polynomial regression analysis of the objective function (corrosion rate), using Full Factorial Experimental Design (FFED) via STATISTICA software, gave two mathematical expressions for four and three variables experiments. Arrhenius Equation and Transition State Equation were used to evaluate the activation parameters : Activation Energy (Ea), Enthalpy of Activation (?H*) and Entropy of Activation (?S*). The values of average Equilibrium Constants (K*) were also calculated at each value of average Gibbs Free Energy Change (?G), to determine the spontaneous of corrosion reaction. The corrosion rate of mild steel in presence and absence of acetic acid were increased with increasing of temperature, acetic acid (HAc) concentration and speed of rotation, but decreased with increasing of pH of solution. Multi - variable regression analysis of objective function (corrosion rate) in presence and absence of acetic acid in weight loss technique as a function of experimental variables (temperature, solution pH, acetic acid (HAc) concentration and speed of rotation), yielded two suggested mathematical expressions.ii. Potentiodynamic Polarization Technique : In this investigation a theoretical model Equation proposed by Korobove and Medvedeva Korobove and Medvedeva, [2000] was used to analyze the shape of polarization curves. The values of polarization resistance (Rp) were also obtained, these values were increased with decreasing of temperature and speed of rotation in absence and presence of the protective film formation. The polarization resistance values in absence of acetic acid are larger than the polarization resistance values in presence of acetic acid, due to the formation of the protective film.The values of mass transfer correction factor (?) were also obtained, these values will approach unity at low overpotential and it decreases as overpotential increases in presence and absence of the protective film formation. Generally, in absence of acetic acid, the values of (?) are adjacent to each other and almost unite value compare with presence of acetic acid at different temperatures and speeds of rotation due to the protective film formation as diffusion barrier is accelerated by measures that restrict the transport of reaction products from the surface.The limiting diffusion currents of hydrogen in CO2 saturated, 3.5 wt% NaCl solutions under turbulent conditions in presence and absence of the acetic acid has been correlated. iii. Characterization of the Corroded Surface Techniques : The effect of presence and absence of the acetic acid (HAc) on the CO2 corrosion of grade API X65 mild steel alloy was investigated at optimum conditions in weight loss technique (45.4 °C, pH 4.8, 2178.5 ppm HAc and 1296.6 rpm) and in absence of acetic acid (68.7 °C, pH 7.9 and 1425.8 rpm) by using analyses of protective film thickness, porosity, roughness, Vickers micro - hardness (VMH), scanning electron microscopy (SEM), computerized metallurgical optical microscopy technique (CMOMT) and X - ray diffraction (XRD). In presence of acetic acid, a porous layer (Fe3C cementite/FeCO3 siderite layer) was formed. In absence of acetic acid, a fairly dense layer ferrous carbonate (FeCO3 / siderite layer) was formed. In absence of acetic acid, the roughness and hardness of protective film were greater than that of film formation in presence of acetic acid.

تسريع انتاج الخل بالطريقة المستمرة == Speeding - Up The Production of Vinegar By Continuous Ferementation

Author name: خليل عيدان حمد الدليمي
Supervisor name: عبد القهار مهدي محمد السامرائي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: Arabic
University location: Salahaddin
First pages:
Abstract: تمت الدراسة على جهاز تخمير ريادي؛ باستخدام الطريقة المستمرة في انتاج حامض الخليك ومن ثم اجراء تقييم للظروف المثلى في عملية الانتا م في هذا البحث دراسة تاثير المتغيرات (معدل تدفق الهواء, وسرع المزج, ودرجة الحرارة ,والدالة الحامضية (pH ), وتركيز الاوكسجين ا | The research has been achieved by means of fermentation system by Continuous method to produce acetic acid and then evaluation of the optimum condition of production process. This research aims to study the effect of some operation variables like (air flow rate, speed of mixing, temperature, acidic function ( pH ) , and dilution rate of alcohol ) , on acetic acid production. The operation conditions that worked are (air flow rate ( 1 - 4) m3 / hr ) , speed of mixing( ( 50 - 400) rpm ) temperature (( 18 - 33)C? ) , and dilution rate ( ( 0.005 - 0.02) hr - 1 )). The optimum operating conditions to produce acetic acid by continuous process are as follow : (air flow rate ( 3 m3 / hr ) ,speed of mixing (100 rpm) , temperature ( 30 C? ), dilution rate of alcohol(0.005 hr - 1) initial alcohol concentration ( 48 g / l ) and initial concentration of acetic acid ( 40 g / l )).. The biological variables of acetic acid bacteria have been studied in the fermentation process in continuous method ( concentration of living mass , consumed alcohol , the produced acetic acid and the dissolved oxygen concentration) in addition to the lateral variables of the process ( aeration flow rate, speed of mixing , temperature , function of acidity and dilution rate ) as algebraic differential equations Mathematical models of the continuous process of fermentation process (used as simulation solutions).

معالجة عناصر الخارصين والنحاس والمنغنيز في مياه الفضلات الصناعية بطريقة الترسيب الكيمياوي == Treatment of Zinc ,Cupper And Manganese In Wastewater By Chemical Precipitation

Author name: يوسف صالح عيسى
Supervisor name: دريد فاضل احمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: Arabic
University location: Salahaddin
First pages:
Abstract: تهدف هذه الدراسة الى ايجاد تاثير المعالجة الكيمياوية بطريقة الترسيب الكيمياوي على كفاءة ازالة العناصر الثقيلة في مياه الفضلات الصناعية المطروحة لتصل الى النهر بالتراكيز المسموح بها. تتم عملية الترسيب الكيمياوي بالسيطرة على الدالة الحامضية لمياه الفضلات ب | This study aims to find the effect of chemical treatment by chemical precipitation on the efficiency of removing heavy metals from wastewater to be poured back to the river. Chemical precipitation is done by controlling the (PH) of wastewater by adding a suitable hydroxide ,different hydroxides were used like the hydroxides of sodium ,calcium and potassium 0.05N each and sodium carbons 0.1N in removing heavy metals of wastewater. The study has taken prepared samples contain different concentrations of heavy metals ions like cupper 2,4 and 6 ppm zinc 5,10 and 15ppm and manganese 2,5,8 ppm Jar taste is used to show the chemical precipitation. Fast and slow mixing periods were written down to get the velocity gradient (G) and (GT) The used materials were highly efficient to remove the ions of metals. The removed amount of metals was measured by (AAS) Atomic Absorption spectroscopy. The paper has also studied the effective factors on the efficiency of precipitation like the (PH) is (8,9,10,11) and The precipitation time is (0.5,1,2,3)h.The result show that the best precipitation efficiency when an ion is used alone in the solution (PH) is (10,11) precipitation time 2h hydroxides precipitation (0.05N) it removes about 98% of cupper ions when sodium and calcium hydroxides are used ,more than 96,66% when the potassium hydroxide is used.a complete removing appears of manganese ions when the calcium hydroxide is used more than 90% when the potassium hydroxide is used.77% when the sodium hydroxide is used more than 98.4% of zinc ions removed when the sodium and calcium hydroxide is used 95.9% of zinc ions is removed when the sodium carbons are used the best treatment condition appear when the (PH) is (9 to10) and precipitation time is 2h when an ion is used alone in the solution 98% of cupper and zinc ions are removing 90% of manganese ions.When the ions are mixed in the solution the best removing efficiency appears when the (PH) is (9 to 11) and precepitition time is 2h when the hydroxides and carbons are used a complete removing of cupper ions 90% of zinc ions and more than 98.2% of manganese ions.The time of reaction to get 10.5 PH using hydroxides is (25 - 30) second when sodium carbon's are used the reaction time to get 8.5 is (50) second for cupper and zinc ,(25) second for manganese.The reaction is zero order when hydroxides are used and first order when carbons are used in treating heavy metals.

المعالجة البايولوجية في المياه الصناعية المصرفة لتخفيض تركيز الميثانول == Bioremediation of Industrial Wastewater For Reducing Methanol Concentration

Author name: نغم اديب عبد الكريم
Supervisor name: Mahmood M. Barbooti | Mumtaz A. Zablouk
General topic: Chemical Engineering
Specific topic: Biochemistry Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تعتمد المعالجة البايولوجية للمياه الصناعية المصرفة على عملية بسيطة وذلك بتامين الكائنات الحية التي لها القدرة على تفكيك المركبات العضوية حيث تستغلها البكتريا كمصدر للتغذية.ان اغلب المركبات العضوية واللاعضوية يمكن ازالتها بصورة فعالة من خلال المعالجة الباي | The present work biological treatment by activated sludge is advocated to reduce methanol concentration in wastewater.Activated sludge is prepared in laboratory from contaminated soil with heavy hydrocarbon. Aerobic biological treatment is applied for synthetic wastewater containing 2 gm/L methanol. Important operating parameters in this system are the sludge volume, temperature, pH and total time. Investigating these parameters can establish sufficient microbial mass for efficient treatment. The treatment is carried out under various conditions of temperature (20, 30 & 40) 0C, pH (6, 7 & 8), total treatment time (2, 3 & 5) days and for different sludge volume (100 ,280 & 450) ml. The best volume used is 280 ml from the prepared activated sludge which gives best removal down to 160 ppm. Treated wastewater samples were collected at different time and stored in deep freeze.The stored samples are analyzed for methanol content by direct injection to Gas - Chromatography. From the experimental investigation results, it has been shown that the aerobic biological treatment is efficient in reducing methanol concentration in treated wastewater. The addition of 280 ml of sludge to seven liters of synthetic wastewater gives maximum removal of methanol. The results are analyzed mathematically. The experimental data collected by this sludge volume are successfully fitted to a second order polynomial empirical correlation.The most favorable operating conditions for the 280 ml sludge volume are 400C temperature, pH = 6.8 and 102 hr total treatment time with 30h aeration.On the basis of the best conditions obtained the empirical correlation, is obtained as follows : Y = 14616.62 - 17.4202X1 - 10.6311X2 - 3592.75X3+ 0.028335 - 0.159515 + 254.532X32 - 0.1263X1X2 + 0.452606X1X3 + 1.7638X2X3. Where : X1=Treatment time. X2=Temperature.X3= pH Average absolute error =10.8 % Correlation coefficient =0.98.

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
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.

تقيم كفاءة مزيج مثبط التاكل لمحاكاة مياه التبريد باستخدام القطب الاسطواني الدوار == Evaluation of Corrosion Inhibitors Blend Efficiency For Simulated Cooling Waters Using Rotating Cylinder Electrode

Author name: عبير عبد الخالق القصب
Supervisor name: قاسم جبار سليمان
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تم بحث كفائة مثبط التاكل لمزيج من نتريت الصوديوم / سداسي فوسفات الصوديوم على تاكل الفولاذ الكربوني في محاكاة انظمة مياه التبريد من خلال فقدان الوزن وتقنية الاستقطاب الكهروكيميائية. شملت الدراسة تاثير درجة الحرارة30، 45، 60 ?م، سرعة الدوران 200، 600، 1000 | The corrosion inhibition action of a blend of sodium nitrite/sodium hexametaphosphate (SN+SHMP) on corrosion of carbon steel in simulated cooling water systems (CWS) has been investigated by weight loss and electrochemical polarization technique. The effects of temperature 30, 45, and 60 oC, rotational velocity 200, 600, and 1000 rpm, and salts concentrations (0.005 N, 0.01 N, 0.03 N, 0.05 N) NaCl + 0.0736 N Na2SO4 on corrosion of carbon steel were studied in the absence and presence of mixed inhibiting blend (SN+SHMP). Also, the effects of inhibitors blend concentrations of 600 ppm, and 800 ppm (SN+SHMP), at temperatures of 30, and 60 oC, and rotational velocity of 200 and 1000 rpm, on corrosion rate of carbon steel were studied using Second - order Rotatable Design (Box - Wilson Design) to identify the significant effects and interaction in performing weight loss studies and corrosion potential approach. Electrochemical polarization measurements were used to study the behavior of carbon steel in different salt concentrations of (CWS) with pH of 7.5 in absence and presence of the inhibiting blend. The results showed that increasing the temperature, rotational velocity, and NaCl salts concentration leads to an increase in the corrosion rate for both uninhibited and inhibited solutions. The regression model (Box - Wilson Design) that has been developed using experimental data was used to verify that the interaction term of temperature with inhibitors blend and the square term of inhibitors blend are significant for corrosion rate in 0.05 N NaCl solution while the main variables are not pronounced. Also, it is found that the corrosion rate decreases with increases in inhibitor blend concentration up to 800 ppm in 0.05 N NaCl solution. Inhibitor blend concentration of 600 ppm is highly effective giving a high efficiency in 0.005, 0.01 and 0.03 N NaCl solutions of 98.5%, 97.7%, and 96% respectively. Electrochemical polarization studies show that increasing the inhibitors blend concentration (SN+SHMP) shifts the corrosion potential to more noble value (more positive), indicating the anodic nature of the inhibiting blend used.

اتزان الاطوار لاستخلاص الملوثات الفينولية من المياه الصناعية باستخدام تقنية الاغشية السائلة == Phase Equilibria For Extraction of Phenolic Pollutants From Industrial Wastewater Using Liquid Membrane Technique

Author name: انور جاسم محسن
Supervisor name: خالد فرهود جسب
General topic: Chemical Engineering
Specific topic: Chemical Processes
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: كلا من الصناعة الكيميائية (chemical industry) والبحث الاكاديمي (academia search) للمذيبات البديلة يجب ان تلبي متطلبات التكنولوجيا النظيفة (cleaner technology) حيث ان المذيبات الاكثر استخداما على نطاق واسع هي المتطايرة والضارة. في العمل الحالي، تم تحقيق | Both chemical industry and academia search for alternative solvents to meet the cleaner technology requirements since the most widely used solvents are volatile and harmful. In the present work, the technical feasibilities of room temperature ionic liquids (RTILs) as bulk liquid membranes (BLM) for phenol removal from Industrial Wastewater was investigated. Room temperature ionic liquids (RTILs) used as a membrane mainly due to their properties of low vapor pressure, low volatility and they are often stable. Four ionic liquids with high hydrophobicity were used : 1 - butyl - 3 - methylimidazolium hexafluorophosphate [Bmim] [PF6], 1 - butyl - 3 - methylimidazolium bis(trifluoromethylsulfonyl) imide [Bmim][NTf2], 1 - Ethyl - 3 - methyimidazolium bis(trifluoromethanesulfonyl) imide [Emim][NTf2] and 1 - hexyl - 3 - methylimidazolium hexafluorophosphate [Hmim][PF6], in which, phenol Extraction efficiency and stripping efficiency were studied. The effect of different types of anion and hydrophobicity of the ionic liquids on the phenol extraction and stripping efficiencies were investigated. Different operating parameters of feed phase pH, feed concentration, NaOH concentration were studied. In addition to the effect of single ionic liquid (SILs) and binary mixtures ionic liquid (BMILs) on the phenol extraction and stripping efficiencies were also studied. The study shows that highest phenol extraction and stripping efficiencies were [Bmim][NTf2], [Bmim][NTf2+PF6] and [Emim][NTf2], [Bmim+Emim][NTf2] respectively. Phase equilibria for the extraction of phenol from industrial wastewater using ionic liquid membranes was determined. The efficiency of ten new solvents as a selective ILs solvent in the extraction of phenol from wastewater was investigated. Data have been estimated experimentally for ten systems containing, phenol + water as a common component liquid and + ten IL solvents. The consistency and accuracy of the tie line data were evaluated using three correlation namely, Bachman, Hand, and Othmer and Tobias. The Plait Point for each ternary system was estimated. Among the ILs used to extract the phenol from wastewater, [Bmim][NTf2+PF6] shows the highest selectivity and distribution coefficient. The liquid - liquid equilibrium data have been predicated using electrolyte non - random - two - liquid (e - NRTL) model and extended UNIversal - QUAsi - Chemical (e - UNIQUAC) model. The binary interaction parameters have been calculated using Maximum Likelihood Principle technique. The experimental data fitted by the e - NRTL model is more accurate than the e - UNIQUAC model.

انتاج ايثايل ثلاثي بينوتايل ايثر من ثلاثي بيوتايل الكحول وايثايل الكحول باستخدام البيتا زيولايت المصنع من قشور الرز العراقي بواسطة التقطير التفاعلي == Production of Ethyl Tert - Butyl Ether From Tert - Butyl Alcohol And Ethyl Alcohol Catalyzed By ? - Zeolite Synthesis From Iraqi Rice Husk In Reactive Distillation

Author name: مؤيد خليل ابراهيم
Supervisor name: ودود طاهر محمد | عمار صالح عباس
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: تم انتاج مادة اثل ثلاثي بيوتايل ايثر من تفاعل ثلاثي البيوتانول والايثانول باستخدام تقنية التقطير التفاعلي وبوجود العامل المساعد بيتا زيولات المحضر محليا من قشور الارز العراقي كعامل مساعد.ثلاثة انواع من العامل المساعد تم تحضيرھا من قشور الرز العراقي باع | This work was conducted to study the production of ethyl tert - butyl ether from tert - butanol and ethanol by using reactive distillation technique in the presence of locally prepared ? - zeolite catalyst from Iraqi rice husk Three types of catalyst have been prepared from Iraqi rice husk as silica source and used in this work with which are ? - zeolite with three different Si/Al ratios (10,20 and 30) for comparing with commercial ? - zeolite which purchased from China to compare its characterization and activity in the production of ethyl tert - butyl ether from tert - butanol and ethanol.Kinetic of reaction of tert - butanol and ethanol to produce ethyl tert - butyl ether was studied separately by using batch reactor. The experiments were carried out under operating conditions of; temperature of (323,333 and 343k), four catalyst types and feed mole ratio ethanol/tert - butanol varied from (1.23 - 1.96) using excess ethanol, the rate equation at 323 k for ethyl tert - butyl ether was found as shown The Arrehnius equations of constants of reactions rate were found as shown : k1 = exp (22.769 - 9912.5 /T)? k2 =exp (37.952 - 11335 /T) kw = exp ( - 40.03 + 9644 /T) The main study includes the continuous packed reactive distillation column to produce ethyl tert - buty ether. The tert - butanol and ethanol reaction was carried out by continuous packed reactive distillation column using the three types of the prepared ? - zeolites and commercial ? - zeolite at atmospheric pressure, The operating variables studied the tert - butanol feed varied from (1 - 7) ml/min., recycle ratio varied from (1 - 7) and weight of catalyst used was varied from (10 - 40) g.The analysis of samples produced from reaction was carried out using gas chromatography GC showed that the tert - butanol conversion was 100% for all types of ? - zeolite with best yield 88% toward ethyl tert - butyl ether by using prepared ? - zeolite with Si/Al of 10, tert - butanol feed flow rate 3 ml/min., weight of catalyst 20g, recycle ratio 3. The result showed that the yield of ethyl tert - butyl ether was increasing from 64% to 88% when the operating conditions varied from lower to upper limit using prepared ? - zeolite with Si/Al of 10. Also, the results showed that, the prepared ? - zeolite with Si/Al of 10 gives better yield than commercial one.

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
Degree: Higher Diploma
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.

تصنيع وتشخيص الزيولايت النانوي المتبلور نوع ZSM - 5 والزيولايت المركب نوع ZSM - 5 / MCM - 41 لانتاج الوقود الحيوي == Synthesis And Characterization of Nanocrystalline ZSM - 5 And ZSM - 5 / MCM - 41 Composite Zeolite For Biodiesel Production

Author name: اسراء عبد الجبار صالح النعمة
Supervisor name: نجوى صابر مجيد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: الزيولايت النانوي - المتبلور بنوعين تم تصنيعهما ووصف خصائصيهما، النوع الاول يحتوي على ويحتوي على ZSM - 5/MCM - والاخر من نوع المركب 41 ZSM - مسام مايكروية ويسمى 5 05 نانومتر(. - نوعين من المسام ,المايكروية )اقل من 2 نانو متر( ومسام متوسطة ) 2 اجريت عم | Nanocrystalline ZSM - 5 zeolite and micro - mesoporous ZSM - 5/MCM - 41 composite zeolite were synthesized by hydrothermal treatment - conventional method. For ZSM - 5 two compositions were under investigation with different silica to alumina ratio of 86 and 68. Study of principal variables affecting the characterisics of synthesized zeolites were investigated in both aspects concerning chemical and process variables. Micro - mesoporous ZSM - 5/MCM - 41 composite zeolite were synthesized using alkaline treatment method and two step crystallization.Loading of synthesized zeolites with transition metals copper, cobalt, and ceria were conducted by impregnation.All zeolites products were characterized by X - ray diffraction (XRD), Atomic force microscopy (AFM), Fourier Transform infrared (FTIR), Brunauer - Emmet - Teller (N2 adsorption - desorption isotherm), Scanning electron microscopy (SEM), Transmission electron microscopy (TEM), X - ray fluorescence (XRF), and Thermogravemetric analysis/differential scanning calorimetry (TGA/DSC).XRD - patterns for ZSM - 5 showed, at different temperature ranging from (150 - 180 oC) and time of crystallization from 48 - 96h, that ZSM - 5 phase is the only obtained in almost all samples and the peaks at angle 2?= 7 ? 9o and 2?= 22.5 - 24.4o are typical. XRD - patterns for ZSM - 5/MCM - 41 identified by the 3 peaks in 2? < 10o and still having the peaks of ZSM - 5.AFM reports for both zeolites, ZSM - 5 and ZSM - 5/MCM - 41 indicated that a nano - level size of about 50 nm has been got. FTIR results showed that for ZSM - 5, the peaks near bands 3400, 1080, 800, 550, 450 cm - 1 have been clearly obtained. For ZSM - 5/MCM - 41 showedthe shifting of band at 1100 cm - 1 accompanied with a decrease of intensity in bands near 440 - 450 cm - 1.BET surface area results for ZSM - 5 samples showed a value of 320 - 380 m2/g and pore volume of 0.2 cm3/g. BET surface area for ZSM - 5/MCM - 41 showed an average value of 612 m2/g and pore volume of 0.5421 cm3/g.TEM images revealed that the loading of transition metals of copper and cobalt on both types of zeolite catalysts are distributed well on the surface of zeolite and on nano - level size.Biodiesel production, using prepared catalysts were conducted by esterification and transesterification by oleic acid and sunflower oil respectively with ethanol and methanol.Batch heterogeneous esterification process gave medium conversion of 69%. Semi - batch heterogeneous esterification gave better conversion of about 85%. The effect of both catalysts (Cu - ZSM - 5 and Co - Cu - ZSM - 5/MCM - 41) were similar and gave increase in conversion between 11 - 13%.Transesterification heterogeneous batch process using base - catalyzed (Ce - Na - ZSM - 5) and acid catalyzed heterogeneous transesterification (HZSM - 5), using sunflower oil and methanol showed a yield of 26% and 33% respectively relative to oil.

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
Degree: Higher Diploma
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.

دراسة تاثير النانو سليكا المحضرة من رمال السيليكا العراقية على بعض الخواص الميكانيكية لمتراكبات الكونكريت == Study The Effect of Nano - Silica Prepared From Iraqi Silica Sand On Some Mechanical Properties of Concrete Composites

Author name: علي داود سلمان
Supervisor name: نجاة جمعة صالح
General topic: Chemical Engineering
Specific topic: Chemical Processes
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: ان الهدف من هذا البحث هو تحضير دقائق السليكا النانوية من رمال السليكا العراقية من منجم ارضمة غرب العراق باستخدام طريقة الطحن المتعدد في (جهاز الطحن بالكرات)،حيث تم تشخيص دقائق السليكا بواسطة اجهزة التشخيص التالية SEM, AFM, PSA,FT - IR, XRD, XRF, BET,TEM. | The purposes of this work are to prepare, characterize silica nanoparticles for a first time from Ardma location at Anbar province in western Iraq by combination of top down approach using ultrafine grinding (Ball milling) and drying processes, evaluate the effect of nano - silica sand (NSS) addition on mechanical properties (compressive and splitting tensile strengths) of mortar mixture, and optimization of the operating variables (NS particle size and percentage of (NS) by using [WinQSB] and [STATISTICA] software technique to find the optimum values. (XRF) test shows enrichment of SiO2 after leaching with sulfuric acid. The prepared (NS) is characterized by SEM, AFM, PSA, FT - IR, XRD, XRF, BET and TEM. According to Particle Size Analyzers (PSA) silica sand has successfully been reduced to particle size of 50 nm after (30) hours of milling. The (AFM) test reveal two different groups of samples were analyzed, the range of first group was (60 - 120) nm after 40 hours of milling, the range of second group was (90 - 170)nm after 50 hours of milling. X - ray diffraction of silica sand before and after milling process shows that surface , structural changes duo to amorphization phenomenon result from an intensive mechanical treatment by (Ball milling) of silica sand. This result supports the incorporating (NS) into cement mortar. The (BET) analysis shows that the (NS) has different surface areas according to particle size. The (TEM) and (SEM) images of NS show that various shapes of the(NS) particles including irregular, spherical, and highly agglomerated in shape due to Van der Walls force on the particles surface. Three different ranges of particle sizes of (NS) have been used; (30 - 100)nm,(60 - 120)nm and(90 - 170)nm with three percentages of each (2% ,6% and 10% per weight of cement) and a w/c of 0.48. The SEM images of mortar mixture at the age of 28 days show existence of many Ca(OH)2 crystals needles over - shadowed and cover a large area with porous structure, while after adding (NSS) the Ca(OH)2needles are invisible and compact structure with the absence of the un - hydrated crystals which explains the superior strengths results. NSS contributes to enhancement of cement mortar through yielding denser, more compact and uniform mixtures. The optimization results of mechanical properties proved that an improvement in compressive strength of 29.889% at optimum conditions (adding 6% of 50nm particle size) in 28 days age, while for tensile strength was 22.863% at optimum conditions (adding 8% of 50nm particle size) in 28 days age. NSS obtained by ball milling of silica sand can be produced in large quantities at low prices, by sustainable method so that mass application in concrete is within reach According to my knowledge there is no previous work focusing on preparing of silica nanoparticles from Iraqi silica sand, and using it to improve mechanical properties of cement mortar by using optimization technique.

دراسة الهيدروديناميكية والحركية في مفاعل الطبقة الفوارة لوحدة النفط الثقيل == Hydrodynamic And Kinetic Study In An Ebullated - Bed Reactor For The Heavy Oil (H - Oil Unit)

Author name: هالة حسين حسن ابو نايلة
Supervisor name: محمد فاضل عبد | شاكر محمود احمد
General topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: ان النمو المضطرد في انتاج النفوط الثقيلة والطلب المتزايد على المقطرات الوسطيه اعطى اهمية قصوى لعمليات التكسير في المصافي النفطية، وتعتبر طريقة (H - Oil) باستخدام مفاعلات الطبقة الفوارة واحدة من اهم عمليات التكسير المحفز والتي تهدف الى تكسير النفوط الثقيل | The present work was devoted to study the hydrodynamic characteristics of a lab - scale cold - flow ebullated bed three phase column. It was also to investigate the kinetic behavior of an industrial - scale ebullated bed reactor, licensed by Axens Co., installed and operated in Lukoil refinery at Bourgas - Bulgaria.For the design of experiments in the lab - scale cold - flow column, factorial method was introduced to study the influence of the operating variables (i.e., gas and liquid superficial velocities and the liquid internal reflux ratio) on the objective functions (i.e., individual holdups and bubble characteristics).Pressure gradient method was used to estimate the individual holdups and bed porosity along the column, while photographic method was utilized to obtain images of the moving gas bubble which analyzed using Ai Adobe Illustrator CC (64 Bit) software to determine the geometric characteristics of bubbles.The results showed that liquid internal reflux ratio, which characterized the ebullated bed three phase bubble column, has a predominant effect on the individual holdups and bubble sizes.The operating and geometric variables of the lab - scale cold - flow ebullated bed were carefully selected to simulate the hydrodynamic characteristic of the industrial unit through matching five dimensionless groups (M - group, E?tv?s number, Reynolds number, density ratio and velocity ratio) of the cold - flowlab - scale and industrial systems.The percentage average deviations between each two particular groups of the two systems were (14.7%, 25%, 13.14%, 15.2%, and 20%), respectively. Although this did not result in a perfect match, considering the uncertainty in the industrial units exact operating properties, the match was considered to be sufficiently close.A five - lump kinetic model was selected, to describe the catalytic hydrocracking of heavy oil, to formulate the reaction rate equations of vacuum residue, vacuum gas oil, middle distillate, naphtha, and gases. These equations were inserted into the individual mass balance equation of each lump and then utilized in a program of MATLAB based on the nonlinear least square method to estimate the kinetic parameters (rate constants and activation energies of the proposed reaction pathways), to investigate the effect of the operating variables (e.g., operating temperature, WHSV, and reaction time ) on the kinetic parameters and performance of the industrial ebullated bed reactor. It was found that, - The intra - pellet (internal) diffusion was the rate - limiting step in the H - Oil reaction system. - The effectiveness factor decreases with increasing reaction temperature and WHSV. - The outcomes of the mathematical model confirmed the reaction orders of hydrocracking of vacuum residue and catalyst deactivation to be 2.1 and 0.18, respectively. - Activation and deactivation energies resulted to be quite similar of 48.87 and 50.68 kcal/mole, respectively, meaning that there is no strong effect of the deactivation process over the global hydrocracking reaction. - The hydrocracking of vacuum residue has a higher selectivity toward VGO production than toward other lumps in the following order : VGO < Middle Distillate < Naphtha <Gases. - WHSV has a negative impact on yield fractions of the industrial ebullated bed reactor while the images were different with the operating temperature. The formulated model was validated by comparing its outcomes with the findings of other related model (e.g Sa´nchez and Ancheyta, 2007) from literature. The results of comparison confirmed the reliability of the present model.Key words : Hydrodynamic, Kinetic Parameters, Heavy Oil, Ebullated Bed, Reactor.

تاكل الفولاذ الكاربوني تحت ظروف الخلط في وسط ثنائي الطور لمحلول ملحي مع زيت الغاز وثنائي اوكسيد الكاربون والسيطرة علية بالحماية الكاثودية == Corrosion of Carbon Steel In Stirred Two Phase Media of Brine - Gas Oil And Brine - CO2 And Prevention By Cathodic Protection

Author name: ساهر محمد عزيز
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
University: Al-Nahrain University
Language: English
University location: Baghdad
First pages:
Abstract: Corrosion tests of carbon steel (CS) in single and two phase media of two immiscible liquids (CaCO3 solution - gasoil mixture) and liquid - gas (CaCO3 solution - CO2 gas) under different operating conditions of temperature, agitation velocity, phase fractions, gas flow rate, and immersion time were carried out using weight loss method and electrochemical polarization technique. Flat blade disc turbine mixer was used to simulate the two phase flow conditions.The ranges of operating parameters in two immiscible phase tests were agitation velocities of (0 - 1200 rpm), temperature of (25 - 45 oC), (1 - 10 vol %) gas oil. The effect of presence of acids such as HCl and H2SO4 on corrosion rate was also investigated under different conditions.Corrosion rate (iL) measurements in CO2 saturated solution were also attained in different operating conditions of temperatures(25 - 45 oC), agitation velocity (0 - 800 rpm), salts concentrations (2.5 × 10 - 3 to 9.9 × 10 - 3M), CO2 flow rate (0.142 to1.132 m3/h ), and immersion time by determining the limiting current density.The pH values, oxygen solubility, and electrical conductivity of tested solutions were measured under all to interpret the obtained result.The results revealed that increasing agitation velocity and temperature leads to an increase of the corrosion rate in single phase brine solution. The corrosion rate in brine - gasoil mixture is irregularly varied with concentration of gasoil and agitation velocity. The limiting current density in single phase CaCO3 increases with the increase in agitation velocity, concentration of brine, and temperature. The corrosion rate in two phase brine - CO2 mixture decreases with the increase of agitation velocity flow rate of CO2, temperature, and immersion time. The corrosion potential of Carbon steel under various conditions were determined and discussed.Cathodic protection was used to protect carbon steel in brine - CO2 mixture by using zinc as sacrificial anode under different operating conditions of flow rate of CO2, agitation velocity, and temperature. Good corrosion protection efficiency was attained.

العوامل المؤثرة على ظاهرة تقليل الاعاقة المصاحبة لجريان السوائل بواسطة المضافات البوليمرية والمواد الخافظة للشد السطحي == Effect of Operating Variables On Drag Reduction Phenomenon By Polymers And Surfactants Additives

Author name: ليث مجيد عبود
Supervisor name: issam kamil salih
General topic: Chemical Engineering
Specific topic: Industrial Processes
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تناول البحث دراسة وتطبيق ظاهرة تقليل الاعاقة لاطالة مسافة تصريف السوائل الساقطة بشكل حر من انبوب افقي. حيث تمت دراسة تاثير ارتفاع ونوع السائل , نوع وتركيز البوليمر , قطر الانبوب وخشونة سطحه, واحدى المواد ذات الفعالية السطحية.تم اجراء الاختبارات العملية | Drag reduction phenomenon has been studied and applied to extend the discharge distance of kerosene, gas oil and tap water falling freely from horizontal tube. The effect of liquid head, type of solvent, polymer characteristics and concentration, pipe diameter and roughness and addition of surfactant were investigated.Experimental tests were performed using apparatus consisting of a reservoir connected to a horizontal tube from which the flux was allowed to fall freely under different heads. The distance traveled horizontally was measured and used to estimate the friction factor (ƒ) and the percentage drag reduction (%DR). The tests were carried out under liquid heads of 140, 165, 190, 215, 240 cm to ensure turbulent flow circumstances, i.e. Re ? 3000.Three types of polymers were tested, viz., polyisobutylene (PIB), xanthan gum (XG) and guar gum (GGM). The activities of these polymers for drag reduction were evaluated at concentrations of 10 - 200 ppm for PIB and 50 - 400 ppm for XG and GGM using three solvents, viz., kerosene, gas oil and tap water. Glass tubes of 3,7,10 and 11mm diameters in addition to carbon steel and stainless steel pipes of 10mm diameter were used to investigate the effect of pipe diameter and roughness.The interactions between polymer and surfactant were investigated using sodium luaryl sulfate (SLS) so that experimental tests were performed with PIB in the absence and presence of (SLS) at different concentrations. The discharge distance and %DR is generally increased with increasing liquid head and additive concentration. However %DR is sometimes reached to a maximum value at a specific concentration termed " critical concentration" beyond which %DR is fallen, the %DR observed with 100ppm of PIB is 44.3% at head equal 140 cm and 56% at head equal 240 cm from stainless steel tube. Moreover, %DR is progressively increased with increasing Reynolds number (Re) at any specific concentration, %DR achieved due to the addition 50ppm of PIB is 20.8% at Re equal 17236 and 45.9% at Re equal 26056 from stainless steel tube.Polyisobutylene has effectively reduced drag with kerosene and gas oil. Its activity seems to be higher with gas oil compared to that with kerosene. The maximum %DR achieved due to the addition 100 ppm of PIB in gas oil and kerosene are 63% & 56% respectively from Stainless steel tube. The activity of SLS for drag reduction with kerosene is evidently lower than that of PIB, and the difference between %DR observed is reduced with increasing concentration. Efficiency of PIB is considerably decreased by adding SLS so that the maximum %DR achieved with their mixture is 40.1%.The polymers XG and GGM are effectively reduced drag when added to tap water. Their activities at any specific operating conditions are decreased according to the sequence of XG ? GGM. The maximum %DR observed with them at 300 ppm are 77% and 48.8% respectively. The values of (%DR) measured with all tested liquids seem consistent with Blasius equation and they are progressively shifted to the direction of Virk asymptote with increasing of polymer concentration. The percent drag reduction is well correlated with Reynolds numbers, (L/D) and polymer concentration according to the relation of the form %DR= a (Re)b (C)d (L/D)k, where a, b, d and k are constants, so that a specific empirical correlation is observed for each polymer.

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
Degree: Higher Diploma
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%).

تثبيط التكلسات في انظمة التناضح العكسي باستخدام مواد كيمياوية == Scale Inhibition In Reverse Osmosis Systems Using Chemical Materials

Author name: زهراء احمد عبد الامير
Supervisor name: نجوى صابر مجيد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تم في ھذا البحث دراسة تثبيط تكون تكلسات كاربونات الكالسيوم على سطح غشاء نظام تناضح عكسي باستخدام نوعين من مثبطات تكون التكلسات وھما كلوريد الزنك ومادة بوليمرية بتراكيز منخفضة ودراسة تاثير تغيير معدل جريان المحلول الداخل, حامضية المحلول الداخل, تركيز ال | The present study deals with the calcium carbonate (CaCO3) inhibition on the membrane surface of the reverse osmosis (RO) desalination system by using two types of scale inhibitors which are Zinc Chloride (ZnCl2) and Polyamino Polyether Methylene Phosphonate (PAPEMP) in low concentrations and study the effect of changing the feed solution flowrate, PH of the feed solution, concentration of the inhibition material and the type of the inhibitor used on the inhibition process. In this study a range of 10 - 25 l/h of feed solution flowrate was used, the concentration of CaCl2 was 610 mg/l, the concentration of NaHCO3 was 511 mg/l, the concentration of MgSO4 was 49 mg/l, the feed pH was in the range of 6 - 10, the operating pressure kept constant at 3 bars and the temperature washeld constant at room temperature (about 40 °C) through all experiments. The concentration of the feed solution was constant, but the concentration of the inhibitors was changed using 2, 4 and 8 mg/l of Zinc Chloride then using 8 and 15 mg/l of Polyamino Polyether Methylene Phosphonate The results showed that : Permeate rate increases as the feed flowrate increases while it decreases with time.Total dissolved solids decreases as the feed flowrate increases while it increases with time.Recovery rate decreases as the feed flowrate increases and it also decreases with time.Permeate rate, recovery rate and the total dissolved solids decreases as the inlet solution pH increases.Permeate rate and recovery rate increases while the total dissolved solids decreases when Zinc chloride or Polyamino Polyether Methylene Phosphonate was used.Permeate rate and recovery rate increases when Polyamino Polyether Methylene Phosphonate inhibitor was used more than the increment of them when Zinc chloride inhibitor was used.Total dissolved solids decreases when Zinc chloride inhibitor was used more than the diminution of them when Polyamino Polyether Methylene Phosphonate inhibitor was used.
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