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الخواص الحرارية والميكانيكية للخرسانة الخالية من الرمل والمعززة بالالياف == Thermal And Mechanical Properties of Fiber Reinforced No - Fines Concrete

اسم المؤلف: باسم هوير امانة
اسم المشرف: باسل صلاح مهدي | اسامة عبد الامير عيدان
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة الانشائية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: تعاني المنشات الخرسانية في العراق من مشاكل كثيرة، ومن ھذه الشاكل التي تتعلق في الاملاح الكبريتية في الرمل في مطابقتھا للمواصفات القياسية. واحد من ھذه الحلول ھو استخدام الخرسانة الخالية من الرمل التي تتكون من سمنت وحصى فقط بدون اي رمل. ھذه الخرسانة تعطينا | Concrete constrictions in Iraq suffer from many problems, some of those are concerning with the deficiency of sand satisfying the sulfate requirements of the standard specifications. One of the solution is to use no - fines concrete that compose from ceme

بناء قواعد بيانات مكانية للخواص الجيوتكنيكية لمنطقة محافظة ذي قار باستخدام التقنيات الرقمية الحديثة == Building Geodatabase For Geotechnical Properties of Thi - Qar Governorate Area Using Modern Digital Techniques

اسم المؤلف: قاسم عبد الحسين عبد العباس
اسم المشرف: عبد الرزاق طارش زبون | فلاح حسن رحيل
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: هندسة الجيوماتيك
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: تهدف هذه الدراسة الى اعداد خرائط رقمية جيوتكنيكية لمحافظة ذي قارجنوب العراق باستخدام تقنيات نظم المعلومات الجغرافية GIS ونظام تحديد المواقع العالمي GPS اللذين يتحدان مع تقنيات التحسس النائي RS وبرمجيات متخصصة تم استخدامها لغرض اظهار خواص التربة في عموم ال | The digital geotechnical maps are widespread nowadays due to the existence of Geographical Information Systems (GIS), Global Positioning Systems (GPS), which both integrated with remote sensing (RS) technique and other special programs that are used for i

تحليل وسلوك الانحناء لعتبات خرسانة المساحيق الفعالة ذات المقطع (T) == Analysis And Behavior of RPC T - Beams In Flexure

اسم المؤلف: حيدر ميثم حكمت
اسم المشرف: Hisham Mohammed Al | Hassani | Bassman R. Mohammad
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة الانشائية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: خرسانة المساحيق الفعالة او عادة ما تسمى الخرسانة فائقة الاداء واحدة من احدث التطورات والاكثر اهمية في تكنلوجيا الخرسانة, لقد اوليت اهتمام كبير في السنوات الاخيرة في العالم نظرا لخصائصها الميكانيكية الفائقة مثل : المقاومة العالية, المطيلية العالية, المتانة | developments in concrete technology. It has received great attention in recent years in the world due to its superior mechanical properties such as; high strength, high ductility, high durability, limited shrinkage consequences, high resistance to corrosi

خواص الخشونة لنهر دجلة لمنطقة كوت - نعمانية وتاثيرها على محطة رصد النعمانية == Roughness Characteristics of The Kut - Nu'Maniyah Reach of The Tigris River And Its Effect on Nu'Maniyah Gaging Station

اسم المؤلف: علي عبد الحسين عبد عبد الصاحب
اسم المشرف: عبد الاله يونس محمد
الموضوع العام: الهندسة المدنية
السنة: 2014
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: Estimation of Manning’s roughness coefficient is of vital importance in hydraulic studies of open channel flows. Manning's n is necessary for calculation of discharges, water levels, backwater curves and for rating curve extensions.The roughness characte

تطوير نظام لادارة الهدر الانشائي خلال مرحلة التنفيذ : محافظة كربلاء كحالة دراسية == A Construction Waste Management System Developed For The Execution Phase - Karbala Projects As A Case Study

اسم المؤلف: علي حسن هادي ال عايم
اسم المشرف: زياد سليمان محمد خالد | باسل صلاح الشذر
الموضوع العام: الهندسة المدنية
السنة: 2014
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: ينجم هدر المواد نتيجة اخفاق في استخدام المعدات او المواد او العمالة او راس المال، مما يؤدي الى استهلاك مواد اكثر مما تتطلبه عملية انتاج المنتج. وقد اصبح الهدر في التشييد تحديا على الصعيدين البيئي والاقتصادي. اذ تشكل الانقاض الناجمة عن التشييد - على الم | Material waste is understood as any inefficiency that results in the use of equipment, materials, labour, or capital causing larger quantities than those considered as necessary in the production of a product. Construction waste became a challenge to the

نمذجة وتشكيل خط الاساس لشبكة الانظمة العالمية للتوابع الملاحية الجيوديسية == Modeling And Configuration of Baseline For Global Navigation Satellite Systems Geodetic Network

اسم المؤلف: زهراء عز الدين حسين
اسم المشرف: Oday Al Hamadani
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: هندسة المساحة
الدرجة: ماجستير
الجامعة: جامعة بغداد
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: This thesis aims to find an optimal configuration for GNSS baselines in terms of the number and distribution baselines to improve quality criteria of GNSS networks. First order design problem (FOD) was applied in this research to optimize GNSS network bas

تصنيف بيانات المسح الليزري من نوع full - waveform لاغراض تحسين النموذج الرقمي التضاريسي الارضي (DTM) == Classification of Full - Waveform Aerial Laser Scanning Data To Improve The Digital Terrain Model (DTM)

اسم المؤلف: نور سمير صادق الخالصي
اسم المشرف: Ayad Ashour
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: هندسة المساحة
الدرجة: ماجستير
الجامعة: جامعة بغداد
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: المسح الضوئي الليزري يسمى ايضا LIDAR هي تقنية الاستشعار النشطة عن بعد التي يتم استخدامها على نطاق واسع للحصول على بنية هندسية من سطح الارض باستخدام ضوء الليزر. فانه يمكن الحصول على معلومات حول تضاريس سطح الارض والغطاء النباتي و/ او ارتفاع قاع البحر في الم | Laser scanning (also referred to as LIDAR) is an active remote sensing technique that is widely used for obtaining the geometric structure of the Earth’s surface using laser light. It can obtain information about the topography of the land surface, the ve

معالجة المياه الجوفيه المحضرة والملوثة بالرصاص والفينول باستخدام حاجز نفاذ فعال == Treatment of Lead And Phenol - Contaminated Simulated Groundwater Using Permeable Reactive Barrier

اسم المؤلف: زياد طارق عبد علي
اسم المشرف: Ayad A.H. Faisal
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة البيئية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: تهدف الدراسة الحالية الى معرفة امكانية استخدام الحماه كماده مازة عضوية اقتصادية, متوفرة وكفوءة كحاجز تفاعلي نفاذ والذي يعتبر احد التقنيات الواعدة المبتكرة في المعالجة الموقعية للمياه الجوفية لازالة الرصاص والفينول او كليهما من الطبقة الملوثة ذات الاعماق ا | The present study investigates the possibility of using granular dead biomass in the permeable reactive barrier (PRB) technology. This technology is one of the promising innovative in situ groundwater remediation methods used in this study for the removal

ازالة النحاس، الرصاص والخارصين من الترب الملوثة المماثلة بالغسل باستخدام محلول EDTA وحامض الستريك == Removal of Copper, Lead And Zinc From Simulated Contaminated Soils By Leaching Using EDTA And Citric Acid

اسم المؤلف: زهراء حسن مطر
اسم المشرف: Hatem Asal Gzar
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة البيئية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: قدمت الدراسة الحالية نتائج التجارب المختبرية التي اجريت لتقييم كفاءة نوعين من محاليل الازالة في عملية غسل التربة ودراسة تاثير بعض المتغيرات على كفاءة الازالة, تتلخص هذه المتغيرات بما يلي : (1) الدالة الحامضية (2) تركيز محلول الازالة (3) زمن الاستخلاص.اجر | Soil contamination by heavy metals is increasing day by day. Now a day’s metal contamination is a persistent problem at many contaminated sites all over the world. This thesis presents the results of an experimental investigation undertaken to evaluate th

تحويل المواد السيليلوزية مختارة الى وقود حيوي == Converting Selected Cellulosic Waste Materials Into Biofuels

اسم المؤلف: مروان حسين عبد الامير
اسم المشرف: جذوة عبد الكريم
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة البيئية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: يعد الايثانول الحيوي وقود سائل يمكن انتاجه منزليا من مصادر نباتية قابلة للتجديد يطلق عليها الكتلة الحيوية. كما ان استعمال الايثانول يساهم بشكل فعال في تقليل السموم المنبعثة الى الهواء من قطاع النقل واخيرا يعد الايثانول البديل الامثل عن مصادر الطاقة القابل | The negative impacts of fossil fuel consumption on the environment, rising prices for fossil fuels and progressive demand for energy have renewed the interest of society in searching for alternative renewable and sustainable forms of energy. Hence, the al

الامتزاز التنافسي للعناصر الثقيلة بواسطة الطحالب ومادة (Fe3O4) النانوية == Competitive Adsorption of Heavy Metals onto Algae And (Fe3O4) Nanomaterial

اسم المؤلف: حسنين سعد عبد الزهرة الحارس
اسم المشرف: شهلاء اسماعيل ابراهيم
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة البيئية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: A competitive biosorption of Cu2+, Ni2+, Zn2+ and Cd2+ ions from a synthetic wastewater onto dead algal biomass and nanomaterial was studied.(Fe3O4) nanoparticles obtained from US Research Nanomaterials, Inc., Houston, TX 77084, (USA), was used as nanoso

تخمين نزول الانضمام في الترب غير المشبعة من الفحوص المختبرية == Prediction of Consolidatio Settlement of Unsaturated Soil From Laboratery Tests

اسم المؤلف: مصطفى ياسين نعمة
اسم المشرف: عبد الكريم عصمت زينل | علاء ناصر الجوراني
الموضوع العام: الهندسة المدنية
السنة: 2014
الموضوع الدقيق: الهندسة المدنية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: The consolidation settlement is one of the important parameters that need to be calculated during the design of shallow foundation.This importance becomes higher as the structure to be constructed is sensitive to settlement especially for long term settl

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

اسم المؤلف: سهى اكرم محمد
اسم المشرف: قاسم جبار سليمان | سيسيليا خوشابا
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.

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

اسم المؤلف: نضال احمد شاكر
اسم المشرف: شذى احمد سامح | شروق طالب الحميري
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.

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

اسم المؤلف: مهند ابراهيم فرحان
اسم المشرف: ثامر جاسم محمد
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: العمليات الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: مصطفى جواد نعمة
اسم المشرف: غزوان احمد محمد | عباس خلف محمد
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: غيداء ضياء الدين نجيب
اسم المشرف: صفاء الدين عبد الله النعيمي | فرح طالب السوادني
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: العمليات الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: عقيل شيخة عرفات
اسم المشرف: خالد مخلف موسى
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: صباح محمد حسن الجبوري
اسم المشرف: رافع جمال يعقوب
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: صلاح الدين
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: سمر خالد الجنابي
اسم المشرف: نيران خليل ابراهيم
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: ياسمين منذر جاعد
اسم المشرف: ودود طاهر محمد
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: جعفر جبار مدلول
اسم المشرف: احمد فائق العلوي
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: سيف عبد الحق عبد الستار
اسم المشرف: نجاة جمعة صالح
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الدرجة: دبلوم عالي
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: خالد حامد رشيد عبد الخالق
اسم المشرف: ابرائيل سركيس يارو
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.
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