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

اسم المؤلف: هبة صباح جعفر
اسم المشرف: علاء عبد الرزاق جاسم | جاسم محمد مهدي الاسدي
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: البصرة
الصفحات الاولى:

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.

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

اسم المؤلف: عبير عبد الخالق القصب
اسم المشرف: قاسم جبار سليمان
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: انور جاسم محسن
اسم المشرف: خالد فرهود جسب
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: العمليات الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: مؤيد خليل ابراهيم
اسم المشرف: ودود طاهر محمد | عمار صالح عباس
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: علي محسن غضبان
اسم المشرف: Safa A. Al | Naimi
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الدرجة: دبلوم عالي
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: يشتمل البحث على عمل نموذج رياضي لمفاعل النازلdowner) ) في وحدة التكسير المحفز بالعامل المساعد وان التفاعل يشمل اربع مكونات هي التغذية Gas oil)) والغازات الخفيفة (Light gases) والكازولين (Gasoline) والفحم (Coke) اوما يسمى ب Four lumps model لوصف حركة تفاعل | In this work, mathematical model for downer reactor have been developed, in which a four - lump model is used to characterize the feed and the products, where gas oil cracks to give lighter fractions and coke. The integrated reactor steady state model makes gross assumption about the hydrodynamics, using 4th. order Runga Kutta method. Polymath version 5.1 and Aspen version 7.3 programs are used to solve the simulation model. This model can predict the mixing temperature and pressure profiles at mixer (MxR) chamber; also shows the physical performance and productivity all over the downer height. An interactive excel worksheet is constructed and used as a powerful tool for solving the model equations and studying the effect of any change in operating variables on the unit performance. Also observed the simulated results by using two programs (Polymath and Aspen) and the difference between them especially in temperature , pressure and product yield profile plotted along the reactor length and shows that the results from Aspen are better than Polymath because the first is more advanced and accurate. The operation of downer reactor for catalytic cracking is associated with several important objectives such as feed rate and height, diameter of reactor and amount of catalyst rate as well as the production requirements, all of which need to be optimized simultaneously. In this study, a validated mathematical model was used to perform the single - objective optimization of the FCC system at the design stage. In the optimization study, four operating parameters were used as decision variables. These variables were chosen based onsystematic sensitivity analysis of the system which showed complex interplay of the decision variables over the system performance indicators. Elitist Polymath version 5.1 enhanced with Excel flow sheet 2007 were used to solve a number of objective function optimization problems. The objective functions used are maximization of the gasoline yield, and minimization of the catalyst flow rate. The optimal results obtained here provide physical insights that can help in the design stage of the downer reactor.

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

اسم المؤلف: وسام عدنان حيدر العبيدي
اسم المشرف: عدنان عبد الجبار عبد الرزاق السالم
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الدرجة: دبلوم عالي
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: علي داود سلمان
اسم المشرف: نجاة جمعة صالح
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: العمليات الكيمياوية
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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)

اسم المؤلف: هالة حسين حسن ابو نايلة
اسم المشرف: محمد فاضل عبد | شاكر محمود احمد
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الدرجة: ماجستير
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.