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تحضير وتطبيق الدقائق النانوية في ازالة قطرات النفط من المياه المصاحبة في الحقول النفطية == Synthesis and Application of Nanoparticles in Removal of Oil Droplets from Oilfield Produced Water

Author name: اية سعد جواد
Supervisor name: Ahmed Faiq Al-Alawy
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:

دراسة تاثير الموائع النانوية على قابلية بلل الصخور الكاربونية لتحسين استخراج النفط == Study the Influence of Nano Fluids on Carbonate Rocks Wettability for The Enhancement of Oil Recovery

Author name: رنا رسول جليل
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad

تحضير مادة الفحم الحيوي من نشارة الخشب لامتزاز الملوثات الصبغية من المياه == PREPARTION OF BIOCHAR FROM SAWDUST FOR THE ADSORPTION OF DYE POLLUTANTS

Author name: محمد عبد الرحمن حنون
Supervisor name: مثنى احمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad

ازالة الكبريت العميق من النفثا العراقية الثقيلة باستخدام انواع مختلفة من المحفزات النانو الزيوليت == Deep Desulfurization of Iraqi heavy naphtha Using Different Types of Nano Zeolites Based Catalysts

Author name: حسام موسى جمعه
Supervisor name: حسين قاسم حسين
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad

تصميم ودراسة عملية لهايدروسايكلون ذي مرحلة واحدة ومرحلتين لفصل الزيت - الماء == Design and Experimental study of single and double – stage hydrocyclones for oil – water separation

Author name: مريم ابراهيم جاسب
Supervisor name: رغد فريد قاسم
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad

ازالة الشمع من زيوت التزييت باستخدام مختلف المذيبات الانتقائية == Recovery of Wax From Lubricating Oil Distillate by Using Different Selective Solvents

Author name: صفاء رشيد ياسين
Supervisor name: عبد الحليم عبد الكريم محمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:

تقييم اداء بعض المواد الكيمياوية المثبطة لتاكل النحاس في الاوساط الحامضية == Evalation The Performance of Some Chemical Inhibitors on Corrosion Inhibition of Copper in Acid Media

Author name: انيس عبد الله كاظم الشمري
Supervisor name: ابرائيل سركيس يارو
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

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

معالجة الماء من حقول النفط باستخدام محاليل ايونية في منظومة التعويم بالهواء المذاب == Treatment of Oilfield Produced Water Using Ionic Liquids In A Dissolved Air Flotation System

Author name: اوس عباس فاضل
Supervisor name: سوسن عبد مسلم محمد | سعدي كاظم عبد الحسين
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: في العراق معدل تراكيز الزيوت والشحوم (OG) في الماء المنتج يجب الا يتجاوز 09 ملغم\لتر. ولذلك فانه يتطلب معالجة المياه المنتجة بغية تلبية الحد التنظيمي للتصريف مسبقا.تم جلب نماذج الماء المنتج الخام من شركة نفط الوسط ) Md.O.C ( من الحقول النفطية من شرق بغد | In Iraq the average Oil and Grease (OG) in water concentration in discharge produced water must not exceed 10ppm. Therefore treatment of produced water is required in order to meet the pre - disposal regulatory limit.Raw produced water samples were procured from the Middle oil company (Md.O.C) (from East of Baghdad fields).Jar tests experiments were used to give a first, rough estimation for coagulants dosage of Ferric chloride and aluminum sulfate and pH values that will be used in the batch Dissolved Air Flotation (DAF) experiments. Then, the effects of the three ionic liquids (ILs) types; 1 - hexyl - 3 - methylimidazolium tetra fluoroborate (ILE), 1 - hexyl - 3 - metylimidazolium hexafluorophosphate (ILF) and 1 - octyl - 3 - methylimidazolium tetra fluoroborate (ILG) on the performance of the batch DAF unit were evaluated.It was concluded that, the beast operating conditions of the batch DAF unit were at a saturation pressure of 5 bar, recycle ratio of 50% and ambient temperature of 30 - 35 ?C. Ferric chloride with a dosage of 10 ppm was chosen as the suitable coagulant due to its low sensitivity to pH change, and its high removal efficiency for oil and turbidity in about ten minutes. ILs were used at concentration of 50 ?l per one liter of treated produced water. It was used in two positions of the DAF system; the saturation vessel and the treatment tank. The OG removal efficiency using ILG as an efficient surfactant in saturation vessel was higher than that in the treatment tank and higher than other ILs (ILG>ILF>ILE). The highest demulsification rates were obtained through saturation pressure range (2 - 5) bar. It reached about 90% removal efficiency at a pressure of 5 bar, and it was obtained 85% at saturation pressure of 3 bar which reduces the operation costs. The treated water concentration at 3bar was 9.5 ppm which meets the Iraqi pre - disposal regulatory limit.The results of testing the three ILs (ILE, ILF and ILG) in the saturation vessel and the treatment tank were used to produce contour line for the OG removal efficiency. This was conducted in order to detect the performance of the three ILs The results of optical microscope which was used to study coalescence of oil droplets in water phase, lead to consider the ILG as an effective demulsifier for Iraqi oil field produced water It was noted that the use of ILs in saturation vessel allowed micro bubble generation at operating pressures lower than 3 bar with high - energy savings.

ازالة الكبريت بالامتزاز من النفثا الثقيلة العراقية بواسطة 13X زيولايت == Adsorption Desulfurization of Iraqi Heavy Naphtha Using 13X Zeolite

Author name: موفق محمد يحيى
Supervisor name: حسين قاسم حسين
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: اجري هذا العمل لدراسة تاثير الامتزاز الانتقائي في ازالة مركبات الكبريت من النفثا الثقيلة العراقية التي تم توريدها من مصفاة الدورة. انجزت عملية الامتزاز بواسطة 13 منخل جزيئي داخل العمود ذو الحشوة الثابتة. X 6?? - من ??5 LHSV وقد نفذ الامتزاز الانتقائي في | This work was conducted to study the effect of selective adsorption on removal of sulfur compounds from Iraqi heavy naphtha which was supplied from Al - Dura refinery. The adsorption was carried out by molecular sieve 13X in a fixed - bed column.The selective adsorption was run out at different operating conditions such as LHSV from 1.5 - 6.0 h P - 1 P , molecular sieve bed weight from 15 - 30 g , sulfur inlet concentration of feedstock from 600 - 1650 ppm, and adsorption temperature at 25 PoPC and 40 PoPC.The breakthrough time, breakpoint and saturation state ( bed replace point ) were determined for different operating conditions in addition to the ratio of accumulated effluent weight per bed weight. Also , regeneration possibility of 13X spent catalyst was studied by using oxidative technique at different temperatures and air flow rates.The results show that increasing in LHSV and inlet concentration makes the breakthrough curves more steeper , also the breakthrough time and breakpoint decreases. Increasing the bed weight will increase both the breakthrough time and breakpoint.The best operating conditions for removing sulfur compounds were LHSV 3.0 h - 1 , bed weight of molecular sieve about 20 g and 25oC temperature , where the sulfur content in a heavy naphtha was reduced from nearly 600 ppm to less than 1 ppm (by weight).Regeneration step was thermally took place by hot air flow in a range of 16.66 - 25 liter / min and temperature range from 200 - 350 oC , the best desorption conditions for (85.8%) weight percent removal were at 16.66 liter / min air flow and 350 oC.

دراسة الحركية ونمذجة تفاعل استرة حامض الاوليك باستخدام NaY زيولايت المحضر == Kinetic Study And Modeling of Olic Acid Esterification Over Prepared Nay Zeolite

Author name: رويدة نزيه عباس
Supervisor name: عمار صالح عباس
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: تم تحضير زيولايت من نوع استرة حامض الاوليك. اجريت فحوصات الاشعة السينية ونسبة الصوديوم ونسبة السيليكا الى الالومينا والمساحة السطحية والحجم المسامي للعامل المساعد المحضر.اظهرت الفحوصات التوافق بين العامل المساعد المحضر مع التركيب العام للزيولايت القياسي. | The NaY zeolite catalyst was prepared from locally available Iraqi kaolin in order to use it in the esterification reaction of oleic acid. X - ray diffraction, scanning electronic microscopy, sodium content, silica to alumina ratio, surface area and pore volume were determined for the prepared NaY zeolite. The results of x - ray diffraction and scanning electron microscopy show that the prepared NaY zeolite has approximately the same crystal structure as the standard. The sodium content was 12.26 wt. %, and the silica to alumina mole ratiowas 2.6, surface area 330 m2/g and pore volume 0.35 cm3/g. Because of the oleic acid is one of the free fatty acids that can found in vegetable oils and animal fats. Oleic acid used as a suggested feedstock to study and simulate production of biodiesel via esterification reaction.Esterification reaction was analyzed at different operational conditions including the ethanol/oleic acid molar ratio of 3/1 and 6/1, different temperature from 40 to 70 °C, reaction time up to 180 minutes and catalyst (2, 5 and 10 wt. % NaY zeolite). The maximum conversion of oleic acid (about 0.83) was observed at 6/1 ethanol/oleic molar ratio, 70 °C reaction temperature, 10 wt. % NaY zeolite as a catalyst, and 60 minutes contact time. The study of the kinetics of the esterification reaction of oleic acid, indicated that the value of the activation energies of esterification ware 42692 and 17218 J/mol for forward and backward reaction respectively, and frequency factors were 7.2*104 (mol - 1/minute) for forward reaction and 4.5 (mol - 1.25/minute) for backward reaction. The values of reactants and products orders were 1, 1, 1.2 and 1 for oleic, ethanol, ester and water respectively.The statistical analysis of the esterification reaction and experimental data indicates that the average relative error was 1.53, within 0.95 confidence level.ReactOp cascade package simulator used for simulation the behavior of batch and plug flow reactors in different operating modes (adiabatic and isothermal) carried out at selected operating conditions Contents Contents.

عمليات التنافذ الامامي - العكسي لمعالجة المياه الملوثة بالزيوت == Forward - Reverse Osmosis Processes For Oily Wastewater Treatment

Author name: نور حمود زغير
Supervisor name: حسن فرهود مكي
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: في هذه الدراسة, تم بحث مدى ملائمة عمليات التنافذ (الامامي - العكسي) لمعالجة المياه الملوثة بالزيوت. حيث طبقت عملية التنافذ الامامي لاسترجاع الماء النقي من المياه الملوثة بالزيوت. تم استخدام زيت محرك الديزل والكازولين نوع (15W - 40) لتحضير محلول اللقيم, بي | In this study, the feasibility of Forward - Reverse membrane osmosis system was investigated for treating the oily wastewater. Forward osmosis (FO) process was applied to recover pure water from oily wastewater. Gasoline and diesel engine oil (15W - 40) was used to prepare the feed solution (FS). While sodium chloride (NaCl) and magnesium chloride (MgCl2) salts were used as draw solutions, and the membrane that was used in FO process was cellulose triacetate (CTA) membrane. While reverse osmosis process was used to recovery water from the diluted draw solution using polyamide (thin film composite (TFC)) membrane. In the first stage was applying the FO process for treating the oily wastewater with two parts. The first part included the FO process using the batch system whereas the second part included the FO process using the flowing system for different draw solutions. Theoperating parameters studied were : draw solution type, draw solution concentrations (0.25 - 0.75 M), oil concentration in FS (100 - 1000 ppm), the temperatures of FS and DS (30 - 45 °C), pH of FS (4 - 10) and for the forward osmosis flowing process the flow rate of both DS and FS (20 - 60 l/h), while the pressure was maintained at 0.5 bar. The run - time of the FO process was for five hours. It was found that water flux through membrane decreases with increasing time, while oil concentration in the FS increases with increasing time. Also, it was found that the water flux produced from the osmosis cell and oil concentration in FS increase by increasing the concentration of draw solutions, the flow rate of FS and the temperature for a limit (40oC), then, the water flux and oil concentration decrease with increasing the temperature because of happening the internal concentration polarization phenomenon. By increasing the oil concentration in FS and the flow rate of the DS, the water flux and oil concentration in FS were decreased. While it had a fluctuated behavior with increasing the pH of oily wastewater. It was found also that MgCl2 gives water flux higher than NaCl. It was observed that the best operating conditions in this study were : concentration of salt (0.75 M) for MgCl2, oil concentration (100 ppm), pH of FS (7.3), temperature of feed and draw solution (40oC), flow rate of FS (60 l/h), and flow rate of DS (20 l/h). The values of resistance to solute diffusion within the membrane porous support layer were 55.93 h/m and 26.21 h/m for NaCl and MgCl2 respectively. The second stage was applied reverse osmosis process for separating the fresh water from a diluted (NaCl) solution using different parameters such as draw solution concentration (0.08 - 0.16 M), feed flow rate (20 - 40 l/h) within two hours of work of the reverse osmosis system.

معالجة واعادة استخدام المياه الناتجة من حقول نفط الاحدب العراقية == Treatment And Reuse of Produced Water From Al - Ahdab Iraqi Oilfields

Author name: حسين باسم عليوي
Supervisor name: Basma A. Abdul | Majeed
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: الهدف الاساسي من هذا البحث هو تطوير طريقة عملية لمعالجة المياه المنتجة من حقول النفط العراقية. في هذه الدراسة تم توظيف نظام متحد من ثلاث عمليات معالجة هي التخثير والامتزاز والتبادل الايوني لازالة وتقليل بعض الملوثات الرئيسية مثل العكورة والمحتوى الزيتي وم | The overall goal of this research was to develop a practical method of treating co - produced waters from oil - field sources. In this study, combined coagulation - adsorption - ion exchange treatment was employed for the removal of some main contaminants like turbidity, oil content, and total dissolved solids from produced water. These combination steps are not studied before. The wastewater used in this work was taken freshly form Al - Ahdab oilfields. The coagulants used in this study were aluminum sulfate (alum) as a primary coagulant and calcium hydroxide (lime) as a coagulant aid. The performance of these coagulants was investigated through jar test by comparing turbidity removal at different coagulant / coagulants aid ratio, coagulant dose, water pH, and sedimentation time. The best conditions for turbidity removal can be obtained at coagulant dosage of 80 mg/L at pH 6 and 120 min for sedimentation time. There was an improvement in the turbidity removal when 25% lime was used in conjunction with 75% alum. At these conditions, the turbidity reading was reduced from 92 to 2.1 NTU. In addition, an attempt was made to examine the relationship between turbidity (NTU) and total suspended solids (mg/L) on the same samples of produced water. This study presents an investigation on the technical feasibility of using organoclay for adsorption of oil content from produced water. The organoclay was prepared by combination of Iraqi bentonite with quaternary amine (tetraethylammonium chloride). Batch mode experiments were conducted to study the effects of amine/ bentonite ratio, organoclay quantity, pH, and contact time. The analysis results showed that the organoclay adsorbent was very effective in removing oil content from produced water and the best results obtained for the removal of oil content are 16 g/L of prepared organoclay having 35 g amine/ 100 g bentonite, pH 3, and 120 min for contact time. These results reduce the concentration of oil content from 532.1 to 2.7 mg/L. Equilibrium adsorption isotherms and kinetics were investigated. The adsorption isotherm data were fitted well to Temkin isotherm as highest coefficient of correlation (R2=0.996) and lowest value of standard deviation (Sd=2.385). The adsorption kinetic data were fitted very well the pseudo - second order kinetics model (R2=0.997 and Sd=1.644). The continuous experiments were carried out in a fixed - bed column. The results revealed that adsorption capacity increases with increasing bed depth and with decreasing flow rate. In this work, a continuous ion exchange study in fixed - bed columns was performed to reduce TDS concentration from produced water. The experiments were subjected to lab - scale ion exchangers, consisting of two types of commercial resins connected in series. The two types of resins used in this work were : strongly acidic cation exchanger of type Dowex 650C and strongly basic anion exchanger of type Dowex I. 550A. Comparison of Thomas, Yoon - Nelson, and Adams - Bohart models with experimental kinetics results was done, and model parameters were evaluated by linear regression analysis for TDS reduction in different bed depths and flow rates. The obtained experimental data were in good agreement with Thomas and Yoon - Nelson models (R2 reaches to 0.996). Reverse flow regeneration was carried out in a fixed - bed column for exhausted resin by washing with diluted acid and base solutions. The regenerated resin was reused in the same column. Approximately, 65% of the original sorption capacity was restored.

فعالية عامل مساعد محضر ومحفز بمعادن مختلفة لعملية ازالة الكبريت بالهدرجة لزيت الغاز العراقي == Activity of A Prepared Catalyst Promoted By Different Metals For The Hydrodesulfurization of Iraqi Gas Oil

Author name: طارق محمد نايف
Supervisor name: Abdul | Halim A.K. Mohammed | Hussein K. Hussein
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: The present work deals with the improvement of Iraqi gas oil containing 1.402 wt. % sulfur by hydrotreating process using different prepared hydrodesulfurization catalysts (Ni - Mo/? - Al2O3, Co - Mo/? - Al2O3, Co - Ni - Mo/? - Al2O3, Ti - Ni - Mo/? - Al2O3 and Re - Ni - Mo/? - Al2O3). All catalysts were prepared under vacuum impregnation to ensure efficient precipitation of metals within the carrier ? - Al2O3. Physical adsorption by nitrogen was investigated, and used for determination of the surface area and pore size distribution of prepared catalysts.The results showed that modified catalysts Ti - Ni - Mo/? - Al2O3 and Re - Ni - Mo/? - Al2O3 have a high surface area 225.1 and 235.23 m2/g respectively, as compered with conventional prepared catalysts Ni - Mo/? - Al2O3 and Co - Mo/? - Al2O3 which their have surface area 178.5 and 191.4 m2/g respectively, and exhibits behavior of type four according to Brunauer, Emmett and Teller (BET) classification, and type H1 according to de Boer classification for hysteresis loop, so, it was concluded that the pores of these catalysts are cylindrical. The performances of all the synthesized catalysts for removal of sulfur and aromatic saturation gas oil were tested at different LHSV (1 to 4 h - 1), temperatures ( 275 to 350 °C), constant pressure 40 bar, and H2/HC ratio 500 ml/ml. The results showed that the sulfur and aromatic content were decresed at all operating conditions for all prepared catalysts. It was found that the sulfur removal from gas oil increases with temperature and decreasing with the space velocity, and the temperature has higher effect on the process of sulfur removal than the space velocity. It was found also that Ni - Mo/? - Al2O3 catalyst is slightly better in sulfur removal (61.5 wt. % ) with than Co - Mo/? - Al2O3 (59.2 wt. %) at the same operation conditions (350 °C and LHSV 1 h - 1), and hydrodesulfurization over Ni - Mo/Al2O3 was improved remarkly by adding Ti and Re promoters. Maximam sulfur removal was 76.81 wt. % using Re - Ni - Mo/? - Al2O3 at temperature 350?C, LHSV 1 h - 1, while minumum aromatic content value is 15.44 wt. % for Ni - Mo/ ? - Al2O3. Calculations showed that the hydrodesulfurization rate expressions fitted with second order reaction kinetics model.The rate constant varied from 0.005 to 0.144 liter/kg.h and the values of activation energy varied from 50.0 to 93.59 kJ/mole for all prepared catalysts. Thiele modulus, for all prepared catalysts was calculated.The lower values of the Thiele modulus (> 0.4) gives strong evidence of negligible pore diffusion limitation.

ازالة المحتوى الكبريتي من وقود الديزل بواسطة الاكسدة والاستخلاص بالمذيب == Desulfurization of Diesel Fuel By Oxidation And Solvent Extraction

Author name: شيم بهجت عبد الكريم
Supervisor name: ودود طاهر محمد | رغد فريد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: يهدف البحث الى ازالة المحتوى الكبريتي من مقطع الديزل المهدرج للتخلص من المركبات الكبريتية الثايوفينية التي تتعذر ازالتها بواسطة عملية الهدرجة المعتمدة في المصافي النفطية. ودراسة افضل الظروف للحصول على اعلى نسبة ازالة.رست الظروف التشغيلية التالية : سرعة ال | 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 diebenzothiophene) are very difficult to remove and need deep desulfurization processes.This work was applied to the desulfurized diesel fuel produced from the conventional HDS process for ultra - desulfurization. The used fuel types in this investigation were either real diesel fuel or simulated diesel fuel, where sulfur - containing compound ( dibenzothiophene DBT) converted to its corresponding sulfone by oxidation using hydrogen peroxide as an oxidant and acetic acid as homogenous catalyst, and solvent extraction by using acetonitrile (ACN) or N - methyl - 2 - pyrrolidone (NMP) as extractants.Simulated diesel fuel according to British Petroleum 200B doped with dibenzothiophene (DBT) was prepared, the effect of stirring speed (150, 250, 350 and 450) rpm, temperature (30, 40, 45 and 50) ?C, oxidant/simulated diesel fuel ratio (0.5, 0.75,1 and 1.5) (v/v), catalyst/oxidant ratio (0.125, 0.25, 0.5 and 0.75) (v/v), solvent type, and solvent/simulated diesel fuel ratio (0.5, 0.6, 0.75 and 1) (v/v) were examined in order to obtain the maximum sulfur removal. The results of this work exhibit that the highest removal of sulfur 98.5% for N - methyl - 2 - pyrrolidone and 95.8% for acetonitrile were obtained under the conditions of operating in table below : Stirring Speed (rpm) 350 Temperature (?C) 50 Oxidant (hydrogen peroxide)/simulated diesel fuel ratio 1 Catalyst (acetic acid)/oxidant ratio 0.5 Solvent (ACN or NMP)/simulated diesel fuel ratio 1 Experiments with the above best conditions were carried out on Real diesel fuel obtained from Al - Dora refinery with 1000 ppm sulfur containing compounds. It was found that sulfur removal from real diesel fuel was 62.5% for acetonitrile and 75% for N - methyl - 2 - pyrrolidone.

استخلاص الزيوت العطرية من قشور الحمضيات باستعمال التقطير البخاري بمساعدة المايكرويف == Extraction of Essential Oils From Citrus By - Products Using Microwave Steam Distillation

Author name: سارة جبير صالح
Supervisor name: ابتهال كريم شاكر
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: يهدف هذا البحث الى استخلاص الزيت العطري من ثلاثة انواع من قشور الحمضيات (البرتقال, الليمون, اللالنكي) بطريقتين : التقطير البخاري والتقطير البخاري بمساعدة المايكرويف.ودراسة تاثير عوامل الاستخلاص : (وزن القشور, وقت الاستخلاص,طاقة المايكرويف ونوع قشور الحمضي | The main objectives of this research is to extract essential oil from : orange( citrus sinensis), lemon( citrus limon) and mandarin( citrus reticulata) peels by two methods : steam distillation (SD) and microwave assisted steam distillation (MASD), study the effect of extraction conditions : weight of the sample( 398.56g, 281.8g, 116.76g), extraction time, microwave power( 135W, 265W, 445W) and citrus peel type( orange, lemon, mandarin) on oil yield and compare the results of the two methods, the resulting essential oil was analyzed by Gas Chromatography (GC).Essential oils are highly concentrated substances used for their flavor and therapeutic or odoriferous properties, in a wide selection of products such as foods, medicines and cosmetics. Extraction of essential oil is one of the most time and effort consuming process. Microwave - assisted extraction is a green technique for the extraction of natural products. (MASD) was better than (SD) in terms of rapidity, energy saving and yield. (MASD) gave higher yield than (SD) with shorter extraction time, yield of orange oil extracted by (MASD) was (1.150%) in (35min.) compared to (1.095%) in (45min.) by (SD) process, same results obtained for lemon and mandarin. It was found that the optimal microwave power was (135W) and the yield was : (1.150%, 1.115%, 0.940%) for orange, lemon and mandarin respectively, (MASD) increased extraction temperature in short time and to a higher level compared to (SD).It was found that the optimal weight was (398.56g) and the yield in (SD) was : (1.095%) and MASD (1.091%) for orange oil, same results obtained for lemon and mandarin.The best citrus peel type which gave the highest yield was orange followed by lemon then mandarin in both processes.Limonene is the most abundant component in citrus essential oil, (GC) analysis showed that the amount of limonene increased in low microwave power with long extraction time for mandarin oil it was (84.3891% at 135W in 60min.), while for (SD) it was (83.0271% in 75min.) and decreased with increasing microwave power for orange oil it was (80.9661% at 265W in 35min.) while for (SD) it was (83.2189% in 45min.), (SD) was more convenient to give high amount of limonene because of the graduate temperature rise, while in microwave extraction exposure to low microwave power for long time would give complete recovery and better quality of essential oil.

تثبيط تاكل الحديد الكاربوني الواطئ في حامض الكبريتيك باستعمال كحول البولي فينيل ومستخلص نبات PIPER LONGUM == Corrosion Inhibition of Low Carbon Steel In Sulfuric Acid By PVA And Piper Longum Extracts

Author name: اياد بهاء الدين احمد
Supervisor name: ماجد ابراهيم عبد الوهاب | ابرائيل سركيس يارو
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Doctorate
Language: English
University location: Baghdad
First pages:
Abstract: The inhibitive power of Polyvinyl Alcohol (PVA) and the synergistic effects added on the inhibition power of PVA by two types of Piper Longum (PL) Ethanol Extracts (PLEXT) were investigated toward the corrosion of carbon steel in (0.2N) H2SO4 solution in the temperature range (30 - 60?C) and PVA concentration range (150 - 2000 PPM).The corrosion rate measurements were carried out using the following two standard corrosion measurements techniques.1. Weight loss technique was applied on carbon steel plates to evaluate inhibition efficiency in presence and absence of these inhibitors.2. Electrochemical Techniques were used to validate and support inhibition efficiencies found in weight loss techniques.A detailed study of the experimental methods and results is reported for each test conducted.The weight loss results showed that PVA could serve as a corrosion inhibitor but its inhibition power was found to be low for the corrosion of carbon steel in the acidic media.It was shown that the inhibition efficiency for (PVA) decreased with increasing temperature at a given PVA concentration. On the other hand it was shown that at given temperature the inhibition efficiency of (PVA) was increased with increasing of PVA concentration until a PVA concentration of 2000 ppm PVA was reached then only a slight decrease in inhibition efficiency was observed when increasing PVA concentration further.The Maximum inhibition efficiency reached was about 71 % at 30?C & 2000 ppm (PVA) concentration, calculated by the weight loss techniques.In order to improve the inhibition efficiency of PVA, by adding 6 ml/l of ethanol extracts of piper longum (PL) to a liter of the acid solution in presence of concentrations of PVA 150,500,1000.1500, and 2000 ppm at temperatures (30,40,50, and 60?C) was investigated.Weight loss results showed a jump in inhibition efficiency (% IE) value of the modified inhibitor mixture compared with the presence of PVA alone at all (PVA) concentrations for temperature range considered in this investigation.This study demonstrated the extra inhibition power added by the (PL) fruit extracts to the organic polymer (PVA) used. Maximum inhibition efficiencies recorded were approximately 95% for Piper Longum Extract Number two (PLEXT2) at 30?C and 2000 ppm PVA.The kinetic and thermodynamic parameters regarding the adsorption process of inhibitors used was calculated.It was found that the changes corrosion rates correlates well with the Arrhenius equation in absence and presence of inhibitors.The Results showed that the adsorption of the polymer and the plant extract follows Langmuir adsorption isotherms and the adsorption of the inhibitor molecules on the metal surface is mainly physical, nevertheless the adsorption is believed to be slightly deviated from the Langmuir model at 30?C.Electrochemical analysis of the corrosion process of carbon steel in an electrochemical corrosion cell was investigated using 3 - Electrode corrosion cell coupled with a potentiostat interfaced with a computer which assisted polarization data interception and interpretation.Polarization technique was used to obtain polarization data which was recorded for carbon steel in 0.2N H2SO4 solutions in presence and absence of the inhibitors investigated. Electrochemical runs were done in the (PVA) concentrations of 150, 1000, and 2000 PPM and a temperatures of 30, 40, 50, and 60?C.Tafel slopes, Corrosion currents, and corrosion rates were calculated from polarization curves by Tafel extrapolation method. Results showed corrosion rate trends similar to findings by the weight loss method. It was indicated also that the corrosion of carbon steel in 0.2N H2SO4 is highly activity controlled.Results revealed that the inhibition action is occurring at both anodic and cathodic sites on the metal surface so that both corrosion reactions were affected, so that the composite inhibitor could be considered as mixed - type inhibitor.Electrochemical results confirmed that (PLEXT2) was more efficient as inhibition improvement additive to (PVA) than (PLEXT1) at all experimental conditions range encountered in this study.The highest inhibition efficiency recorded using Tafel polarization method was 83% obtained at 30?C and 2000 ppm of PVA with 6 ml/l PLEXT2.

تحضير الكاربون المنشط من نوى التمر باستخدام كاربونات البوتاسيوم كعامل منشط في ازالة صبغة المثيلين الزرقاء == Preparation of Activated Carbon From Date Stones By K2Co3 Activation For Methylene Blue Dye Adsorption

Author name: اسماء فاضل عباس
Supervisor name: مثنى جبار احمد
General topic: Chemical Engineering
Specific topic: Chemical Engineering
Degree: Master
Language: English
University location: Baghdad
First pages:
Abstract: Present study deals with the preparation of activated carbon (AC) from date stones by K2CO3 activation via microwave heating and the removal of methylene blue (MB) dye from aqueous solution by using such carbon as adsorbent. The influence of radiation time (4 - 12min), radiation power (540 - 700W) and impregnation ratio (0.5 - 2.5g/g) on the yield and MB uptake of such carbons were studied. Central composite design was used to determine the optimum preparation conditions and two quadratic models were developed to correlate the preparation variables for both responses.The optimum preparation conditions were reported as 8 min radiation time, 660 W radiation power and 1.5 g/g impregnation ratio resulting in 19.99% yield and 460.123 mg/g MB uptake. From the analysis of variance (ANOVA), it was found that the radiation time had the greatest effect on the yield while impregnation ratio had the greatest effect on MB uptake.The characteristics of AC were examined by pore structure analysis, scanning electron microscopy (SEM) and Fourier transforms infrared spectroscopy (FTIR). The BET surface area and total pore volume were indentified to be 1144.25 m²/g and 0.656 m³/g, respectively. Batch adsorption study was adopted to determine the experimental adsorption isotherm data of different initial concentration of MB (50 - 450 mg/l). The equilibrium data were analyzed using Langmuir, Freundlich and Sips isotherm models. The results showed that the experimental data were well fitted with sips isotherm with maximum monolayer adsorption capacity of 484.7 mg/g. Pseudo - First order, Pseudo - Second order, and intraparticle diffusion models were used to analyze experimental kinetics data with high correlation coefficient for Pseudo - second - order model.
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