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دراسة اقتناص ثاني اوكسيد الكاربون من الغاز الطبيعي == Study on CO2 Capture from Natural Gas

اسم المؤلف: ضياء جمعة جاسم
اسم المشرف: ثامر جاسم محمد | محمد فاضل عبد
الموضوع العام: الهندسة الكيمياوية
السنة: 2022
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

تطبيق MCM-41 كمادة مازة في نظام الغشاء الهجين لازالة صبغة الميثيل الخضراء من محلول مائي == Application of MCM-41as an Adsorbent in Hybrid Membrane System for Removal of Methyl Green Dye from Aqueous Solution

اسم المؤلف: سجى محسن جبار
اسم المشرف: طالب محمد البياتي | جمال مانع الربيعي
الموضوع العام: الهندسة الكيمياوية
السنة: 2020
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

تحضير وتوصيف محلول سحب جديد لتحلية المياه باستخدام التناضح الامامي والتقطير الغشائي == Preparation and Characterization of a Novel Draw Solution for Water Desalination Using Forward Osmosis and Membrane Distillation

اسم المؤلف: عفراء هلال كامل
اسم المشرف: قصي فاضل الصالحي | صلاح سلمان ابراهيم
الموضوع العام: الهندسة الكيمياوية
السنة: 2022
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

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

اسم المؤلف: صفاء رشيد ياسين
اسم المشرف: عبد الحليم عبد الكريم محمد
الموضوع العام: الهندسة الكيمياوية
السنة: 2005
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

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

اسم المؤلف: انيس عبد الله كاظم الشمري
اسم المشرف: ابرائيل سركيس يارو
الموضوع العام: الهندسة الكيمياوية
السنة: 2005
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

Hydrodynamic Characteristics of Three-phase non-Newtonian Liquid-Gas and Solid fluidized beds

اسم المؤلف: علي حسين جواد
اسم المشرف: Abbas H. Sulaymon | Thamer J. Mohammed
الموضوع العام: الهندسة الكيمياوية
السنة: 2006
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

Hydrodynamic Interaction in Bubbly Two - Phase Flow

اسم المؤلف: Thamer Jasim Mohammed
اسم المشرف: Abdullah A. Kendoush | Balasim A. Abid
الموضوع العام: الهندسة الكيمياوية
السنة: 1997
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

Heat Transfer With Mass Transfer Effect in Forced Convective Boiling of Multi Component Fluids

اسم المؤلف: Neran Khalil Ibrahim
الموضوع العام: الهندسة الكيمياوية
السنة: 1997
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:

Development of a Microcomputer Environment for Cemical Process Design : an Object-Oriented Approach

اسم المؤلف: Riad Raouf Sabti
اسم المشرف: M. S. H. Al-Anbaki
الموضوع العام: الهندسة الكيمياوية
السنة: 1998
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد

The Improvement Of Rheological Properties Of Al - Dura Refinery As Phaltic Binders Vsing Different Add It Ives

اسم المؤلف: Qays mothanna ammouri
الموضوع العام: الهندسة الكيمياوية
السنة: 2010
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
مكان الجامعة: بغداد
الكلمات الدلالية:
  • chemical engineering

Removal Of Emulsified Kerosen From Water By Flotation

اسم المؤلف: al - genabi ahmed abid mohammed
الموضوع العام: الهندسة الكيمياوية
السنة: 2004
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
مكان الجامعة: بغداد
الكلمات الدلالية:
  • mass transfer

Tree Phase Direct Contact Heat Transfer

اسم المؤلف: Najim Abid Jassim
الموضوع العام: الهندسة الكيمياوية
السنة: 2004
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
مكان الجامعة: بغداد
الكلمات الدلالية:
  • Heat - transmission

Astudy Of The Dehydration Process Of Natural Gas In Iraqi North Gas Company And The Treatment Methods Of Molecular Sieve Problems

اسم المؤلف: zangana farman saeed abd
الموضوع العام: الهندسة الكيمياوية
السنة: 2012
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
مكان الجامعة: بغداد
الكلمات الدلالية:
  • gas , natural - underground storage

Treatment Of The Industrial Water Using Ion Exchange

اسم المؤلف: sandra solaqa poulus
الموضوع العام: الهندسة الكيمياوية
السنة: 2012
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
مكان الجامعة: بغداد
الكلمات الدلالية:
  • ion exchange

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.

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.

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.

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

اسم المؤلف: اسراء عبد الجبار صالح النعمة
اسم المشرف: نجوى صابر مجيد
الموضوع العام: الهندسة الكيمياوية
السنة: 2015
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.

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

اسم المؤلف: حسين باسم عليوي
اسم المشرف: Basma A. Abdul | Majeed
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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

اسم المؤلف: طارق محمد نايف
اسم المشرف: Abdul | Halim A.K. Mohammed | Hussein K. Hussein
الموضوع العام: الهندسة الكيمياوية
السنة: 2014
الموضوع الدقيق: الهندسة الكيمياوية
الدرجة: دكتوراه
اللغة: الانكليزية
مكان الجامعة: بغداد
الصفحات الاولى:
المستخلص: 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.
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