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    Azote Removal in Submerged Fixed Bed Reactor by Modified Ludzack-Ettinger (MLE)Process

    , M.Sc. Thesis Sharif University of Technology Rajaei, Forough (Author) ; Borgheei, Mahdi (Supervisor)
    Abstract
    Nitrogen compounds are becoming increasingly important in wastewater management, because of the many effects that nitrogenous material can have on the environment that need nitrogen removal. In this study, the performance of a submerged fixed bed reactor in nitrogen removal, constructed two anoxic and aerobic sections under Modified Ludzack-Ettinger process was investigated. Laboratory experiments were conducted at a constant COD concentration of 350 mg/lit, hydraulic retention times of 8, 12 and 18 hours and influent ammonia loading rate between 0.128 and 0.955 g NH3/m2.day. Nitrogen removal efficiency was obtained between 80.4 and 97.3%, and COD removal efficiency was achieved between 88.9... 

    Upgrading Activated Sludge Study System by Introducing Moving Carriers

    , M.Sc. Thesis Sharif University of Technology Mofidian, Maryam (Author) ; Borghei, Mehdi (Supervisor) ; Mosleh Abadi, Moslehi (Co-Advisor)
    Abstract
    In this study, the use of a fixed bed of the Kaldnes commercial carrier in the activated sludge system has been investigated. In this way, at zero time, a submerged fixed bed of Kaldnes was placed into a completely mixed activated sludge reactor and its various parameters were investigated during the time. During the experiment, the fixed bed (Kaldnes carriers enclosed in a lace) with 20, 35 and 50 percentage of volumes were compared to regular activated sludge reactors (without any carriers). The studied parameters are COD, DO, MLSS, and P-PO43-. Input COD was changed at concentrations of 1200 and 400 mg/L, and the reactor hydraulic time was adjusted to 10 and 16 hours. It was observed that... 

    Study of Capability a Fixed-bed Anaerobic-aerobic System to Remove Phosphorus from Wastewater

    , M.Sc. Thesis Sharif University of Technology Barzinmehr, Hossein (Author) ; Borghei, Mehdi (Supervisor)
    Abstract
    Discharge of Raw wastewater or effluent of Treatment plants into the natural bodies of water, in the case of high nutrients may cause serious problems such as algae bloom which results in a reduction in concentration of dissolved oxygen. Among the nutrients, phosphorous is known as a limiting factor in growth and intensification (intensifier) of eutrophication. Therefore, elimination of phosphorus from wastewater prior to the discharge point is highly important. Phosphorus can be removed chemically as well as biologically. Chemical methods are known, efficient and reliable but Problems like operational and maintenance costs and chemical sludge production cause tendency to use biological... 

    Experimental Removal of Aromatic Hydrocarbons by Thermophilic Bacteria in a Fixed Bed Reactor

    , M.Sc. Thesis Sharif University of Technology Bokaee, Shima (Author) ; Borghei, Mehdi (Supervisor) ; Vossoughi, Manouchehr (Supervisor) ; Zeinali, Majid (Supervisor)
    Abstract
    According to the environmental lows and standards, wastewater of petroleum industries such as refineries and petrochemical that include many petroleum compounds like aromatic and aliphatic hydrocarbons, must be treated up to desirable limit, before entering the collecting network. Using microorganisms is one of the fundamental ways of biodegradation of these polluted compounds. Since phenolic compounds are the main components of raw petroleum, strains that are capable of tolerating phenol and usage of this poisonous hydrocarbon are specifically important. Therefore, in this study the potentiality of the indigenous thermophilic bacterium Nocardia otitidiscaviarum strain TSH1, for degradation... 

    CFD Modeling of Fixed Bed Reactor for Direct Synthesis of DME from Syngas and Carbon Dioxide

    , M.Sc. Thesis Sharif University of Technology Moradi, Fazel (Author) ; Kazemeini, Mohammad (Supervisor)
    Abstract
    Today, the global environmental restrictions as well as; energy problems have directed researchers toward developing ideas of producing a clean liquid fuel from coal or natural gas as a major research topic. In this regard, a special attention is paid to the dimethyl ether (DME) as a clean material containing 34.8% oxygen possessing enough positive potential to replace the diesel and LPG fuels. One of the most economic routes for producing the DME is known to be the direct conversion of the synthesis gases and carbon dioxide first to the methanol and then its dehydration to the DME. Moreover, the DME is not limited to a particular country or resource area since small reservoirs of natural... 

    Modeling and Control of Ethylene Oxide Reactor

    , M.Sc. Thesis Sharif University of Technology Ghaffari, Soodabeh (Author) ; Shahrokhi, Mohammad (Supervisor)
    Abstract
    Modeling and Control of Ethylene Oxide Reactor In this thesis, steady and dynamic modeling of an ethylene oxide fixed bed reactor has been studied and one dimensional pseudo homogeneous model was used for simulating the reactor. Kinetic parameters were obtained by minimizing an object function and using the genetic algorithm. A good agreement is observed between simulation and experimental results. In steady state condition, the influence of some parameters such as shell temperature, feed rate were investigated on the performance of the reactor. The heat of reaction is used to produce steam. A dynamic model for steam drum was also considered and used for control purpose. A PI controller was... 

    Mathematical Modeling of Fixed bed Reactor for Oxidative Dehydrogenation (ODH) Process of Light Paraffins

    , M.Sc. Thesis Sharif University of Technology Darvishi, Ali (Author) ; khorashe, Farhad (Supervisor)
    Abstract
    An industrial scale reactor for light olefinsproduction was modelledusing the oxidative dehydrogenation (ODH) of light paraffinsin a multi-tubular reactor system involving 10000 small diameter tubes immersed in a shell with proper liquid-cooled flows. Here a theory-based pseudo-homogeneous 1-D model describing the operation of a fixed bed reactor for the ODHparaffinstoolefins over a Ni-Nb-O mixed oxide catalyst (for ethane) and over a V2O5/γ-Al2O3catalyst (for Propane),was employed. The paraffin and oxygen conversions, gas process and coolant temperatures, as well as other parameters affecting the reactor performance, including pressure, were examined. Furthermore, the applied model showed... 

    Computational Fluid Dynamic (CFD) of Fixed-Bed Reactor for Bio-treatment of Sulfur from Petroleum Cuts

    , M.Sc. Thesis Sharif University of Technology kharghanian, Hosein (Author) ; Yaghmaei, Soheila (Supervisor)
    Abstract
    Bio-desulfurization is the sulfur removal process from organosulfur compounds by the action of microorganisms (which are capable of removing sulfur). Too many studies have been carried out in the use of biocatalysts for BDS process. In this project, we have used data obtained from a previous experiment in which a trickle bed reactor (diameter: 0.066 m, height: 0.6 m) and a Rhodococcus sp. 12891 starin immobilized on bed particles are used to produce diesel with low sulfur content. Sulfur concentration of inlet diesel is between 200ppm to 540 ppm. parameters of process are recycle Ratio , volumetric flow rate and sulfur content of inlet diesel.
    A mathematical model for trickle bed... 

    CFD Simulation of Hydro-desulfurization Process of Gas oil in TBR Reactor

    , M.Sc. Thesis Sharif University of Technology Tavakoli, Saeed (Author) ; Farhadi, Fathollah (Supervisor)
    Abstract
    One of the most undesirable compounds present in various crude oil cuts are sulfur compounds That creates a lot of problems in different stages of refining and when consumed. In this study, the hydro-desulfurization process that is the most common method of treating oil cuts in the refinery industry and in terms of economic and environmental special place in the oil industry and related industries, has been discussed. In hydro-desulfurization process, sulfur compounds under high pressure and temperature, are converted to hydrogen disulfide in a catalytic reactor. In this study, the catalytic reactor may be simulated with the utmost care. In this context, Euler-Euler two-phase model that is... 

    Mathematical Modeling of Catalyst Deactivation of the Methanol to Gasoline (MTG) Process in a Fixed-bed Reactor

    , M.Sc. Thesis Sharif University of Technology Hashemizadeh, Yahya (Author) ; Kazemeini, Mohammad (Supervisor)
    Abstract
    Nowadays, with respect to environmental pollution and energy supply, producing gasoline from methanol or syngas is one of the most interesting research subjects. Gasoline production from methanol is a catalytic process that produces high-quality gasoline with minimum unwanted compounds. So this gasoline is a clean fuel and it can be replaced to petroleum gasoline. Because of that, it can be a valuable process in the petrochemical industry. One of the most important aspects of this process is catalyst deactivation with respect to time on stream. Catalyst deactivation is usually caused by poisoning, sintering, blocking pores, and coking. In this research, material and energy balance equations... 

    Studying of Laccase Immobilization on Nanoparticles for Bisphenol A Removal

    , M.Sc. Thesis Sharif University of Technology Sadeghzadeh, Sadegh (Author) ; Borghei, Mehdi (Supervisor) ; Ghobadi Nejad, Zahra (Co-Supervisor)
    Abstract
    Bisphenol A is one of Endocrine Disturbing Chemicals. Enzymatic removal of bisphenol A is an interesting and green method. However, application of enzymes has been hampered due to lower operational stability and lots of difficulties in recovery and recycling. Enzyme immobilization can ba an innovative approach to circumvent these drawbacks. Laccase from Trametes hirsuta used for Bisphenol A removal. Firstly, magnetic nanoparticles were synthesized by coprecipitation method and aminofunctionalized by (3-aminopropyl)-mmethoxysilane. Subsequently, laccase was precipitated with i-propanol in the presence of aminofunctionalized nanoparticles and followed by addition of glutaraldehyde to the final... 

    Simulation and Control of Fixed Bed OCM Reactor

    , M.Sc. Thesis Sharif University of Technology Valadkhani, Ali (Author) ; Shahrokhi, Mohammad (Supervisor) ; Pishvaei, Mahmoud Reza (Supervisor) ; Zarrinpashneh, Saeed ($item.subfieldsMap.e)
    Abstract
    Oxidative coupling of methane (OCM) in a fixed bed tubular reactor over Mn-Na2WO4/SiO2 catalyst has been studied. Four kinetic models have been considered for OCM reactions. Based on an objective function and using genetic algorithm, kinetic parameters have been estimated. A reactor tube with 20 mm diameter and 400 mm length surrounded by molten salt for removing heat of reaction has been used for experimental study. Effects of different factors such as CH4/O2 ratio, nitrogen content in feed and contact time are investigated experimentally and by simulation. A good agreement has been observed between simulation and experimental data. Oxidative coupling of methane (OCM) in an industrial fixed... 

    Optimization of Biological Removal of Nitrogenous Compounds by Using Aerobic and Anoxic Fixed-Bed Bioreactors

    , M.Sc. Thesis Sharif University of Technology Ghasem Aligoudarzi, Mehdi (Author) ; Borghei, Mehdi (Supervisor)
    Abstract
    Nitrogen compounds are becoming increasingly important in wastewater management. Due to several adverse effects which nitrogenous materials can have on the environment, there is a significant need for nitrogen removal. In this study, the biological nitrogen removal process from a wastewater with low COD was investigated in a submerged fixed bed reactor, constructed two anoxic and aerobic sections under Modified Ludzack-Ettinger process. Volume of each section was 10 liters. About 60% of each section was occupied with pumice stone.Experiments were conducted in 9 runs, for hydraulic retention times of 8, 6 and 4 hours, influent ammonia concentrations of 180, 90 and 30 mg/lit and recyle ratios... 

    Application of a continuous kinetic model for the hydrocracking of vacuum gas oil

    , Article Petroleum Science and Technology ; Vol. 32, Issue. 18 , 2014 , Pages 2245-2252 ; ISSN: 10916466 Arefi, A ; Khorasheh, F ; Farhadi, F ; Sharif University of Technology
    Abstract
    Hydrocracking is one of the most versatile petroleum refining processes for production of valuable products including gasoline, gas oil, and jet fuel. In this paper, a five-parameter continuous lumping model was used for kinetic modeling of hydrocracking of vacuum gas oil (VGO). The model parameters were estimated from industrial data obtained from a fixed bed reactor operating at an average temperature of 400°C and residence time of 0.3 h. Product distributions were obtained in terms of the weight fraction of various boiling point cuts. The model parameters were estimated using the Nelder-Mead optimization procedure and were correlated with temperature. Comparison of experimental and... 

    A three dimensional CFD simulation and optimization of direct DME synthesis in a fixed bed reactor

    , Article Petroleum Science ; Vol. 11, issue. 2 , 2014 , pp. 323-330 ; ISSN: 1672-5107 Moradi, F ; Kazemeini, M ; Fattahi, M ; Sharif University of Technology
    Abstract
    In this study, a comprehensive three-dimensional dynamic model was developed for simulating the flow behavior and catalytic coupling reactions for direct synthesis of dimethyl ether (DME) from syngas including CO2 in a fixed bed reactor at commercial scale under both adiabatic and isothermal conditions. For this purpose, a computational fluid dynamic (CFD) simulation was carried out through which the standard k-e{open} model with 10% turbulence tolerations was implemented. At first, an adiabatic fixed bed reactor was simulated and the obtained results were compared with those of an equivalent commercial slurry reactor. Then the concentration and temperature profiles along the reactor were... 

    Fixed-bed multi-tubular reactors for oxidative dehydrogenation in ethylene process

    , Article Chemical Engineering and Technology ; Volume 36, Issue 10 , 2013 , Pages 1691-1700 ; 09307516 (ISSN) Fattahi, M ; Kazemeini, M ; Khorasheh, F ; Darvishi, A ; Rashidi, A. M ; Sharif University of Technology
    2013
    Abstract
    An industrial-scale reactor for ethylene production was modeled using the oxidative dehydrogenation of ethane (ODHE) in a multi-tubular reactor system, examining a variety of parameters affecting reactor performance. The model showed that a double-bed multi-tubular reactor with intermediate air injection scheme was superior to a single-bed design, due to the increased ethylene selectivity while operating under lower oxygen partial pressures. The optimized reactor length for 100% oxygen conversion was theoretically determined for both reactor designs. The use of a distributed oxygen feed with a limited number of injection points indicated a significant improvement on the reactor performance... 

    Simulation and experimental studies of methane oxidative coupling reaction in a bench scale fixed bed reactor

    , Article Energy Sources, Part A: Recovery, Utilization and Environmental Effects ; Volume 35, Issue 15 , Aug , 2013 , Pages 1418-1426 ; 15567036 (ISSN) Valadkhani, A ; Shahrokhi, M ; Pishvaie, M. R ; Zarrinpashneh, S ; Sharif University of Technology
    2013
    Abstract
    Oxidative coupling of methane in a bench scale fixed bed tubular reactor over Mn-Na2WO4/SiO2 catalyst has been studied. Four kinetic models have been considered for oxidative coupling of methane reactions and compared through experimental data, and the best kinetic model has been selected. For removing the heat of reaction, a molten salt bath system surrounding the reactor tube has been proposed. Effects of different factors, such as CH4/O2 ratio, are investigated through experimental and simulation studies. A good agreement has been observed between simulation and experimental data. The reactor behaviors under isothermal and adiabatic conditions have also been simulated  

    A Three dimensional dynamic CFD simulation for the direct dme production in a fixed bed reactor

    , Article Computer Aided Chemical Engineering ; Volume 32 , June , 2013 , Pages 247-252 ; 15707946 (ISSN) Moradi, F ; Kazemeini, M ; Vafajoo, L ; Fattahi, M ; Sharif University of Technology
    2013
    Abstract
    Dimethyl ether (DME) as a clean fuel seems to be a superior candidate for high-quality diesel fuel in near future. In this study, a comprehensive three-dimensional dynamic heterogeneous model developed to simulate the flow behavior and catalytic coupling reactions for synthesis of the DME from hydrogenation of the CO and CO2, dehydration of methanol to dimethyl ether and water gas shift reaction in a fixed bed reactor. For this purpose, a CFD simulation was articulated where the standard k-ε model with 10% turbulence tolerations implemented. Then the concentration and temperature profiles along the reactor were determined. It was revealed that under conditions considered, a single phase... 

    Theoretical investigations of methane conversion to heavier hydrocarbons in a plasma reactor

    , Article Advanced Materials Research, 2012, Chengdu ; Volume 548 , 5- 6 May , 2012 , Pages 153-159 ; 10226680 (ISSN) ; 9783037854532 (ISBN) Kazemeini, M ; Zare, M. H ; Safabakhsh, N ; Ferdosi, S. R ; Fattahi, M ; Sharif University of Technology
    2012
    Abstract
    In this study, mathematical modelling of oxidative coupling of methane (OCM) to C 2 hydrocarbons (C 2H 6 and C 2H 4) over La 2O 3/CaO catalyst in a fixed-bed reactor operated under isothermal and non-isothermal conditions was investigated using the MATLAB program. In this process, methane and acetylene were the inputted feed and ethane, ethylene, propylene, propane, i-butane and n-butane were the output products. The amount of methane conversion obtained was 12.7% for the former feed however; if pure methane was inputted this conversion rose to 13.8%. Furthermore, the plasma process would enhance the conversion, selectivity towards desired product and process yield. A comparison between the... 

    Simulation of activity loss of fixed bed catalytic reactor of MTO conversion using percolation theory

    , Article Chemical Engineering Science ; Volume 66, Issue 23 , December , 2011 , Pages 6199-6208 ; 00092509 (ISSN) Izadbakhsh, A ; Khorasheh, F ; Sharif University of Technology
    2011
    Abstract
    In this investigation, a reactor model for prediction of the deactivation behavior of MTO's porous catalyst in a fixed bed reactor is developed. Effect of coking on molecular transport in the porous structure of SAPO-34 has been simulated using the percolation theory. Thermal effects of the reaction were considered in the model and the temperature profile of the gas stream in the reactor was predicted. The predicted loss in catalyst activity with time-on-stream was in very good agreement with the experimental data. The resulting coke deposition and gas temperature profiles along the length of reactor suggested a reaction front moving toward the outlet of the fixed bed reactor at the...