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    A Heuristic Framework with Mathematical Modeling for Inherently Safe Design of Chemical Process with Sustainability Assessment of Case Study

    , M.Sc. Thesis Sharif University of Technology Daliri, Reza (Author) ; Rashtchian, Davoud (Supervisor)
    Abstract
    Inherently safer design is the new approach to maximize the overall safety of a process plant. This approach suggests some risk reduction strategies to be implemented in the early stages of design. There are different well-established strategies for making a process plant inherently safer. The benefits of applying these strategies on reducing the overall risk inside a plant are obvious. However, some of these changes are rejected many times because they appear to be too costly. But if the effects of applying inherently safer design strategies are investigated not only on the processing costs of a plant but also on the potential accident costs, the decision would in fact be different. In this... 

    Set membership identification and control of an iterative process

    , Article 18th European Control Conference, ECC 2019, 25 June 2019 through 28 June 2019 ; 2019 , Pages 36-41 ; 9783907144008 (ISBN) Rezaeizadeh, A ; European Control Assoication (EUCA) ; Sharif University of Technology
    Institute of Electrical and Electronics Engineers Inc  2019
    Abstract
    For processes that repeat the same task an iterative control method can be applied that learns from the previous runs and corrects the tracking error for the next run. Meanwhile, a set membership identification technique is be combined with the regulation part to identify the plant response using the informative input-output data of previous observations. This combination method has been experimentally tested on a radio frequency machine and the results are presented in the paper. © 2019 EUCA  

    Optimization of Process Plant Layout and Pipe Routing

    , M.Sc. Thesis Sharif University of Technology Mehrizi, Rahil (Author) ; Shadrokh, Shahram (Supervisor)
    Abstract
    Process plants such as refineries and petrochemical plants are complex facilities consisting of equipment, piping systems, instruments, electrical systems, computers, and control systems. Process units design is mostly based on designer`s experience and design general criteria and standards. Using mathematical methods to optimize the design may have an effective role in cost reduction and it would give the designer some general view in case that the exact design is not applicable.
    Optimization of Process units is described in this study. This optimization includes the exact location of each equipment, nozzle, pipe rack and also pipe route layouts. Mixed integer linear programming (MILP)... 

    An Ontological Study of Environmental Impact Assessment of Process Plant to Develop an Identification Software

    , M.Sc. Thesis Sharif University of Technology Mortazavi Asadabad, Behnoosh (Author) ; Farhadi, Fathollah (Supervisor) ; Bozorgmehry Boozarjomehry, Ramin (Supervisor)
    Abstract
    The environmental impact of process plants is one of the causes of the environmental disturbance in the world. Including the effects of these destructive impacts can be mentioned to the phenomena such as global warming, climate change, severe air pollution and water shortage. Hence, the economic justification of a process, without the review of relevance of its environmental impacts, it does not lead to the implementation and construction of a process plant. For this reason, it is a requirement to provide a software platform (preferably object-oriented) for quick and automatic checking of this item and the exact determining of these effects. On the other hand, due to the complexity of the... 

    Application of Quantitative Risk Assessment to Site and Layout Process Plants

    , Ph.D. Dissertation Sharif University of Technology Badri, Naser (Author) ; Rashtchian, Davod (Supervisor) ; Nourai, Farshad (Co-Advisor) ; Narimannejad, Alireza (Co-Advisor)
    Abstract
    Plant layout and siting are the earliest steps in any process design that may have significant effects on the further required level of safety and costs. Extensive carried out studies have been published in literatures in which, the safety factor has been taken into account in the form of prediction the severity of likely accidents. Majority of these studies are based on the accident consequence and other important parameters such as the accident frequency and the density of vulnerable items have been ignored. This recent negligence may lead to over conservative designs. To eliminate this recent deficiency, quantitative risk assessment (QRA) is the best procedure than can be suggested.... 

    Multi-Scale Design and Optimization of A High-Nitrogen-Content Natural Gas Processing Plant

    , M.Sc. Thesis Sharif University of Technology Mostafavi, Mahdi (Author) ; Farhadi, Fathollah (Supervisor) ; Eini, Saeed (Supervisor)
    Abstract
    Given the environmental benefits of natural gas (NG) in comparison to other fossil fuels and its potential contribution to the shift towards renewable energy, there is an anticipated rise in the demand for NG as an energy source in the coming years. This surge in demand has sparked a growing interest in the exploration and development of unconventional gas fields with low hydrocarbon content, which were previously considered economically unviable. Among these fields, those rich in nitrogen have garnered significant attention. However, the presence of high nitrogen content in NG poses notable challenges, including a decrease in calorific value and increased costs associated with... 

    Energy consumption in pervaporation, conventional and hybrid processes to separate toluene and i-octane

    , Article Chemical Engineering and Processing - Process Intensification ; Volume 128 , June , 2018 , Pages 46-52 ; 02552701 (ISSN) Khazaei, A ; Mohebbi, V ; Mosayyebi Behbahani, R ; Ramazani Saadat Abadi, A ; Sharif University of Technology
    Elsevier B.V  2018
    Abstract
    Chemical industries need to employ new process designs due to environmental policies and energy optimization because of the global energy challenge. Pervaporation has been introduced as a promising alternative for conventional processes such as distillation, known as energy intensive process, in chemical plants. In this work, the energy consumption of different processes for separation of toluene and i-octane (representatives of aromatics and aliphatic mixtures) has been evaluated, based on our previous laboratory pervaporation experiments using Polyvinyl alcohol/Graphene oxide mixed matrix membranes. Accordingly, hybrid distillation-pervaporation and cascade pervaporation systems have been... 

    Application of scheduling models for utility management of process plants and its extension to DG networks

    , Article 2008 1st International Conference on Infrastructure Systems and Services: Building Networks for a Brighter Future, INFRA 2008, Rotterdam, 10 November 2008 through 12 November 2008 ; 2008 ; 9781424468874 (ISBN) Behdani, B ; Pishvaie, M. R ; Sharif University of Technology
    2008
    Abstract
    Scheduling models are one of the main parts of computer-aided process design research in recent years. One of the novel applications of scheduling models is their usage for in-site utility management of a process plant. It is very common for huge process plants to provide their utility by themselves; therefore, they shall make decision on utility supply and demand simultaneously. This approach can be extended to other similar systems such as distributed generation networks. In fact, it is possible to consider a DG unit as an autonomous system which is responsible for its energy (heat and power) supply and demand. Of course, for achieving its reliability and dispatchability goals, it would... 

    Combined UV-C/H2O2-VUV processes for the treatment of an actual slaughterhouse wastewater

    , Article Journal of Environmental Science and Health - Part B Pesticides, Food Contaminants, and Agricultural Wastes ; Volume 52, Issue 5 , 2017 , Pages 314-325 ; 03601234 (ISSN) Vaezzadeh Naderi, K ; Bustillo Lecompte, C. F ; Mehrvar, M ; Abdekhodaie, M. J ; Sharif University of Technology
    Taylor and Francis Inc  2017
    Abstract
    In this study, a three-factor, three-level Box-Behnken design with response surface methodology were used to maximize the TOC removal and minimize the H2O2 residual in the effluent of the combined UV-C/H2O2-VUV system for the treatment of an actual slaughterhouse wastewater (SWW) collected from one of the meat processing plants in Ontario, Canada. The irradiation time and the initial concentrations of total organic carbon (TOCo) and hydrogen peroxide (H2O2o) were the three predictors, as independent variables, studied in the design of experiments. The multiple response approach was used to obtain desirability response surfaces at the optimum factor settings. Subsequently, the optimum...