Dissertations / Theses on the topic 'Mathematical Modeling and Industrial Mathematics'
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Uzel, Esra Örnek M. Arslan. "A mathematical modeling approach to energy cost saving in manufacturing plant/." [s.l.]: [s.n.], 2004. http://library.iyte.edu.tr/tezler/master/enerjimuh/t000265.pdf.
Full textNordle, Bjorn, and Marcus Johansson. "Analysis and mathematical modelling of industrial truck silencers." Thesis, Växjö University, School of Mathematics and Systems Engineering, 2007. http://urn.kb.se/resolve?urn=urn:nbn:se:vxu:diva-1808.
Full textThe currently low requirements on sound emissions for industrial trucks are expected to be raised in the near future. The company Kalmar Industries AB, which develop, produce and market industrial trucks, want to improve their truck silencers as a precaution to the future harder restrictions and also to improve their competitiveness. The sound emission produced by a vehicle depends on type and range of application it is designed for but the dominant part of the sound is usually produced by the engine and silencer.
A new measuring method is developed for studying sound emanating through the silencer system. The analysis of the measurement data establishes that the silencers are not working well. The simulations made with SIDLAB, which is a computer programme for calculating the propagation of sound in ducts, confirms that the silencers are inefficient and that they are simply too small.
A simulation which implements a parallel resonator in the main silencer shows that it is possible to make great improvements in reducing the noise from the truck as well as meeting requirements on space.
Mathematical modelling based on linearity and one-dimensional interaction between the silencer elementsis advantageous and gives very good results when understanding, analysing and simulating the silencer. The simulation tool SIDLAB works well and saves a lot of time by its fast modelling and easy interface.
Gannon, Terry. "Mathematical modelling of distillation columns with particular reference to industrial equipment." Thesis, Teesside University, 1985. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.351898.
Full textThomson, Stuart. "Mathematical modelling of elastoplasticity at high stress." Thesis, University of Oxford, 2017. http://ora.ox.ac.uk/objects/uuid:a7d565c6-abeb-4932-8c1e-aebc38da7584.
Full textSinangil, Mehmet Selcuk. "Modeling and control on an industrial polymerization process." Thesis, Georgia Institute of Technology, 1995. http://hdl.handle.net/1853/10150.
Full textO'Kiely, Doireann. "Mathematical models for the glass sheet redraw process." Thesis, University of Oxford, 2017. https://ora.ox.ac.uk/objects/uuid:3788de4d-8254-4fba-9cd0-4bec32409d1e.
Full textDu, Plessis J. Prieur. "Modelling and industrial application of flow through two-dimensional porous media." Thesis, Stellenbosch : Stellenbosch University, 2002. http://hdl.handle.net/10019.1/52941.
Full textENGLISH ABSTRACT: A Representative Unit Cell (RUC) model for flow through two-dimensional porous media is presented and applied to two industrial related problems. The first application is to that of cross-flow in tube banks. Both staggered and square (inline) configurations are investigated and the model results are compared to experimental data. The second application is to flow through a stack in a timber-drying kiln. The RUC model is applied to the anisotropic timber stack ends and the centre part is modelled with a standard duct flow solution. The results of the models applied to a timber stack are compared to experimental data obtained from model tests undertaken in a wind tunnel. The results of the RUC and duct flow models are found to be in excellent agreement with the data of the experimental models. These models may be used to optimize kiln designs.
AFRIKAANSE OPSOMMING: 'n Verteenwoordigende Eenheid Sel (VES) model vir vloei deur twee-dimensionele poreuse media word weergegee en toegepas op twee industriële toepassings. Die eerste toepassing is op dwarsvloei deur banke van buise. Beide gestapelde en inlyn konfigurasies word ondersoek waarvan die model resulte met eksperimentele data vergelyk word. Die tweede toepassing is op vloei deur 'n stapel in 'n hout-droogoond. Die VES model word toegepas op die anisotropiese ente van houtstapels en die middelste seksie word gemodelleer deur 'n standaard kanaalvloei oplossing. Die resultate van die modelle toegepas op n 'houtstapel word vergelyk met eksperimentele data verkry uit model toetse wat in 'n wind-tonnel uitgevoer is. Die VES en kanaalvloei modelle se resultate stem uitstekend ooreen met die data van die eksperimentele modelle. Hierdie modelle kan gebruik word om die ontwerp van droogoonde te optimeer.
Murat, Ekrem Alper. "An allocation based modeling and solution framework for location problems with dense demand /." Thesis, McGill University, 2005. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=102685.
Full textOur approach has two fundamental characteristics: Demand representation in the form of continuous density functions and allocation decisions in the form of service regions. Accordingly, our framework is based on continuous optimization models and solution methods. On a plane, service regions (allocation decisions) assume different shapes depending on the metric chosen. Hence, this thesis presents separate approaches for two-dimensional Euclidean-metric and Manhattan-metric based distance measures. Further, we can classify the solution approaches of this thesis as constructive and improvement-based procedures. We show that constructive solution approach, namely the shooting algorithm, is an efficient procedure for solving both the single dimensional n-facility and planar 2-facility problems. While constructive solution approach is analogous for both metric cases, improvement approach differs due to the shapes of the service regions. In the Euclidean-metric case, a pair of service regions is separated by a straight line, however, in the Manhattan metric, separation takes place in the shape of three (at most) line segments. For planar 2-facility Euclidean-metric problems, we show that shape preserving transformations (rotation and translation) of a line allows us to design improvement-based solution approaches. Furthermore, we extend this shape preserving transformation concept to n-facility case via vertex-iteration based improvement approach and design first-order and second-order solution methods. In the case of planar 2-facility Manhattan-metric problems, we adopt translation as the shape-preserving transformation for each line segment and develop an improvement-based solution approach. For n-facility case, we provide a hybrid algorithm. Lastly, we provide results of a computational study and complexity results of our vertex-based algorithm.
Charnsirisakskul, Kasarin. "Demand fulfillment flexibility in capacitated production planning." Diss., Georgia Institute of Technology, 2003. http://hdl.handle.net/1853/25667.
Full textBailey, Robert Reid. "Input-output modeling of material flows in industry." Diss., Georgia Institute of Technology, 2000. http://hdl.handle.net/1853/19104.
Full textLevakin, M., and A. Doroshenko. "About real-mathematical model of electrical systems specific industrial energy consumers." Thesis, Sumy State University, 2016. http://essuir.sumdu.edu.ua/handle/123456789/46948.
Full textYang, Xuedong. "Modeling and control of two-axis belt-drive gantry robots." Diss., Georgia Institute of Technology, 2000. http://hdl.handle.net/1853/13061.
Full textLan, Tian. "MATHEMATICAL MODELING FOR PLATFORM-BASED PRODUCT CONFIGURATION CONSIDERING TOTAL LIFE-CYCLE SUSTAINABILITY." UKnowledge, 2015. http://uknowledge.uky.edu/me_etds/56.
Full textShi, Zhenzhen. "A MARKOV DECISION PROCESS EMBEDDED WITH PREDICTIVE MODELING: A MODELING APPROACH FROM SYSTEM DYNAMICS MATHEMATICAL MODELS, AGENT-BASED MODELS TO A CLINICAL DECISION MAKING." Diss., Kansas State University, 2015. http://hdl.handle.net/2097/20578.
Full textDepartment of Industrial & Manufacturing Systems Engineering
David H. Ben-Arieh
Chih-Hang Wu
Patients who suffer from sepsis or septic shock are of great concern in the healthcare system. Recent data indicate that more than 900,000 severe sepsis or septic shock cases developed in the United States with mortality rates between 20% and 80%. In the United States alone, almost $17 billion is spent each year for the treatment of patients with sepsis. Clinical trials of treatments for sepsis have been extensively studied in the last 30 years, but there is no general agreement of the effectiveness of the proposed treatments for sepsis. Therefore, it is necessary to find accurate and effective tools that can help physicians predict the progression of disease in a patient-specific way, and then provide physicians recommendation on the treatment of sepsis to lower risk for patients dying from sepsis. The goal of this research is to develop a risk assessment tool and a risk management tool for sepsis. In order to achieve this goal, two system dynamic mathematical models (SDMMs) are initially developed to predict dynamic patterns of sepsis progression in innate immunity and adaptive immunity. The two SDMMs are able to identify key indicators and key processes of inflammatory responses to an infection, and a sepsis progression. Second, an integrated-mathematical-multi-agent-based model (IMMABM) is developed to capture the stochastic nature embedded in the development of inflammatory responses to a sepsis. Unlike existing agent-based models, this agent-based model is enhanced by incorporating developed SDMMs and extensive experimental data. With the risk assessment tools, a Markov decision process (MDP) is proposed, as a risk management tool, to apply to clinical decision-makings on sepsis. With extensive computational studies, the major contributions of this research are to firstly develop risk assessment tools to identify the risk of sepsis development during the immune system responding to an infection, and secondly propose a decision-making framework to manage the risk of infected individuals dying from sepsis. The methodology and modeling framework used in this dissertation can be expanded to other disease situations and treatment applications, and have a broad impact to the research area related to computational modeling, biology, medical decision-making, and industrial engineering.
Singh, Manjeet. "Mathematical Models, Heuristics and Algorithms for Efficient Analysis and Performance Evaluation of Job Shop Scheduling Systems Using Max-Plus Algebraic Techniques." Ohio University / OhioLINK, 2013. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1386087325.
Full textFiore, Ian Koscialkowski. "Modelagem matemática de um reator industrial de alquilação de butenos utilizando HF como catalisador." Universidade de São Paulo, 2012. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-07062013-112915/.
Full textAlkylation is the process which light hydrocarbons (like butenes and iso-bute) are transformed into heavier hydrocarbons, called alkylate. The alkylate demand as a gasoline component has been growing since the middle 90s, mostly due to more severe quality requirements for gasoline. This work proposes a mathematical model that accounts for the main chemical reactions for a HF Alkylation Unit. The alkylate yield and quality, described by its composition, are also represented as well. This model as based on mass and energy balances for the alkylation reactor, using the most accepted kinetic mechanism available at literature. The model constants were estimated by non-linear regression with available data from literature. The model validation was performed comparing the simulation results with data collected at an industrial Alkylation unit at Cubatão, Brazil, without further parameter adjustment. The results show a good model response for the consumption of reagents and alky yield. The model, however, underpredicts the yield of heavier fractions.
Hu, Xiaohong. "Probability modeling of industrial situations using transform techniques." Ohio : Ohio University, 1995. http://www.ohiolink.edu/etd/view.cgi?ohiou1179433956.
Full textCerminara, Matteo. "Modeling dispersed gas-particle turbulence in volcanic ash plumes." Doctoral thesis, Scuola Normale Superiore, 2016. http://hdl.handle.net/11384/86206.
Full textKamat, Kuldip U. "Minimizing total tardiness and crew size in labor intensive cells using mathematical models." Ohio : Ohio University, 2007. http://www.ohiolink.edu/etd/view.cgi?ohiou1181108441.
Full textStrelnikova, E., and E. Serikova. "Critical changing groundwater level in Ukrainian industrial cities." Thesis, Sumy State University, 2015. http://essuir.sumdu.edu.ua/handle/123456789/40863.
Full textHarihara, Ramachandra Sharma. "Modeling of Scheduling Algorithms with Alternative Process Plans in an Optimization Programming Language." Ohio University / OhioLINK, 2004. http://www.ohiolink.edu/etd/view.cgi?ohiou1108045192.
Full textHaines, Alastair Neil. "The mathematical modelling of industrial electrolytic reactions." Thesis, Teesside University, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.235728.
Full textSartor, Rafael Busato. "Modelagem, simulação e otimização de uma unidade industrial de extração de óleos essenciais por arraste a vapor." reponame:Biblioteca Digital de Teses e Dissertações da UFRGS, 2009. http://hdl.handle.net/10183/21924.
Full textThis work has as objective the development of a mathematical model of essential oils extraction by steam distillation and the optimization of this process on an industrial scale. We used experimental data obtained from rosemary and citronella in an industrial steam distillation unit. The model consists a system of partial differential equations, which represent the one-dimensional mass balance in steam and solid phases. To solve the developed model, we used the method of lines with the finite differences technique to discretize the spatial coordinate and its derivatives, resulting in a system of ordinary differential equations implemented in the EMSO simulator. The model parameters were estimated by the method of flexible polyhedra, using two experimental runs and a third experimental run to test the model. The model fitted to the experimental data industry, resulting, for two environmental and geographical conditions of rosemary, in mass transfer coefficients of 8,64 x 10 -4 s -1 and 9,10 x 10 -4 s -1, and the equilibrium constant of 2,72 x 10 -4 m3/kg and 1,07 x 10 -2m3/kg. For citronella, the obtained mass transfer coefficient of 8,29 x 10 -4 s -1 and 1,23 x 10 -3 s -1 and equilibrium constant of 1,25 x 10 -2 m3/kg and 1,52 x 10 -3 m3/kg. It was also proposed an optimization problem to determine the optimum extraction time and number of batches per day. The optimization results indicate that the process can reduce the extraction time, allowing other extractions are performed each day, maximizing the essential oil volume extracted in the day.
Clark, John Malcolm. "Mathematical modelling of G.F.M. forging." Thesis, University of Sheffield, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.266125.
Full textMese, Emre M. "Cell Loading and Family Scheduling for Jobs with Individual Due Dates in a Shoe Manufacturing Company." Ohio University / OhioLINK, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1248975462.
Full textPerera, Sattambiralalage Anura Lalindra. "Mathematical modelling of two-phase for industrial applications." Thesis, Imperial College London, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.267699.
Full textOikawa, Eduardo Hiroshi. "Avaliação de um sistema industrial de resfriamento de água." Universidade de São Paulo, 2012. http://www.teses.usp.br/teses/disponiveis/3/3137/tde-16112012-114140/.
Full textIn the present work, the performance of a system composed of a cooling tower integrated in butadiene hydrogenation plant was studied. An experimental investigation was made to characterize the cooling towers based on a phenomenological model and in real process conditions. The hydrogenation process was configured on a process simulator and design specifications were considered as base case. A cooling tower module was developed and integrated to the process simulator. The interaction of the cooling tower system and the plant operation was investigated.
DI, BENEDETTO GIACOMO. "Data mining and mathematical modelling on diabetes." Doctoral thesis, Politecnico di Torino, 2013. http://hdl.handle.net/11583/2513770.
Full textHuang, Jing. "Resource Management and Sourcing Strategies in Supply Chain Coordination under an Uncertain Environment." Ohio University / OhioLINK, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1354756891.
Full textHashim, Syed Fuad Bin Saiyid. "Mathematical modelling the two-compartment mill and classification /." [St. Lucia, Qld.], 2004. http://www.library.uq.edu.au/pdfserve.php?image=thesisabs/absthe17867.pdf.
Full textZamanipour, Mehdi, and Mehdi Zamanipour. "A Unified Decision Framework for Multi-Modal Traffic Signal Control Optimization in a Connected Vehicle Environment." Diss., The University of Arizona, 2016. http://hdl.handle.net/10150/620993.
Full textPanchal, Jitesh H. "A framework for simulation-based integrated design of multiscale products and design processes." Diss., Available online, Georgia Institute of Technology, 2005, 2005. http://etd.gatech.edu/theses/available/etd-11232005-112626/.
Full textEastman, Chuck, Committee Member ; Paredis, Chris, Committee Co-Chair ; Allen, Janet, Committee Member ; Rosen, David, Committee Member ; Tsui, Kwok, Committee Member ; McDowell, David, Committee Member ; Mistree, Farrokh, Committee Chair. Includes bibliographical references.
Imaev, Aleksey A. "Hierarchical Modeling of Manufacturing Systems Using Max-Plus Algebra." Ohio University / OhioLINK, 2009. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1257871858.
Full textPierantozzi, Mariano. "Mathematical modeling for Thermodynamics: Thermophysical Properties and Equation of State." Doctoral thesis, Università Politecnica delle Marche, 2015. http://hdl.handle.net/11566/242931.
Full textAbstract In the modern multicultural and multidisciplinary society, always adopting more and more wider prospective than before. In this thesis, we try to adopt a multidisciplinary method, which involves Mathematics, Physics, but also Chemistry, Statistics, and in general the scientific engineering. The aspects explained are thermo physical properties, and Equations of State (EOS) of gases. Regarding thermo physical properties have been analysed Surface Tension, Thermal Conductivity, Viscosity, and the second virial coefficient. On this arguments, the work had been subdivided between the gathering of experimental data, the analysing of data with statistical techniques transforming them to more reliable data than row. The second step was to collect the equations of literature. Then we went ahead studying the sensibility of data to find out which physical properties could have bigger impact to property examined. At the end, we looked for an equation that could represent experimental data in a better way. We always preferred the scaled equations that respect chemical and physical aspects, to the empirical ones. Comparing our results with better equations in literature, our results are always better, in fact all of the have been published in the best international journals on this subject. A separate discussion is that of EOS. Analyzing the previous literature, the first thing that came to our minds was that to find the best possible equation is impossible. Or as Martin wrote copying words of the famous fables Snow White: “Mirror mirror on the wall, who is the fairest of them all?”. We choose to modify The Carnahan-Starling-De Santis (CSD) equation of state, a parametrich equation with good results in the calculation of Vapor Liquid Equilibrium. Due to multi objective minimization techniques the performance of CSD has been improved. These are the principals aspect brought to light in this research, which apart from the results, with good results has opened to me the world of research.
Wilson, Darin C. "Comparison of Alternative Manufacturing Systems for Global Supply ChainBusiness Strategies in Blood Sugar Monitoring Industry." Ohio University / OhioLINK, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1446035356.
Full textEshraghi, Alireza. "Prediction of exposure to industrial solvents." Thesis, London South Bank University, 1999. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.312998.
Full textShoemaker, Katherine L. Shoemaker. "The Mathematical Modeling of Magnetostriction." Bowling Green State University / OhioLINK, 2018. http://rave.ohiolink.edu/etdc/view?acc_num=bgsu1522694644858063.
Full textFarrell, Troy W. "The mathematical modelling of primary alkaline battery cathodes." Thesis, Queensland University of Technology, 1998.
Find full textFerreira, Marcelo. "Problemas de programação de produção em indústrias de embalagens de papelão ondulado." Universidade Estadual Paulista (UNESP), 2018. http://hdl.handle.net/11449/155914.
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Nessa tese abordamos dois problemas reais identificados no processo produtivo de indústrias de embalagens de papelão ondulado, que denotaremos por Problema de Minimização de Trocas de Gramaturas e Rolos Corrugadores (PMTGRC) e Problema da Alocação de Bobinas no Corrugador (PABC). Ambos os problemas ocorrem no corrugador, máquina multiestágio que produz as chapas de papelão ondulado. O PMTGRC surge da necessidade de minimizar trocas de gramaturas e rolos corrugadores durante o processo de produção dos boletins, uma vez que cada boletim traz as gramaturas específicas das camadas da chapa, além do tipo de onda empregada no(s) miolos(s). O sequenciamento dos boletins impacta na quantidade de mudanças de gramaturas nos porta-bobinas e se haverátrocaderoloscorrugadoresparadoisboletinssubsequentes. Astrocasdegramaturas impactam em custos de transporte de bobinas e as trocas de rolos corrugadores impactam em perda de produtividade. Para o PMTGRC propomos quatro modelos inéditos de programação inteira capazes de integrar essas duas considerações. O PABC integra várias considerações relacionadas à alocação das bobinas no corrugador, como por exemplo, a minimização das sobras não aproveitáveis e das quantidades de consumos parciais, fatores que influenciam diretamente nos custos de produção. Um modelo linear inteiro misto inédito é proposto, determinando quais bobinas serão utilizadas em cada porta-bobinas. Além disso, propomos uma estratégia de sequenciamento das bobinas em cada porta-bobina, evitando paragens no corrugador. Uma série de testes computacionais utilizando instâncias geradas com base em dados reais foram realizados. Os resultados indicam que os modelos foram eficientes em tratar os problemas propostos.
In this thesis we approached two real problems identified over the productive process of corrugated cardboard industries, which we will denote as the Minimization of Converting Weights and Corrugators Problem (MCWCP) and the Corrugators Coil Allocation Problem (CCAP). Both of these problems happen in the corrugators, a multistage machine which produces corrugated cardboard. The MCWCP appears from the necessity to minimize changes of weight and corrugator rolls during the production process of the bulletins, since each one brings the specific layers’s weight of the sheets, besides the kind of wave put in the middle. The sequence of bulletins impact in the number of weight changes in the coil holders and if there will be corrugating rollers’s exchange for two following bulletins. The gramature’s exchanges impact in the costs of transportation and the corrugating rollers exchange causes lost in the productivity. We propose four whole programming models capable of integrating both considerations. The CCAP integrates many considerations related to the coils’s allocation on the corrugators, for example, the minimization of the non-usable leftovers and the amount of partial consumption, factors which influence directly on the production’s costs. A whole new mist linear model is proposed, determined which coil on the corrugators are going to be used in each coil holder. Besides this, we propose a sequel strategy for the coils in each coil holder, avoiding stops on the corrugators. A series of computation tests using instances created based on real data were made. The results indicate that the models were efficient in solving the problems.
Farias, Everton da Silveira. "Modelagem para o projeto de rede da cadeia de suprimentos de uma indústria de multi-commodity." reponame:Biblioteca Digital de Teses e Dissertações da UFRGS, 2011. http://hdl.handle.net/10183/31776.
Full textWe present a mathematical modeling of the Supply Chain Network Design (SCND) for a company responsible for producing and distributing commodities. Investment in a new plant requires that the company has reconfigured its logistics project. The development of mathematical formulations is based on the work of Jayaraman and Pirkul (2001). Were performed three (3) mathematical formulations for different approaches to solving the logistics project. Computational implementations were done in CPLEX© Optimization Academic Research Studio version 12.2. Computational experiments were developed through scenarios that sought to represent problems of the real dimensions. Still in the experimentation fase were performed sensitivity analysis of models. A study to identify market demands and transportation costs was made, so the models could be applied in the case study data from actual demand and costs. For carrying out the actual instances were selected 2 (two) different approaches: Single-source-based and Arc. Different market shares were set to build new scenarios and actual instances have been implemented within limits satisfactory computational time. The results for each scenario were compared and analyzed for solving the proposed problem. The thesis contributes to modeling area of supply chain models that provide satisfactory results for decision making in this phase of the project's logistics industry theme of this research.
Correia, Sara Alexandra Chanoca. "Development of improved mathematical models for the design and control of gas-fired furnaces." Thesis, University of South Wales, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.369080.
Full textBeen, Amy L., and Amy L. Been. "Teacher Views of Mathematical Modeling." Thesis, The University of Arizona, 2016. http://hdl.handle.net/10150/621172.
Full textWu, Gianna. "Mathematical Modeling of Type 1 Diabetes." Scholarship @ Claremont, 2019. https://scholarship.claremont.edu/hmc_theses/231.
Full textSousa, Juliana Rabelo de. "Produção de lipopeptídeos e glicolipídeos a partir da bioconversão do co-produto da produção do biodiesel." Universidade Federal de São Carlos, 2012. https://repositorio.ufscar.br/handle/ufscar/3920.
Full textUniversidade Federal de Sao Carlos
Biosurfactants are a surface-active chemical compounds synthesized by microorganisms. These compounds have many advantages when compared to their chemically synthesized counterparts as specific action, low toxicity, higher biodegradability, effectiveness at extreme temperatures, pH and strength ionic. They appear as promising candidates to replace chemical surfactants produced from petrochemicals. The use of renewable and low cost substrates such as agro based industrial wastes is one of the attractive strategies for economical large scale biosurfactants production. In this work, it was evaluated glycerol, a co-product of biodiesel production, as carbon source for biosurfactant production. Two microorganisms, Pseudomonas aeruginosa MSCIC02 and Bacillus subtilis LAMI009, both isolated from environmental sources, were used thorough this work. In the first part of the work experiments were carried out in shake flasks using P. aeruginosa. The results showed that the increase in nitrogen source (sodium nitrate) and the decrease in the carbon source (glycerin) favored rhamnolipids production. In the range studied, the maximum biosurfactant concentration obtained was 2.3 g⋅L-1 (C/N ratio 12). The effect of nitrogen concentration on the biosynthesis of rhamnolipids and pH behavior as a function of the nitrate concentration in the cultures indicated that this strain probably carried a denitrification route favoring the production of rhamnolipids. Experimental runs carried out in bioreactor indicated that the integrated process of production and separation/concentration by fractionation in bubble column equipment caused many operation problems, such as the drag cell, and reducing the concentration of rhamnolipids to 0.4 g⋅L-1in the reaction medium. The kinetics of product formation was evaluated by two models. The Luedeking-Piret model was not able to represent the process. The model proposed by MERCIER et. al. (1992) could adequately describe the rhamnolipids production from P. aeruginosa strain. Emulsifying capacity of the cell-free culture medium was assessed by the emulsification index (EI24). The biosurfactant produced was able to emulsify vegetable oils as well as mineral oils. EI24 greater than 55% was reached. In the second part of the work experimental data from Bacillus subtilis LAMI009 cultivated in shake flasks showed that the growth of this strain was dependent on iv the medium supplementation with yeast extract. A change in culture medium was implemented in order to reduce the length of the lag phase. The use of inorganic nitrogen sources showed that both ammonium nitrate and ammonium sulphate reached similar values of surfactin concentration and volumetric productivity. It was obtained 35 mg⋅L-1 and 6.1 mg⋅L-1⋅h-1, respectively. Surface tension of the cell-free culture medium was similar for both nitrogen sources. The minimal value obtained was 29.7 mN⋅m-1. Sodium nitrate was found to be an adequate nitrogen source for cell growth. However, in these assays low productivity and low surface tension reduction were obtained when compared to the other nitrogen sources evaluated. The supplementation of the culture medium with yeast extract improves the surfactin concentration (60.0 mg⋅L-1) and volumetric productivity (5.2 mg⋅L-1⋅h-1). In this assay the surface tension reached 28.1 mN⋅m-1. The inoculum size had a great influence on cell growth and production of surfactin. When 2% (v/v) of inoculum was used the surfactin concentration and volumetric productivity obtained were 148.2 mg⋅L-1 e 14.22 mg⋅L-1⋅h-1, respectively. The search for genes responsible for production of lipopeptides surfactin and iturine indicated the presence of the genes lpa14 and ituD in B. subtilis LAMI009 genome. Analysis of the chromatography profile of methanol extracts of the lipopeptides from culture medium with ammonium nitrate and sodium nitrate as nitrogen source showed characteristic peaks of the surfactin and iturine. Thereby, it is believed that this strain is a co-producer of both surfactin and iturine. Emulsifying capacity of the cell-free culture medium showed higher stability with the media that employed ammonium nitrate and sodium nitrate as nitrogen source. It was obtained EI24 of 65% with n-hexadecane and 45% with kerosene. The acid precipitation of biosurfactant from the cell-free culture medium showed that this prepurification step promoted an increase in the emulsifying capacity of the mixture of lipopeptides synthesized by B. subtilis LAMI009. The aqueous solution of crude biosurfactant was able to emulsify naphthenic oils, vegetable oils, and an aromatic hydrocarbon. Values of EI24 greater than 65% were obtained. Emulsions formed with naphthenic oils were more stable according to droplet-size distribution. The smaller the size of droplets, the more stable was the emulsion.
Biossurfactantes são compostos químicos tensoativos sintetizados por microrganismos. Estes compostos possuem muitas vantagens quando comparados com seus equivalentes sintetizados quimicamente como ação específica, baixa toxicidade, alta biodegradabilidade, efetividade em condições extremas de temperatura, pH e força iônica. Apresentam-se como substitutos promissores aos surfactantes químicos derivados da indústria do petróleo. A utilização de substratos renováveis e de baixo custo, como os resíduos agroindustriais, consiste em um dos fatores mais importantes para a viabilização econômica da produção destes compostos em escala industrial. Neste trabalho avaliou-se o uso da glicerina, um coproduto da produção de biodiesel, como fonte de carbono para produção de biossurfactante. Dois microrganismos, Pseudomonas aeruginosa MSIC02 e Bacillus subtilis LAMI009, ambos isolados a partir de amostras ambientais, foram empregados neste trabalho. Na primeira parte do trabalho experimentos realizados em frascos agitados com a P. aeruginosa mostraram que o aumento da produtividade de ramnolipídeos foi favorecido pelo aumento da concentração da fonte de nitrogênio (nitrato de sódio) e pela redução da concentração da fonte de carbono (glicerina). Na faixa estudada a concentração máxima de biossurfactante obtida foi de 2,3 g⋅L-1 (razão C/N de 12). O efeito da concentração de nitrogênio sobre a biossíntese de ramnolipídeos e o comportamento do pH em função da concentração de nitrato durante os cultivos indicou que esta cepa possivelmente realizou uma rota denitrificante favorecendo a produção de ramnolipídeos. Os cultivos realizados em biorreator indicaram que o processo de produção integrado a extração/concentração por fracionamento em coluna de bolhas acarretou diversos problemas operacionais, como o arraste de células, e a redução da concentração de ramnolipídeos no meio reacional para 0,4 g⋅L-1. Foram avaliados dois modelos cinéticos de formação de produto para os ensaios realizados. O modelo de Luedeking-Piret não apresentou boa representatividade do processo. O modelo proposto por MERCIER et al. (1992) mostrou-se mais adequado para representar a produção de ramnolipídeos pela cepa estudada. A avaliação da capacidade emulsificante do meio de cultivo livre de células mostrou que o biossurfactante produzido pela P. aeruginosa teve um desempenho eficiente, sendo capaz de emulsificar óleos de origem vegetal e mineral e atingir índice de emulsificação (IE24) maior que 55 %. Na segunda parte do trabalho, cultivos realizados em frascos agitados para avaliação da produção de biossurfactantes lipopeptídeos por B. subtilis LAMI009 indicaram que o crescimento desta cepa foi dependente da suplementação do meio com extrato de levedura. Uma adaptação ao meio de fermentação foi necessária para eliminar a extensa fase lag durante o processo fermentativo. A utilização de fontes de nitrogênio inorgânicas mostrou que tanto o nitrato de amônio quanto o sulfato de amônio apresentaram valores de concentração de surfactina e produtividade volumétrica da ordem de 35 mg⋅L-1 e 6,1 mg⋅L-1⋅h-1, respectivamente. A tensão superficial do meio de cultivo livre de células também foi semelhante para ambas fontes de nitrogênio, cujo valor mínimo foi 29,7 mN⋅m-1. O nitrato de sódio foi fonte de nitrogênio adequada para o crescimento celular, entretanto apresentou baixa produtividade quando comparado com as demais fontes de nitrogênio avaliadas. Com a suplementação do meio de cultivo com extrato de levedura ii obteve-se maior concentração de surfactina (60,0 mg⋅L-1) e produtividade volumétrica (5,2 mg⋅L-1⋅h-1) e menor tensão superficial (28,1 mN⋅m-1) relativamente ao meio de cultivo contendo fonte de nitrogênio inorgânica. O tamanho do inóculo exerceu grande influência sobre a concentração de surfactina e a produtividade volumétrica. Quando se utilizou 2% (v/v) de inóculo a concentração de surfactina e a produtividade volumétrica alcançaram valores de 148,2 mg⋅L-1 e 14,22 mg⋅L-1⋅h-1, respectivamente. A pesquisa de genes responsáveis pela produção dos lipopeptídeos surfactina e iturina indicou a presença dos genes lpa14 e ituD no genoma da linhagem B. subtilis LAMI009. A avaliação do perfil cromatográfico dos extratos metanólicos de lipopeptídeos obtidos a partir dos cultivos com as fontes de nitrogênio nitrato de amônio e nitrato de sódio apresentou picos característicos de outro lipopeptídeo além da surfactina, a iturina,. Portanto, acredita-se que esta linhagem é uma co-produtora de surfactina e iturina. A capacidade emulsificante do meio de cultivo livre de células apresentou maior estabilidade com os cultivos com nitrato de amônio e nitrato de sódio, obtendo-se IE24 de 65 % com n-hexadecano e 45 % com querosene. A separação do biossurfactante por precipitação ácida a partir do meio de cultivo livre de células mostrou que esta etapa de pré-purificação promoveu um aumento da capacidade emulsificante da mistura de lipopeptídeos sintetizada por B. subtilis LAMI009. A solução aquosa do biossurfactante bruto foi capaz de emulsificar óleos naftênicos, óleos vegetais e um hidrocarboneto aromático, apresentando IE24 maiores que 65 % com os óleos avaliados. As emulsões formadas com óleos naftênicos, utilizados como base para lubrificantes, foram mais estáveis. Quanto menor o tamanho das gotas mais estável foi a emulsão formada.
Celikbilek, Can. "Alternative Supply Chain Design Strategies with Operational Considerations: A Case Study for a Windows Manufacturing Company." Ohio University / OhioLINK, 2016. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1458302171.
Full textРосохата, Анна Сергіївна, Анна Сергеевна Росохатая, and Anna Serhiivna Rosokhata. "Застосування методів моделювання у прогнозуванні напрямів інноваційного розвитку промислових підприємств." Thesis, Sp. z o.o. «Nauka i studia», 2014. http://essuir.sumdu.edu.ua/handle/123456789/38272.
Full textРабота раскрывает проблематику применения методов экономико-математического моделирования в прогнозировании направлений инновационного развития промышленных предприятий. Представлены особенности осуществления данного вида формализованного прогнозирования на основе количественных данных.
The work reveals the problematic of economic and mathematical modeling methods' application in forecasting of innovative development directions at industrial enterprises. The features of the implementation of this formalized forecasting based on quantitative data has been presented.
Росохата, Анна Сергіївна, Анна Сергеевна Росохатая, and Anna Serhiivna Rosokhata. "Класифікація методів економіко-математичного моделювання у прогнозуванні інноваційного розвитку промислових підприємств." Thesis, «Бял ГРАД-БГ» ООД, 2014. http://essuir.sumdu.edu.ua/handle/123456789/38279.
Full textАвтором представлены основные методы экономико-математического моделирования в системе прогнозирования инновационного развития промышленных предприятий. Предложено распределение методов по классификационным признакам. Обоснована необходимость адаптации формализованных методов в реальных экономических условиях современности, что выдвигают рыночная среда и принципы стратегического маркетингового управления.
The author presented the main methods of economic-mathematical modeling in the forecasting's system of industrial enterprises innovative development. Methods' distribution by classification features has been proposed. The necessity of adapting formal methods to real economic conditions of our time has been substantiated. This makes the market environment and strategic marketing management principles.
Weatherwax, John Lloyd 1973. "Mathematical modeling of shock induced martensitic phase transitions." Thesis, Massachusetts Institute of Technology, 2001. http://hdl.handle.net/1721.1/8223.
Full textIncludes bibliographical references (p. 123-129).
Recently Bruno and Vaynblat introduced a new mathematical model to describe shock induced martensitic phase transitions. This model is much simpler than prior ones -- requiring, essentially, no quantities that cannot be measured directly. Nevertheless, its predictions are in very good agreement with the experimental results. In the calculations that Bruno and Vaynblat did to match their model against experiments, they simplified the dynamics - replacing rarefaction waves by "rarefaction discontinuities". In this thesis we implement the Bruno-Vaynblat model without any such simplifications. In the process of doing this, a new numerical method for nonlinear hyperbolic conservation laws with phase transitions is developed. Furthermore, in order to improve the quantitative agreement with experiments, several extensions of the Bruno-Vaynblat model are introduced and studied. These include the addition of dissipative effects, and the introduction of a modification to the equation of state (for the Austenite phase) near the critical transition pressure.
by John Lloyd Weatherwax.
Ph.D.
Erenay, Bulent. "Concurrent Supply Chain Network & Manufacturing Systems Design Under Uncertain Parameters." Ohio University / OhioLINK, 2016. http://rave.ohiolink.edu/etdc/view?acc_num=ohiou1459206318.
Full textKeller, Peter. "Mathematical modeling of molecular motors." Universität Potsdam, 2013. http://opus.kobv.de/ubp/volltexte/2013/6304/.
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