Dissertations / Theses on the topic 'Production Process'
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Saliba, Ninos. "Standardization of a production process." Thesis, Mälardalens högskola, Akademin för innovation, design och teknik, 2018. http://urn.kb.se/resolve?urn=urn:nbn:se:mdh:diva-39865.
Full textLöfroth, Jaime, and Samuel Wiklund. "A Multivariate Process Analysis on a Paper Production Process." Thesis, Umeå universitet, Institutionen för matematik och matematisk statistik, 2018. http://urn.kb.se/resolve?urn=urn:nbn:se:umu:diva-149283.
Full textEn stor utmaning när det gäller att hantera storskaliga industriprocesser, som i pappers- och massaindustrin, är att minska tiden för driftstopp och reducera källor till varia- tioner i produktkvalitén till ett minimum, och samtidigt vara kostnadseffektiv. För att uppnå detta är det viktigt att förstå processvariablernas komplexa natur och att kvantifiera orsakssambanden mellan dem och produktkvaliteten tillsammans med pro- duktionsmängden. Pappers- och massasindustrin består huvudsakligen av kemiska pro- cesser och den relativt låga kostnaden för sensorer idag möjliggör insamling av stora mängder data, både variabler och observationer inom frekventa tidsintervall. Med des- sa datamängder får man ofta problem med multikollinearitet, vilket kräver effektiva multivariata statistiska verktyg för att extrahera användbara insikter bland bruset. Ett mål i denna multivariata situation är att bryta igenom bruset och hitta en relativt liten delmängd variabler som är viktiga, det vill säga variabel selektion. Syftet med denna masteruppsats är att hjälpa SCA Obbola, en stor pappersprodu- cent som har haft ett varierat produktionsutfall, att komma fram till slutsatser som kan hjälpa dem att säkerställa en långsiktig hög produktionskvantitet och kvalitet. Vi tillämpar olika metoder för variabel selektion, som har visat sig framgångsrika i lit- teraturen. Resultaten av arbetet är av blandad framgång, men vi lyckas hitta både variabler som SCA Obbola vet påverkar specifika responser, men även variabler som de tycker är intressanta för vidare utredning.
Chew, Ryan W. (Ryan Wayne). "Process improvements during production ramp-up." Thesis, Massachusetts Institute of Technology, 2007. http://hdl.handle.net/1721.1/39589.
Full textIncludes bibliographical references (p. 62-63).
Raytheon Company is currently ramping up production radars for a fighter aircraft. This product is doubling production in the next year to meet customer demand; however, the program has not been able to meet the current demand schedule for the radar. In addition, the cost of producing this radar is over the budgeted amount. Management is pushing cost and cycle time reductions on every piece of the radar, a task the team is diligently working to accomplish. The main focus of this project is one sub-assembly of the AESA radar system, the "coldwall", a heat sink that also provides the base structure by which all of the radar sensing equipment is connect to. The coldwall also acts as a heat sink, reducing the internal temperature of the radar assembly, thereby improving the fidelity of the radio frequency signal and longevity of the system itself. Currently, the cycle time to manufacture the coldwall is on average twice the planned cycle time and the cost is three times the budgeted amount. This thesis provides a case in which a process improvement investigation takes place under tight budgetary and time constraints in ramp-up mode.
(cont.) The goal of this thesis is to develop a case for accurate and complete data collection to help future process improvement decisions. The act of focusing this investigation was cumbersome due to the lack of data available on the process. In addition, the case study shows a situation where proactive issue resolution and active waste elimination could alleviate the stress incurred by cost over runs and delayed product shipments.
by Ryan W. Chew.
S.M.
M.B.A.
Ballot, Francis. "Bacterial production of antimicrobial biosurfactants." Thesis, Stellenbosch : University of Stellenbosch, 2009. http://hdl.handle.net/10019.1/2250.
Full textSurfactants are compounds that reduce interfacial surface tension, resulting in detergency, emulsifying, foaming and dispersing properties. Surfactants produced via biochemical processes (biosurfactants) form a niche market with their low toxicity, biodegradability and high specificity attributes. Biosurfactants have recently received considerable attention owing to their potential as biomedical molecules. In this study a knowledge base was established for the development of a process which produces biosurfactants for use as antimicrobial agents. Specifically, rhamnolipid biosurfactants were produced from Pseudomonas aeruginosa and tested for antimicrobial activity against target organisms. Accurate and reproducible analyses for the quantification of rhamnolipids and antimicrobial activity were developed. The amount of rhamnolipid was determined indirectly by measuring the rhamnose concentration. A novel HPLC method as well as an orcinol colorimetric method were developed for rhamnose measurement. In order to obtain accuracy with the orcinol method it was found that samples must be extracted at least three times prior to the analysis. An examination of literature on rhamnolipid production showed that many studies used colorimetric methods without extraction. Antibacterial activity was quantified by zone clearing around wells of supernatant in soft agar containing the target organism Mycobacterium aurum. This target organism is especially important in a South African context, since it is used to indicate possible susceptibility of tuberculosis to antibiotics. This method was developed for antibacterial testing, after a standard disk diffusion method proved to be ineffective. Antifungal activity of rhamnolipids was evaluated against the fungus Botrytis cinerea, by growing a lawn of fungus on a plate and adding rhamnolipid. The factors influencing rhamnolipid production were studied by growing different Pseudomonas aeruginosa strains from the ATCC culture collection, namely ATCC 9027 and ATCC 27853 as well as a locally isolated strain under different media conditions. The initial focus was on production of biosurfactants in media containing glucose as substrate. Alkanes were subsequently investigated as an alternative substrate, since they are readily available in South Africa as byproducts from the petrochemical industry. The rhamnolipids produced from the culture collection strains were evaluated for their antibacterial activity against Mycobacterium aurum. A number of key factors were identified which were important for the development of a rhamnolipid production process. Of critical importance were the media conditions. Good production was achieved on glucose media containing a phosphate limitation, pH buffering around neutral pH and a high carbon concentration (2 % carbon). When Pseudomonas aeruginosa ATCC 9027 was cultured on this medium (a minimal salts phosphate limited medium with a Tris buffer), it produced 1.31 g/l rhamnose, equivalent to 4.0 g/l rhamnolipid. This rhamnolipid concentration is 2.7-fold higher that of 1.47 g/l reported in the literature with the same strain (cultured on a different phosphate limited medium The particular strain also proved to be a factor which influenced the yield of rhamnolipids. A rhamnose concentration of 0.43 g/l was obtained with Pseudomonas aeruginosa ATCC 27853 grown on MSM+Tris medium, compared to 1.31 g/l produced by Pseudomonas aeruginosa ATCC 9027 on the same medium. The most promising strain and medium, Pseudomonas aeruginosa ATCC 9027 and MSM+Tris medium, were evaluated under controlled conditions in an instrumented bioreactor. Nearly double the rate of growth and production were obtained in the bioreactor, indicating that production time can be shortened considerably under controlled conditions. However, when compared to shake flask studies, only a 4 % increase in growth and a 5 % increase in rhamnolipid production were achieved in the bioreactor, indicating that the yield was limited by the media components or process conditions. With media containing hexadecane as sole carbon source, negligible rhamnolipid production was achieved. Slow growth was observed and the stationary phase had not been reached even after 2 weeks of growth. It was shown that in glucose media rhamnolipid production only commenced in the stationary phase. Since the stationary phase was not reached during growth on hexadecane, rhamnolipids, which are known to increase the availability of alkanes through emulsification and solubilisation, could not be produced. A strategy was devised to accelerate growth on alkane media. A dual substrate medium containing both glucose and hexadecane was investigated. It was hypothesised that growth would be promoted by glucose leading to rhamnolipid production, which would then increase the uptake of hexadecane. Rhamnolipid was produced in the dual substrate experiments, but the hexadecane uptake was still poor. This was suggested to be due to the exposure of the cells to glucose in the inoculum or test flask, which hampered the ability of the cells to utilise hexadecane. It was reasoned that the ability to utilise hexadecane was determined by the cell hydrophobicity, which was influenced by the exposure to hydrophilic or hydrophobic substrates. Rhamnolipids from Pseudomonas aeruginosa ATCC 9027 and ATCC 27853 were shown to have antibacterial activity against Mycobacterium aurum. The largest zone of clearing of 45 mm was obtained with 4 g/l rhamnolipid from Pseudomonas aeruginosa ATCC 9027. The activity was shown to be directly related to the rhamnolipid concentration, highlighting the importance of maximising the biosurfactant yield when developing a process for the production of rhamnolipids as antimicrobial agents. Antifungal activity tests against Botrytis cinerea were inconclusive. Future studies should expand the antimicrobial application of rhamnolipids by testing their activity against a larger range of target organisms. In order to maximise the rhamnolipid yield in future studies, a fed batch process is proposed which would increase the cell density thereby increasing rhamnolipid production and prolonging the stationary phase, which was found to be the phase associated with rhamnolipid production. Different feeding strategies should be investigated, depending on the kinetics of substrate consumption. It is desirable to feed the smallest volume of substrate that is necessary with a high concentration in order to keep the dilution rate low and maximise the product concentration. A factorial design is recommended for this purpose. Further studies with alkanes as carbon source should be conducted using strains that have been maintained and cultured on media containing alkanes as sole carbon source. Alternative biosurfactant producing strains should also be investigated, which have higher natural cell hydrophobicities.
Marky, Bazan Karina. "Sistema de costos por proceso que contribuye en la obtención de costos eficientes de la Empresa Mobiliarios Hospitalarios Sin Fin SAC, del distrito La Victoria, año 2016." Bachelor's thesis, Universidad Ricardo Palma, 2016. http://cybertesis.urp.edu.pe/handle/urp/1433.
Full textTubychko, K. V., and O. M. Pihnastyi. "About the methods of formalization of technological process." Thesis, Брама, 2016. http://repository.kpi.kharkov.ua/handle/KhPI-Press/48303.
Full textChen, Yongjiang. "An integrated process planning and production scheduling framework for mass customization /." View Abstract or Full-Text, 2003. http://library.ust.hk/cgi/db/thesis.pl?IEEM%202003%20CHENY.
Full textIncludes bibliographical references (leaves 146-154). Also available in electronic version. Access restricted to campus users.
Yu, Hui. "Effects of process approaches and process parameters on assembly precision /." View Abstract or Full-Text, 2002. http://library.ust.hk/cgi/db/thesis.pl?IEEM%202002%20YU.
Full textIncludes bibliographical references (leaves 140-148). Also available in electronic version. Access restricted to campus users.
Kocaker, Bahadir Mustafa. "Production Properties Prediction After Forming Process Sequence." Master's thesis, METU, 2003. http://etd.lib.metu.edu.tr/upload/4/1095512/index.pdf.
Full textBoran, Efe. "Process Development For Continuous Photofermentative Hydrogen Production." Master's thesis, METU, 2011. http://etd.lib.metu.edu.tr/upload/12612955/index.pdf.
Full text- hydroxybutyrate, specific rates of product formation were determined.
Treitz, Martin. "Production process design using multi-criteria analysis." Karlsruhe : Univ.-Verl. Karlsruhe, 2006. http://www.uvka.de/univerlag/volltexte/2006/178/.
Full textDahlin, Jesper, and Simon Karlsson. "Streamline the production process using Lean 5S." Thesis, Linköpings universitet, Medie- och Informationsteknik, 2013. http://urn.kb.se/resolve?urn=urn:nbn:se:liu:diva-94743.
Full textLou, Yuhang. "Decarbonisation in power production and process sites." Thesis, University of Manchester, 2008. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.489510.
Full textSmith, Stephen E. "Process management applications in biopharmaceutical drug production." Thesis, Massachusetts Institute of Technology, 2011. http://hdl.handle.net/1721.1/66048.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 71-73).
Genzyme's manufacturing and supply chain organization is responsible for the production and delivery of medically necessary medicines for patients with rare diseases around the world. Because of the nature of the products produced at Genzyme, a lapse in operational performance has societal as well as economic impacts. Therefore increased understanding of the complex production systems at Genzyme is helpful to reduce risk and improve performance. This thesis is an analysis of a system of two critical production processes at Genzyme. These processes are studied collectively because shared resources make them a tightly coupled system. The research is presented in three sections. The first section explores the current state of the system and explains general performance trends. The second section examines the impact of scheduling complexity arising from shared resources. The third section discusses how process improvement methodologies could be applied at Genzyme. The following conclusions arise from the work conducted for this thesis. First, the performance of the system has declined due to an increase in utilization and an already high level of variability. Second, variability caused by shared resource conflicts can be minimized using new scheduling techniques. And finally, continuous improvement methods are recommended to further reduce variability and increase overall process performance.
by Stephen Smith.
S.M.
M.B.A.
Mohamed, Abdulaziz Hemmali. "Process intensification in syngas production and cleaning." Thesis, University of Newcastle upon Tyne, 2013. http://hdl.handle.net/10443/2135.
Full textRodrigues, Ana Rita Guerra Silva. "A green integrated process for biodiesel production." Master's thesis, FCT - UNL, 2009. http://hdl.handle.net/10362/2716.
Full textNeste trabalho experimental desenvolveu-se um processo contínuo de produção de biodiesel, a partir de óleo virgem e óleo usado, usando dióxido de carbono supercrítico como solvente e utilizando catálise enzimática. A produção de biodiesel através da reacção de transesterificação de óleo de girassol com metanol, utilizando a Lipozyme TL IM® demonstrou tratar-se de um processo com um elevado potencial nas seguintes condições p = 20 MPa; T = 313,15 K; tempo de residência: 20 segundos e razão molar óleo: metanol: 1:24. O processo integra, igualmente, uma fase de fraccionamento. A separação a p=12 MPa e 333,15 K permite um elevado enriquecimento da fase gasosa em biodiesel. Usando apenas a Lipozyme TL IM® a conversão do óleo usado em biodiesel revelou-se inferior à obtida com óleo virgem, no entanto, a combinação de duas enzimas, Lipozyme TL IM® e Novozyme 435®, revelou ser uma opção viável, atingindo-se um rendimento de 98,9% nas seguintes condições: p=20 MPa; T = 313,15 K; tempo de residência: 30 segundos e razão molar óleo: metanol: 1:24. Uma vez que este rendimento é muito elevado, foi descrito um processo simples de fraccionamento para a recuperação do glicerol e metanol. Foi desenvolvido um estudo de engenharia para o processo de produção contínua de biodiesel utilizando óleo usado com a elaboração de balanços de massa e de energia. Através do aproveitamento do calor libertado durante a compressão de CO2, conclui-se ser necessário fornecer ao sistema 89,75 MJ / h. Um estudo de viabilidade económica foi desenvolvido através do qual se determinou um valor de investimento total de 21.728.718 € e um lucro anual de 3.359.731 €.
Nevlydov, I., V. Yevsieiev, S. Miliutina, and V. Bortnikova. "Accelerometers production technological process decomposition parameters model." Thesis, 2016 XII International Conference on Perspective Technologies and Methods in MEMS Design (MEMSTECH), 2016. http://openarchive.nure.ua/handle/document/3508.
Full textCrosby, Aaron James. "Brigadoon Lighting Design: In Process and Production." Master's thesis, Temple University Libraries, 2015. http://cdm16002.contentdm.oclc.org/cdm/ref/collection/p245801coll10/id/313244.
Full textM.F.A.
The following thesis document examines the production process for the lighting design of Temple University Theatre Department's production of Brigadoon. It will explore the analytical, conceptual, and technical aspects of my personal process as a lighting designer, as well evaluate the department's Master of Fine Arts program and how it contributed to my development as a fine artist in the field of lighting design.
Temple University--Theses
Eltepe, Hüdal Emre Balköse Devrim. "The Development of Zinc Borate Production Process/." [s.l.]: [s.n.], 2004. http://library.iyte.edu.tr/tezler/master/kimyamuh/T000499.pdf.
Full textColquhoun, Thomas Angus. "Floral fragrance production is a specialized process." [Gainesville, Fla.] : University of Florida, 2009. http://purl.fcla.edu/fcla/etd/UFE0025170.
Full textRonchi, Fabrizio. "Design of experiment in production process innovation." Doctoral thesis, Università degli studi di Padova, 2018. http://hdl.handle.net/11577/3425892.
Full textNel suo famoso libro Progettazione ed Analisi degli Esperimenti, Montgomery descrive il Design of Experiment (DOE) come un esteso approccio ad un esperimento che parte dall’enunciato del problema, attraversa la progettazione della fase sperimentale e lo studio delle possibili soluzioni, per chiudersi con le conclusioni e le raccomandazioni. In particolare, il DOE è riconosciuto essere un potente strumento che si basa sulla statistica per progettare ed analizzare gli esperimenti. Le potenzialità del DOE sono ben conosciute ed apprezzate tra gli studiosi. In alcuni campi le sue potenzialità sono riconosciute ed apprezzate anche dai professionisti. Per questo motivo c’è un uso esteso del Design of Experiment nel miglioramento della qualità dei processi industriali. Secondo la definizione fornita da Bisgaard, l’innovazione è l’intero processo di sviluppo ed alla fine commercializzazione di nuovi prodotti e servizi, di nuovi metodi di produzione o approvvigionamento, di nuovi metodi di trasporto o servizi di consegna, di nuovi modelli di business, nuovi mercati, o nuove forme di organizzazione. Mentre l’uso del DOE è ben diffuso nella sperimentazione industriale per il miglioramento della qualità, il vantaggio dell’uso del DOE per l’innovazione è fonte di dibattito tra gli studiosi e tra i professionisti. L’idea di studiare l’uso del DOE per l’innovazione dei processi di produzione ha origine da questo dibattito. La ricerca è stata condotta secondo diverse prospettive. La prima prospettiva riguarda l’efficacia del DOE nel supportare e potenziare la fase di innovazione di un processo produttivo. Essa è evidenziata grazie ad un caso studio nel quale è stata sviluppata una strategia per innovare il processo di termoformatura per la produzione di un packaging funzionale. Il DOE ha favorito la capacità di innovazione permettendo una riduzione degli errori sistematici e delle distorsioni, una completa esplorazione dello spazio fattoriale, ed una riduzione del numero dei test. Il DOE ha permesso di identificare e superare la discrepanza tra i fattori di controllo in laboratorio e quelli nella linea di produzione. Una seconda prospettiva è di taglio manageriale ed è stata quella della gestione del processo di innovazione. L’impatto positivo che l’adozione del DOE ha avuto sulla gestione del processo di innovazione viene qui mostrato per mezzo di un caso studio. Il DOE ha dato prova di essere utile fornendo appropriati strumenti ed impattando su cinque dimensioni tipiche dell’ambito manageriale: capacità decisionali, integrazione, comunicazione, tempi e costi, e gestione della conoscenza. Sono stati poi studiati alcuni metodi non parametrici. Attraverso uno studio di simulazione sono stati confrontati alcuni test univariati in un piano fattoriale a due vie. Lo studio ha mostrato come l'efficacia dei metodi di analisi vari a seconda del data set da analizzare. Di conseguenza non è emerso un unico approccio da utilizzare nella fase di progettazione dell’esperimento, ma bensì vari aspetti devono essere tenuti in considerazione simultaneamente. Una accurata scelta del test favorisce l’impatto positivo che il DOE ha sull’innovazione dei processi di produzione. Inoltre, è stato sviluppato un nuovo approccio multivariato non parametrico basato sulla NonParametric Combination applicata ai test Synchronized Permutation. Questo approccio si è rivelato essere un buono strumento quando sono violate le assunzioni della MANOVA. Un grosso vantaggio di questo tipo di test sono le ottime performances nel caso di campioni non numerosi che riflette le necessità dei professionisti in ambito industriale dove ci sono limitazioni o risorse scarse per la sperimentazione. Inoltre può essere osservato un aumento della potenza sotto ipotesi alternativa quando il numero delle variabili risposta aumenta ed il numero dei campioni rimane costante. Le proprietà di questo test multivariato lo rendono un utile strumento per l’innovazione dei processi produttivi.
Schiffers, Reinhard, Georg P. Holzinger, and Gernot Huster. "Adaptive process control for stabilizing the production process in injection moulding machines." Saechsische Landesbibliothek- Staats- und Universitaetsbibliothek Dresden, 2016. http://nbn-resolving.de/urn:nbn:de:bsz:14-qucosa-200201.
Full textLozada, Luis O. "Reengineering the process of manufacturing thermal-cryogenics tanks." Online version, 2001. http://www.uwstout.edu/lib/thesis/2001/2001lozadal.pdf.
Full textSaunders, Aidan Cyril Giles. "Process monitoring and non-linear observers." Thesis, University of Newcastle Upon Tyne, 1992. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.308921.
Full textAkkus, Derya. "Analysis Of Coining Process In Production Of Medallion." Master's thesis, METU, 2009. http://etd.lib.metu.edu.tr/upload/12610347/index.pdf.
Full textÅhlström, Pär. "Sequences in the process of adopting lean production." Doctoral thesis, Handelshögskolan i Stockholm, Management av Innovation och Produktion (T), 1997. http://urn.kb.se/resolve?urn=urn:nbn:se:hhs:diva-854.
Full textDiss. Stockholm : Handelshögsk.
Åhlström, Pär. "Sequences in the process of adopting lean production /." Stockholm : Economic Research Insitute, Stockholm School of Economics [Ekonomiska forskningsinstitutet vid Handelshögsk.] (EFI), 1997. http://www.hhs.se/efi/summary/456.htm.
Full textFerré, Anna. "Process development for the robust production of polyhydroxyalkanoates." Thesis, University of Manchester, 2018. https://www.research.manchester.ac.uk/portal/en/theses/process-development-for-the-robust-production-of-polyhydroxyalkanoates(91fd1ca5-b907-4061-b232-99528b0862c0).html.
Full textElhoweris, Ammar. "The process and production of calcium sulfoaluminate cements." Thesis, University of Aberdeen, 2017. http://digitool.abdn.ac.uk:80/webclient/DeliveryManager?pid=232619.
Full textMcIntosh, Timothy Jr (Timothy P. ). "A process for improving long-term production planning." Thesis, Massachusetts Institute of Technology, 2011. http://hdl.handle.net/1721.1/66058.
Full textCataloged from PDF version of thesis.
Includes bibliographical references (p. 67).
This project presents improvements to the business process used to generate the Sikorsky five-year production scheduling plan that is a central coordinating process for company operations. Recommendations will improve the speed and quality of the planning process. The current production planning method leaves Sikorsky at risk of reserving too little capacity to satisfy demand for its most important customers. Additionally, the current method can lead to overproduction of rotorcraft. Both scenarios are very costly to Sikorsky. In the absence of a more data-driven planning approach, shortcomings of the current planning method will only be exacerbated as Sikorsky continues to pursue new customers in emerging markets. Sikorsky may struggle to continue applying judgment-based planning methods to a customer base for which there is little historical information. To investigate the problem, we used interviews, surveys, and lean techniques to study the current state of the five-year planning process. As part of the solution, we developed and applied statistical demand forecasting methods and a more formal process definition. We documented and communicated the new planning process using standard work templates and instructions. New methods were disseminated to stakeholders through a variety of showcase exercises that featured demonstrations and hands-on exercises. In general, Sikorsky production planning stakeholders were receptive to a more formal and datadriven planning process. We expect that the new methods will enable an overall planning process time of two weeks, compared to current process time of several months. Furthermore, the new methods improve forecasting accuracy by integrating and synthesizing previously unused forward-looking sales and marketing data. Going forward, a small pilot team will continue to apply and improve new planning methods. The team will engage in a preliminary pilot exercise during an upcoming revision to the five-year plan, which will occur in early 2011.
by Timothy McIntosh.
S.M.
M.B.A.
Underwood, Curtis J. (Curtis James), and Jacob R. Wood. "Applying an analytical framework to production process improvement." Thesis, Massachusetts Institute of Technology, 2007. http://hdl.handle.net/1721.1/39694.
Full textIncludes bibliographical references (p. 74).
As the medium voltage switchgear industry moves from air insulated to gas insulated technology, Siemens Frankfurt factory is introducing a new gas insulated product line that will improve their relative market position. It is their intent to design a product and supporting production system that will enable substantial cost and lead time reduction over existing Siemens gas insulated switchgear products. This thesis outlines a framework for analyzing the existing production process from 'customer order to customer delivery', identifying areas of opportunity, valuing projects aimed at achieving these opportunities, and prioritizing highest value projects for implementation. To provide a rigorous analytical approach to project selection, it was important to rethink existing ways of valuing inventory holding costs, material handling costs, and lead time. By uncovering hidden costs and benefits for each, projects that otherwise seemed unattractive become important to achieving overall factory objectives. Conversely, other projects that had been historically pushed by factory leadership were shown to generate little overall return on investment.
(cont.) By using the approach outlined in this thesis, improved alignment was achieved across departments on several high value projects. This alignment positioned the factory to move forward with plans for successful implementation. It is the authors' hope that Frankfurt not only finalizes implementation of high value projects identified during this analysis, but also use the framework provided for future analysis and continued improvement.
by Curtis J. Underwood & Jacob R. Wood.
S.M.
M.B.A.
Lindsey, Christine M. (Christine Marie) 1977. "Critical process parameter determination during production start-up." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/34741.
Full textIncludes bibliographical references (p. 83-84).
Production start-up data is consistently utilized in a reactive manner during the initial stages of a product's lifecycle. However, if proactive information systems are created before full scale production starts, ramp-up cycles can be shortened considerably. This project attempts to develop a framework for analyzing process data quickly and efficiently during a new product start-up in order to provide information for the short term goals relating to attaining stable processes as well as provide guidance on long term handles for process improvement. First, a summary of previous literature regarding start-up process data as well as typical stable process data usage will be presented. This will provide adequate background for evaluating typical gaps present during production ramp-up. Then, solutions to these gaps will be discussed in order to develop tools for better data analysis in shorter periods of time. These methods will then be applied to a case study involving the. new production of Kodak's DCS Pro 14N digital camera. The Kodak Professional DCS Pro 14N was an amazing leap in technology: a camera with double the resolution for roughly half the price of any product available. Unfortunately, it soon became apparent that the original demand estimates were grossly underestimated, straining original resource allocations. Manufacturing struggled to start and was already a year behind in backorders. With over 1.500 process attributes collected on each camera, the key drivers of quality had yet to be determined. The surrounding circumstances made the quick analysis of start-up data vital to effective resource management and yield improvement of the camera.
(cont.) After using the new process modeling framework and modified control techniques on the example Kodak case, two additional topics will be discussed. First, the many classifications of return on investment in proactive start-up data analysis will be presented. Ranging from waste minimization to higher customer satisfaction, these incentives justify early preparation for start- up data analysis. Finally, future areas of study will be recommended to augment the findings within the thesis.
by Christine M. Lindsey.
M.B.A.
S.M.
Belo, José Nuno Palma e. "A process-based control for evolvable production systems." Master's thesis, Faculdade de Ciências e Tecnologia, 2011. http://hdl.handle.net/10362/5967.
Full textNowadays, companies in a challenging environment are compelled to adapt to the rapid changes in the manufacturing business. The search for new processes to create products with short life-cycles at low cost, while keeping the same levels of productivity and quality is greater than ever. This has generated the need to create even more agile manufacturing systems, which could easily adapt to the market changes at a low cost. Advances in information technologies have allowed manufacturing systems to achieve new levels of agility, opening the doors to new approaches. These same advances helped companies in several sectors other than manufacturing to gain e ectiveness through the synchronization of the processes of their several departments by using Business Process Management tools. This thesis proposes a system that reacts and adapts itself to di erent production orders by means of recon guration. To reach this goal, the concept of Business Process Management was used. This concept, already used in many companies, allows them to model their inner behaviours with processes that can be changed according to their needs. A manufacturing system using this may become equally agile and alter its functioning in accordance with the needs of other departments of the same company. To create the system presented in this thesis it was used a multi-agent architecture based on process execution. Each agent contains a knowledge base, used by its processes,that stores internal or external information. This system may be used not only in the manufacturing shop oor, but also in any other areas within a company. This thesis also presents an application of the system to the shop oor, based on the Evolvable Production Systems concept, in which each agent represents a manufacturing resource that o ers a given set of services useful to the production process. The resources,by means of the agents, may aggregate among themselves to execute services together. Keywords: Manufacturing system, multi-agent system, ontology, process, BPM, EPS.
Beatriz, Ricardo Filipe Martins. "Safety function analysis in an industrial production process." Master's thesis, Faculdade de Ciências e Tecnologia, 2012. http://hdl.handle.net/10362/8075.
Full textAim: The purpose of this work was to identify and assess safety features on a production line of paper manufacturer called Renova. The assessment includes technical as well as organisational factors. The study was carried out through the evaluation of safety functions (SF), either present or absent in the system analyzed. Methods: The methodology applied was the SFA (Safety Function Analysis), which was developed by Harms-Ringdahl in 2001 and was updated further, in 2011 (draft version). The analytical framework was applied in two processes (raw material loading and transversal cut of log) of a production line (Line H4) of Renova. Results: In the first process analyzed (raw material loading), 47 safety functions (SF) were identified and evaluated, whereas 36 SF were assessed in the second case (transversal cut of log). The evaluation has shown that most of the SF considered are in good condition and being well monitored, therefore they do not need any improvements. In contrast, this work has also identified a number of safety functions that need essential improvements. Conclusions: As a consequence of this SFA analysis, the author proposes a number of specific recommendations to improve safety and the system’s performance in general. Since Renova is a manufacturer of paper products, fire safety is of paramount importance and one of the most relevant recommendations is perhaps the implementation of thermo graphic tests to identify possible hot spots that may originate a fire.
Pihnastyi, O. M. "Statistical two-level model of the production process." Thesis, Apostrophe, 2011. http://repository.kpi.kharkov.ua/handle/KhPI-Press/42134.
Full textXu, Dikai Xu. "Chemical Looping Partial Oxidation Process for Syngas Production." The Ohio State University, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=osu1503277899450895.
Full textZhiltsova, Tatiana Vladimirovna. "Injection moulding process optimization for microstructured parts production." Doctoral thesis, Universidade de Aveiro, 2013. http://hdl.handle.net/10773/12059.
Full textAo longo das últimas décadas, a micromoldação (u-moldação) por injeção de termoplásticos ganhou um lugar de destaque no mercado de equipamentos eletrónicos e de uma ampla gama de componentes mecânicos. No entanto, quando o tamanho do componente diminui, os pressupostos geralmente aceites na moldação por injeção convencional deixam de ser válidos para descrever o comportamento reológico e termomecânico do polímero na microimpressão. Por isso, a compreensão do comportamento dinâmico do polímero à escala micro bem como da sua caraterização, análise e previsão das propriedades mecânicas exige uma investigação mais alargada. O objetivo principal deste programa doutoral passa por uma melhor compreensão do fenómeno físico intrínseco ao processo da μ-moldação por injeção. Para cumprir com o objetivo estabelecido, foi efetuado um estudo paramétrico do processo de μ-moldação por injeção, cujos resultados foram comparados com os resultados obtidos por simulação numérica. A caracterização dinâmica mecânica das μ-peças foi efetuada com o objetivo de recolher os dados necessários para a previsão do desempenho mecânico das mesmas, a longo prazo. Finalmente, depois da calibração do modelo matemático do polímero, foram realizadas análises estruturais com o intuito de prever o desempenho mecânico das μ-peças no longo prazo. Verificou-se que o desempenho mecânico das μ-peças pode ser significativamente afetado pelas tensões residuais de origem mecânica e térmica. Estas últimas, resultantes do processo de fabrico e das condições de processamento, por isso, devem ser consideradas na previsão do desempenho mecânico e do tempo de serviço das u-moldações.
Over the last decades, microinjection moulding (uIM) of thermoplastics has gained a pertinent place on the market of electronic equipment and a broad range of the mechanical aids. However, when size of components drop to the micro level, the assumptions of the conventional injection moulding cease to describe the complex rheological and thermo-mechanical behavior of the polymer in the microimpression. Therefore, understanding of the polymer flow dynamics at the micro scale as well as characterization, assessment and prediction of the final mechanical properties require a great deal of additional research. The prime objective of this doctoral thesis is to get an insight into the physical phenomena inherent to μIM process. In order to comply with the established objective, a number of parametrical studies of the μIM process were carried on an instrumented micromould and then their results were compared with the obtained numerical simulation results gathered from process modeling phenomena. Dynamical mechanical characterization of μ-moulded parts was performed in order to collect the data required for prediction of their long-term mechanical performance. Finally, after calibration of polymer material model, a long-term transient structural analysis was carried out. It was found out that the structural performance of microparts was significantly affected by the thermo-mechanical (residual) stresses. The latter is an inherent feature of the injection moulding processing, and therefore has to be accounted for the prediction of the u-moulded parts’ service life.
Ingwald, Anders. "Technologies for better utilisation of production process resources." Doctoral thesis, Växjö : Växjö University Press, 2009. http://urn.kb.se/resolve?urn=urn:nbn:se:vxu:diva-2505.
Full textStorgårds, Erna. "Process hygiene control in beer production and dispensing /." Espoo [Finland] : Technical Research Centre of Finland, 2000. http://www.vtt.fi/inf/pdf/publications/2000/P410.pdf.
Full textGiesteira, Artur Amorim Gonçalves. "Primary Good Production Process Improvement." Master's thesis, 2017. https://hdl.handle.net/10216/105774.
Full textGiesteira, Artur Amorim Gonçalves. "Primary Good Production Process Improvement." Dissertação, 2017. https://hdl.handle.net/10216/105774.
Full textChiou, Wei-Hau, and 邱偉豪. "Production-inventory management underdeterioration process." Thesis, 2011. http://ndltd.ncl.edu.tw/handle/37726482648906659809.
Full text逢甲大學
工業工程與系統管理學研究所
99
In conventional production-inventory management approach, the production order quantity is determined by referring to the costs such as ordering cost and inventory cost. However, the quality level being produced may change during production process due to the deterioration process. Thus, under the deterioration process, production order quantity solely based on the conventional production-inventory management system may be overproduced, due to a lack of consideration of varied quality costs at different points of time, along with the production run length. Hence, for cyclical quality promotion and cost reduction, there is a motivation to extend the conventional production-inventory management approach by adding the process-quality design approach which considers the process resetting as a function of time. The decision variables include: initial setting, process tolerance, resetting cycle, production order quantity which have to be determined simultaneously for true optimization, so that the average total cost, which includes: setup cost for production reordering and process resetting, quality loss and tolerance cost for process quality, and inventory cost for production inventory, is minimized. An example is presented to demonstrate the proposed model.
Lin, Chun-Yu, and 林俊宥. "Process Development for Biodiesel Production." Thesis, 2011. http://ndltd.ncl.edu.tw/handle/91718034457296518052.
Full text國立中正大學
化學工程研究所
99
Biodiesel have been produced commercially by using basic homogeneous catalysts, such as NaOH and KOH. However, the base-catalyzed reactions are very sensitive to the free fatty acid (FFA) contenting in the oil feed. Hence, the basic catalysts are unsuitable to produce esters from unrefined oils which have FFA content higher than approximately 3 wt%. In this study, organ-metallic, B(OCH3)3, and heterogeneous catalysts, V2O5/SiO2, have been found to be useful for remedying the drawbacks of the basic catalysts. By the use B(OCH3)3, up to 60 % of vegetable oil was catalytically converted to bio-diesel within two hours in a batch reactor under a condition of oil to methanol ratio of 1 to 6 at 230 C and 13.6 bar, while more than 95% oil was converted for V2O5/SiO2 catalysts. In order to understand the superior catalytic properties of V2O5/SiO2 catalysts, the structure of the fresh and used catalysts were characterized by synchrotron PXRD, EXAFS, and FT-IR. The results indicated that V2O5 was converted to vanadium organic compounds (vanadium methylate) anchored on silica supports. For commercial application, process with reactive distillation technique was developed. Under atmospheric pressure and catalyzed by B(OCH3)3, the conversion of oil in a reactive column is about 15% without methanol recycle, while about 25% for the same operating conditions with methanol recycle. Different from base catalyst system, biodiesel products could simply be separated and purified from outlet stream vacuum distillation; troublesome acid-base neutralization, water wash, and filtration steps are not necessary for the new process.
Meher, Anil. "ECM Process Characteristics." Thesis, 2009. http://ethesis.nitrkl.ac.in/1311/1/ECM_Process_Characteristics.pdf.
Full textSamal, C. "Study of process parameters towards improving efficiency of closed die hot forging process." Thesis, 2014. http://ethesis.nitrkl.ac.in/5909/1/E-87.pdf.
Full textTzeng, Fu-Sheng, and 曾福勝. "Process For Production Of Aliphatic Esters." Thesis, 2000. http://ndltd.ncl.edu.tw/handle/63134375922938014552.
Full text國立中正大學
化學工程研究所
88
Abstract The commercial production of ethyl acetate is mainly by two processes: the Tischenko reaction which produces ethyl acetate by direct conversion of ethanol via acetaldehyde using aluminum alkoxide catalyst; and the production of ethyl acetate by direct esterification of ethanol with acetic acid using a sulfuric acid catalyst. Since both process have wasted-catalyst-treatment problem and have to suffer high cost of raw material, it motivates us to develop a process for the conversion of water-containing ethanol to ethyl acetate. By Pd/SDB (styrene divinylbenzene copolymer) catalyst developed before, the process includes two stages operated in a fix-bed reactor. The first stage is the catalytic oxidation of ethanol to acetic with air over the Pd catalyst and the second stage is the esterification of acetic acid with ethanol over Amberlyst-15 catalysts. In this study, we found that Pd(II)-acetate formed from the reaction of the reaction immediate, acetic acid, with Pd clusters on the catalysts results in a leaching and aggregating of Pd clusters thereby decreasing the catalyst activity. To remedy the drawbacks of the catalysts, zeolite-supported bimetallic catalysts have been developed. By controlling the properties of supports including pore size, acidity, and polarity, the goals of high esterification selectivity, stability maintenance, and low impurity have been achieved. The experimental results indicated that catalyzed by Pd-X(Pt, Ag, Ni, Ru, Zn)/Zeolite catalysts, about 62.5% ethanol was converted and the selectivity to ethyl acetate selectivity was up to 93.3%. Moreover, since the catalysts can be regenerated under very mild conditions, they are regarded to be promising for industrial application.
RizkiviaRadita, Deqi, and 丁艾琳. "Mathematical Modeling of Biohydrogen Production Process." Thesis, 2013. http://ndltd.ncl.edu.tw/handle/26115615356603926783.
Full text國立成功大學
環境工程學系碩博士班
101
Fermentative bio-hydrogen production process is a very complex process that contain particular step. The hydrogen production rate from this process is influenced by many factors. This process always suffers from instability because of its complex process and a lack of understanding of the process. The instability of the process can cause process failure and lack of hydrogen gas production. Mathematical model can help to obtain better understanding of some process. It contains a set of relationship between the variables that influence each process step. It can observe the possible behavior and the important step that happened in the process. Appropriate mathematical model needs to be developed in order to get better understanding of fermentative bio-hydrogen production process. The fermentative bio-hydrogen production process that used different kind of main carbohydrate in the substrate such as maltose and xylose did not seem to follow the common patterns of fermentative bio-hydrogen production process by glucose fermentation. The possible patterns of the fermentative bio-hydrogen production process by maltose and xylose is expected to be explained by using mathematical model. The previous research results that used maltose and xylose as the main carbohydrate in the substrate are used to obtain appropriate mathematical model. It is assumed that there are two main processes happened in the maltose and xylose fermentation bio-hydrogen production process. The first step is maltose or xylose consumption that produced lactate and acetate compound. The next step is lactate and acetate consumption that produced butyrate. The mathematical model simulation of maltose and xylose fermentation bio-hydrogen production process fit well with the experimental data. The mathematical model describes each step from maltose or xylose consumption until butyrate production properly. Although it do not fit well with hydrogen and carbon dioxide but it can describes well the hydrogen and carbon dioxide production rate.
Moberg, Annelie K. "Process engineering fundamentals of microalgae production." Thesis, 2012. http://hdl.handle.net/1959.13/940358.
Full textThis thesis addresses the process engineering fundamentals of a new design of photobioreactor and determines the practical range of operating parameters to support high productivity algae growth. The fluid dynamic conditions within the reactor are important in designing for high performance. Liquid phase mass transfer controls the transfer rates of the photosynthetic gases in and out of the culture. Radial mixing impacts on the effectiveness of the light regime, as individual algae cells move between lighter and darker regions of the culture. These phenomena have been studied for the distinguishing design features of the system, in which the culture circulates through oating, partially filled, horizontal tubular solar receivers. Key variables, including liquid velocities, gas compositions, reactor lengths and tube diameters, have been analyzed and optimum conditions identified. Investigations included the use of an experimental prototype, CFD modeling, particle tracking, and the development of process modeling algorithms and simulations. Results showed that the photobioreactor under study can be configured and operated to create a culture environment likely to support the high productivity target of 55 g m⁻² day⁻¹ using a gas phase of flue gas composition. Suitable mass transfer rates at the solar receiver free surface can be achieved at liquid velocities of 0.3-0.5 m s⁻¹, and makes a substantial difference to the maximum tube lengths possible without excessive oxygen accumulation compared to tubes operating full. Lengths of 100 m are likely to support high productivity and stable pH regimes. Under these fluid dynamic conditions, the algae cell light/dark cycling frequency range is of the order of 1 Hz where productivity increases may be expected. Scale-up of the reactor design to the commercial demonstration stage by the industry partner has been made possible following a detailed engineering feasibility study based on fundamental insights, design parameters and practical tools developed in this work.
Mohanty, Suranjan. "Modelling of hard turning process." Thesis, 2014. http://ethesis.nitrkl.ac.in/6312/1/E-60.pdf.
Full textBoipai, Budhram. "FEM analysis for WEDM process." Thesis, 2014. http://ethesis.nitrkl.ac.in/6489/1/212ME2293-7.pdf.
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