Dissertations / Theses on the topic 'Chemical processes Design'
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Lai, Sau Man. "Feasibility and flexibility in chemical process design /." View abstract or full-text, 2009. http://library.ust.hk/cgi/db/thesis.pl?CBME%202009%20LAI.
Full textEggersmann, Markus. "Analysis and support of work processes within chemical engineering design processes /." Düsseldorf : VDI-Verl, 2005. http://bvbr.bib-bvb.de:8991/F?func=service&doc_library=BVB01&doc_number=013342934&line_number=0001&func_code=DB_RECORDS&service_type=MEDIA.
Full textZhu, Jianye. "Integrated process design and control of chemical processes." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0009/NQ34864.pdf.
Full textAmale, Amit. "New approach to the design and optimization on energy efficient chemical processes /." View online ; access limited to URI, 2008. http://0-digitalcommons.uri.edu.helin.uri.edu/dissertations/AAI3314439.
Full textBarrera, Michael D. "Optimal design and operation of batch processes." Thesis, Massachusetts Institute of Technology, 1990. http://hdl.handle.net/1721.1/80458.
Full textVan, Dyk Braam. "Computerized design of solvents for extractive processes." Thesis, Stellenbosch : Stellenbosch University, 2001. http://hdl.handle.net/10019.1/52171.
Full textENGLISH ABSTRACT: Separation processes are an integral part of chemical engineering. The purity of a chemical product is among the principal factors influencing its value. Therefore, any method that can increase the purity of a product or decrease the cost of purification will have a direct effect on the profitability of the entire plant. An important class of separation processes is the solvent-based separations. This includes processes like extractive distillation, liquid-liquid extraction and chromatographic separation. Heterogeneous azeotropic distillation is closely related to these processes. The most important variable in the design of a solvent-based separation process is the choice of solvent. A genetic algorithm for the computer-aided molecular design of solvents for extractive distillation had been previously developed by the author. This algorithm was improved and expanded to include liquid-liquid extraction, heterogeneous azeotropic distillation, gas-liquid chromatography and liquid-liquid (partition) chromatography. At the same time the efficiency of the algorithm was improved, resulting in a speed increase of up to 500% in certain cases. An automatic parameter tuning algorithm was also implemented to ensure maximum efficiency of the underlying genetic algorithm. In order to find suitable entrainers for heterogeneous azeotropic distillation a method is required to locate any ternary heterogeneous azeotropes present in a system. A number of methods proposed in the literature were evaluated and found to be computationally inefficient. Two new methods were therefore developed for ternary systems. A methodology for applying these methods to quaternary and higher systems was also proposed. Two algorithms to design blended solvents were also developed. Blended solvents allow the use of simpler and thus cheaper solvents by spreading the active functional groups over several molecular backbones. It was observed in a number of cases that the blended solvents performed better than their individual components. This was attributed to synergistic interactions between these components. Experimental evidence for this effect was also found. The algorithm was applied to a number of industrially important separation problems, including the extremely difficult final purification process of alpha olefins. In each case solvents were found that are predicted to perform substantially better than those that are currently used in industry. A number of these predictions were tested by experiment and found to hold true.
AFRIKAANSE OPSOMMING: Skeidingsprosesse is 'n integrale deel van chemiese ingenieurswese. Die suiwerheid van 'n chemiese produk is een van die hoof faktore wat die waarde daarvan bepaal. Derhalwe sal enige metode wat die suiwerheid van 'n produk kan verbeter, of die koste van die suiwering daarvan kan verlaag, 'n direkte effek op die winsgewendheid van die hele aanleg hê. 'n Belangrike groep skeidingsprosesse is die oplosmiddel-gebaseerde skeidings. Dit sluit prosesse soos ekstraktiewe distillasie, vloeistofvloeistof ekstraksie en chromatografiese skeidings in. Heterogene azeotrope distillasie is nou verwant aan hierdie prosesse. Die belangrikste veranderlike in die ontwerp van so 'n oplosmiddel-gebaseerde proses is die keuse van oplosmiddel. 'n Genetiese algoritme vir die rekenaargesteunde molekulêe ontwerp van oplosmiddels vir ekstraktiewe distillasie is voorheen ontwikkel deur die skrywer. Hierdie algoritme is verbeter en uitgebrei om vloeistofvloeistofekstraksie, heterogene azeotrope distillasie, gas-vloeistof chromatografie en vloeistof-vloeistof (verdelings) chromatografie in te sluit. Ter selfde tyd is die doeltreffendheid van die algoritme verbeter, wat 'n verbetering in spoed van tot 500% in sekere gevalle tot gevolg gehad het. 'n Algoritme om die parameters van die onderliggende genetiese algoritme outomaties te verfyn is ook geïm plementeer om die optimale werksverrigting van die algoritme te verseker. Om gepaste saamsleepmiddels vir heterogene azeotrope distillasie te vind, word 'n metode benodig om enige ternêre heterogene azeotrope aanwesig in 'n stelsel op te spoor. 'n Aantal sulke metodes wat in die literatuur voorgestel is, is geëvaluEer en daar is gevind dat hierdie metodes ondoeltreffend is. Twee nuwe metodes is derhalwe ontwikkel vir ternêre stelsels. 'n Metodiek om hierdie metodes op kwaternêre en hoër stelsels toe te pas, is ook voorgestel. Twee algoritmes vir die ontwerp van gemengde oplosmiddels is ook ontwikkel. Gemengde oplosmiddels laat die gebruik van eenvoudiger en dus goedkoper oplosmiddels toe, deur die aktiewe funksionele groepe oor 'n aantal molekulêe strukture te versprei. Daar is 'n aantal gevalle waargeneem waar die mengsel beter skeiding bewerkstellig het as die individuele oplosmiddels waaruit dit bestaan. Dit is toegeskryf aan 'n sinergistiese wisselwerking tussen die komponente van die mengsel. Eksperimentele getuienis vir hierdie effek is ook ingewin. Die algoritme is toegepas op 'n aantal belangrike skeidingsprobleme vanuit die bedryf, insluitende die uiters moeilike finale suiwering van alfa olefiene. In elke geval is oplosmiddels gevind wat volgens voorspelling aansienlike beter skeidings sal bewerkstellig as dié wat tans in die bedryf gebruik word. 'n Aantal van hierdie voorspellings is eksperimenteel getoets en korrek bewys.
Smith, Edward Maxwell de Brant. "On the optimal design of continuous processes." Thesis, Imperial College London, 1996. http://hdl.handle.net/10044/1/7850.
Full textSchug, Brett W. "Standardized modular process design with interval reasoning." Diss., Georgia Institute of Technology, 1998. http://hdl.handle.net/1853/10239.
Full textQuirante, Natalia. "Rigorous Design of Chemical Processes: Surrogate Models and Sustainable Integration." Doctoral thesis, Universidad de Alicante, 2017. http://hdl.handle.net/10045/74373.
Full textPetridis, Dimitrios P. (Dimitrios Petros). "Computer-aided design of integrated biochemical processes : development of BioDesigner." Thesis, Massachusetts Institute of Technology, 1990. http://hdl.handle.net/1721.1/13749.
Full textSaraidaris, C. "The optimal design of chemical processes considering multiple objectives and uncertainty." Thesis, University of Manchester, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.384384.
Full textPanjapornpon, Chanin Soroush Masoud. "Model-based controller design for general nonlinear processes /." Philadelphia, Pa. : Drexel University, 2005. http://dspace.library.drexel.edu/handle/1860/611.
Full textMarcoulaki, E. C. "Stochastic optimisation tools for targeting and design of chemical engineering processes." Thesis, University of Manchester, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.504691.
Full textPfeiffer, Celaya Carlos Fernando. "Analysis and design of heterogeneous control laws for nonlinear chemical processes /." Digital version accessible at:, 1999. http://wwwlib.umi.com/cr/utexas/main.
Full textPasanen, Antti. "Phenomenon-driven process design methodology : computer implementation and test usage /." Espoo, [Finland] : Technical Research Centre of Finland, 2001. http://www.vtt.fi/inf/pdf/publications/2001/P438.pdf.
Full textPan, Yanbo. "Energy efficiency-based design of catalytic and non-catalytic processes." University of Akron / OhioLINK, 2020. http://rave.ohiolink.edu/etdc/view?acc_num=akron1596203425631645.
Full textRao, Vikram Mohan. "Investigation of Decision Processes in Chemical Substitution Decision Making." Thesis, The George Washington University, 2021. http://pqdtopen.proquest.com/#viewpdf?dispub=28261055.
Full textDominguez, Palomeque Luis Felipe. "Investigation of robust techniques for the design of chemical processes under uncertainty." Thesis, University of Ottawa (Canada), 2007. http://hdl.handle.net/10393/27833.
Full textDrage, Michael John. "Economic trade-offs in process design." Thesis, University of Nottingham, 1992. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.334996.
Full textBrunet, Solé Robert. "Optimal design of sustainable chemical processes via a combined simulation-optimization approach." Doctoral thesis, Universitat Rovira i Virgili, 2012. http://hdl.handle.net/10803/108997.
Full textResumen La sociedad es cada día más consciente de la escasez y los cambios ambientales. Por lo que las empresas químicas tienen la necesidad de adaptarse y desarrollar procesos químicos más sostenibles. Por lo tanto, se ha creado una clara demanda dentro de la comunidad científica para desarrollar herramientas sistemáticas que consigan reducciones en el coste y en el impacto ambiental de los procesos químicos. Esta Tesis introduce un nuevo mecanismo para el diseño de procesos químicos más sostenibles. El sistema que se presenta está basado en el uso combinado de simulación de procesos, herramientas de optimización multi-objetivo, análisis económico, análisis de ciclo de vida y sistemas de soporte a la toma de decisiones. La estrategia presentada se utiliza en la resolución de problemas complejos, por lo que será también necesario desarrollar nuevos algoritmos y estrategias de descomposición para dividir el problema original, en sub-problemas más manejables, para obtener el diseño óptimo del proceso. La Tesis se presenta utilizando seis artículos que se han publicado en revistas científicas. La primera parte, que incluye dos publicaciones, está enfocada en el diseño de bioprocessos sostenibles, ya que han ganado mucho interés en el mercado debido a su alto valor. En el primer trabajo, se ha estudiado la maximización del Valor Actual Neto en la producción del amino-ácido L-lisina. El problema se formula como un problema de optimización dinámica entera mixta, solucionándolo mediante un método de descomposición que itera entre los sub-problemas esclavo y maestro. La optimización dinámica del problema esclavo es resuelta mediante un algoritmo secuencial que integra el simulador de proceso (SuperPro Designer®) con un solver de problemas de programación no lineal implementado en Matlab®. En el segundo artículo, el problema de optimización permite una resolución conjunta de los aspectos económicos y ambientales del proceso. En este caso se optimiza el Valor Actual Neto conjuntamente con diferentes indicadores ambientales. La solución del problema se presenta mediante diferentes curvas de Pareto, a las que se aplica el análisis de componentes principales. Debido a que la demanda de energía a incrementado drásticamente durante los últimos años, el análisis energético en los procesos industriales ha ganado mucho interés. Es por eso que en la segunda parte de la Tesis nos enfocamos en el diseño óptimo de ciclos termodinámicos. En esta sección se han publicado dos artículos. En el primero de esta segunda parte se presenta un método para el diseño óptimo de ciclos de absorción de amoníaco-agua, teniendo en cuenta el análisis económico y ambiental. El caso se plantea como un problema de programación no-lineal entera con múltiples objetivos. En el segundo, se aplica una estrategia similar al primero pero a diversos ciclos termodinámicos. En este trabajo se demuestran las capacidades del método con diversos ciclos termodinámicos. Entre ellos un ciclo Rankine de 10 MW simulado en Aspen Hysys® y un ciclo de absorción de amoníaco-agua de 90 kW simulado en Aspen Plus®. La producción de biocombustibles sigue creciendo a nivel mundial a una gran velocidad. En la tercera parte de la Tesis, hemos aplicado herramientas matemáticas a desarrollar procesos de producción de biocombustibles. Esta tercera parte incluye nuevamente dos publicaciones. En el primer trabajo el problema es reducir el impacto ambiental de las plantas de producción de biodiesel mediante la inclusión de paneles solares para la generación del vapor utilizado en dicha planta. Para realizar este estudio se utiliza un modelo de sistemas de energía solar en GAMS®. Este modelo se combina con un modelo de simulación riguroso en Aspen Plus® de la planta de biodiesel. En el problema el sistema de energía solar tiene en cuenta la minimización del coste y del potencial de calentamiento global. En el segundo trabajo, el problema es el diseño multi-objectivo de una planta de producción de bioetanol combinada con un sistema de paneles solares para la generación de vapor en la planta. En general, se puede considerar que la Tesis presenta un marco interesante en el ámbito del diseño optimo de procesos sostenibles. Los resultados numéricos muestran cómo es posible conseguir mejoras ambientales y económicas utilizando estos modelos rigurosos. Además, este método ha sido aplicado a diferentes tipos de procesos como: los bioprocesos, los ciclos termodinámicos y los biocombustibles. Este método será muy útil para los tomadores de decisiones a fin de evaluar la topología y las condiciones de funcionamiento en la ingeniería de proceso.
The society is every day more conscious about the scarce of resources, the global economy, and the environmental changes. Hence, chemical companies have the necessity to be adapted and develop more sustainable processes. There is a clear demanding to the scientific community to develop systematic tools to achieve reductions in the production costs as well as the associated environmental impact in order to develop decision support tools for the design of chemical plants. This thesis introduces a novel framework for the optimal design of sustainable chemical processes. Our approach combines process simulation, multi-objective optimization tools (MOO), economic analysis, life cycle assessment (LCA) and decision support systems (DSS). The developed strategy will be used to solve very complex problems. For that it will be necessary to develop new algorithms and decomposition strategies to divide the original problem in more manageable sub-problems, to obtain the optimum design of the process. The capabilities of the methodology have been tested in different processes along the Ph.D Thesis. This PhD dissertation is presented using six articles that have been published in international peer reviewed journals. The first part, which includes two publications, is focused in the development of sustainable bioprocesses, as these processes have recently gained wider interest for their potential to produce high-value products. In the first work, we studied the maximization of the Net Present Value (NPV) in the production of the amino acid L-lysine. The design task is mathematically formulated as a mixed-integer dynamic optimization (MIDO) problem, which is solved by a decomposition method that iterates between primal and master sub-problems. The dynamic optimization primal sub-problems are solved via a sequential approach that integrates the process simulator SuperPro Designer® with an external non-linear programming (NLP) solver implemented in Matlab®, while the task of the master problem is to decide on the value of the integer variables. In the second paper, the optimization allows for the simultaneous consideration of economic and environmental concerns. We optimize in this case the economic (NPV) and different environmental indicators. The solution is given by various bi-objective Pareto sets, and then we applied principal component analysis (PCA) in order to find redundant objective functions between the environmental indicators. Because the energy demand has drastically increased over the last few years, the energetic analysis of industrial processes has gained wider interest. Hence, we focused in the second part of the thesis in the optimal design of thermodynamic cycles. In this section, we published two papers. In the first article of the second part we present a method for the optimal design of ammonia-water absorption cycles for cooling and refrigeration applications with economic and environmental concerns. The design task is posed as multi-objective mixed-integer non-linear programming (MINLP). In the second article, we expand our work to different thermodynamic cycles. We demonstrate the capabilities of the approach with a 10 MW Rankine cycle simulated in Aspen Hysys® and a 90 kW ammonia-water absorption cycle in Aspen Plus®. Biofuels production worldwide is continuing to grow at very rapid pace. Hence, in the third part of the thesis, we applied the techniques developed in different biofuels production processes. This third part includes two publications. In the first work we address the problem of reducing the environmental impact of biodiesel plants through their integration with a solar thermal energy system that generates steam. A mathematical model of the solar energy system that includes energy storage is programmed and coupled with a rigorous simulation model of the biodiesel facility developed in Aspen Plus®. The solar energy system accounts for the simultaneous minimization of cost and global warming potential. In the second work, we address MOO of a corn-based bioethanol plant coupled with solar assisted steam generation system with heat storage. Our approach relies on the combined use of process simulation, rigorous optimization tools and, economic and energetic plant analysis. Overall, we can consider that this thesis presents a promising framework for the optimal design of sustainable chemical processes. Numerical results show that it is possible to achieve environmental and cost saving using this rigorous approach. Additionally, this approach has been applied in very different type of processes, such as: bioprocesses, thermodynamic cycles and biofuels. This methodology will be very useful for decision-makers in order to evaluate the topology and operating conditions in process system engineering
Al-Hwayzee, Mohammed. "Design and development of gasification processes in fluidised bed chemical reactor engineering." Thesis, Cardiff University, 2016. http://orca.cf.ac.uk/97762/.
Full textWoods, Patricia Dawn. "An investigation into chemical processes for colouring pewter and their creative application." Thesis, University of Plymouth, 2011. http://hdl.handle.net/10026.1/1234.
Full textNg, Christine Sau Ting. "A systematic approach to the design of plant-wide control strategies for chemical processes." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/10408.
Full textGao, Jianying. "Robust Control Design of Gain-scheduled Controllers for Nonlinear Processes." Thesis, University of Waterloo, 2004. http://hdl.handle.net/10012/847.
Full textUerdingen, Eric. "Retrofit design of continuous chemical processes for the improvement of production cost-efficiency /." Berlin : dissertation.de - Verlag im Internet, 2002. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=14570.
Full textAbraham, Thomas Kannankara. "Kinetic bounds on attainability in the reactor synthesis problem." Connect to resource, 2005. http://rave.ohiolink.edu/etdc/view?acc%5Fnum=osu1126791863.
Full textTitle from first page of PDF file. Document formatted into pages; contains xvi, 190 p.; also includes graphics (some col.). Includes bibliographical references (p. 182-190). Available online via OhioLINK's ETD Center
Halsall-Whitney, Hayley. "The development and application of a multi-objective optimization technique for chemical processes and controller design." Thesis, University of Ottawa (Canada), 2004. http://hdl.handle.net/10393/26649.
Full textSteimel, Jochen [Verfasser]. "Model-based Conceptual Design and Optimization of Continuous Chemical Processes under Uncertainty / Jochen Steimel." Aachen : Shaker, 2016. http://d-nb.info/1122545592/34.
Full textFeng, Zhangpeng. "Design of optimal procedural controllers for chemical processes modelled as stochastic discrete event systems." Thesis, Imperial College London, 2008. http://hdl.handle.net/10044/1/1446.
Full textPalmer, Kurt D. "Data collection plans and meta models for chemical process flowsheet simulators." Diss., Georgia Institute of Technology, 1998. http://hdl.handle.net/1853/24511.
Full textHoltbrügge, Johannes [Verfasser]. "Conceptual Design, Experimental Investigation and Economic Evaluation of Intensified Chemical and Petrochemical Processes / Johannes Holtbrügge." München : Verlag Dr. Hut, 2015. http://d-nb.info/1070124109/34.
Full textMehta, Bhavin V. "Computer aided design of streamlined dies." Ohio : Ohio University, 1988. http://www.ohiolink.edu/etd/view.cgi?ohiou1182867408.
Full textOzyurt, Burhanettin Derya. "Geographic and process information systems for multi-facility design and operation." Diss., Georgia Institute of Technology, 1999. http://hdl.handle.net/1853/11003.
Full textBrazier, Angela Jane. "Reactor design for two-liquid phase biocatalytic processes : oxidation of toulene to its cis-glycol using pseudomonas putida." Thesis, University College London (University of London), 1989. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.265115.
Full textCalmeyn, Timothy Joseph. "A design algorithm for continuous melt-phase polyester manufacturing processes optimal design, product sensitivity, and process flexibility." Ohio : Ohio University, 1998. http://www.ohiolink.edu/etd/view.cgi?ohiou1175097000.
Full textGrooms, Daniel Douglas. "Optimization of hybrid dynamic/steady-state processes using process integration." [College Station, Tex. : Texas A&M University, 2006. http://hdl.handle.net/1969.1/ETD-TAMU-1752.
Full textSwernath, Subramanian [Verfasser], and Achim [Akademischer Betreuer] Kienle. "Design and control of combined chemical processes for the production of pure enantiomers / Subramanian Swernath. Betreuer: Achim Kienle." Magdeburg : Universitätsbibliothek, 2013. http://d-nb.info/1054135274/34.
Full textGhirian, Alireza. "Coupled Thermo-Hydro-Mechanical-Chemical (THMC) Processes in Cemented Tailings Backfill Structures and Implications for their Engineering Design." Thesis, Université d'Ottawa / University of Ottawa, 2016. http://hdl.handle.net/10393/34605.
Full textHarianto, Rina. "Design of a Novel Thin Film Reactor for Photocatalytic Water Treatment Process." Miami University / OhioLINK, 2020. http://rave.ohiolink.edu/etdc/view?acc_num=miami1604335732713241.
Full textChabalenge, Billy, Sachin A. Korde, Adrian L. Kelly, Daniel Neagu, and Anant R. Paradkar. "Understanding Matrix Assisted Continuous Cocrystallisation using Data Mining approach in Quality by Design (QbD)." ACS, 2020. http://hdl.handle.net/10454/18005.
Full textThe present study demonstrates the application of decision tree algorithms to the co-crystallization process. Fifty four (54) batches of carbamazepine–salicylic acid co-crystals embedded in poly(ethylene oxide) were manufactured via hot melt extrusion and characterized by powder X-ray diffraction, differnetial scanning calorimetry, and near-infrared spectroscopy. This dataset was then applied in WEKA, which is an open-sourced machine learning software to study the effect of processing temperature, screw speed, screw configuration, and poly(ethylene oxide) concentration on the percentage of co-crystal conversion. The decision trees obtained provided statistically meaningful and easy-to-interpret rules, demonstrating the potential to use the method to make rational decisions during the development of co-crystallization processes.
Porkert, Sebastian. "Physico-Chemical Processes during Reactive Paper Sizing with Alkenyl Succinic Anhydride (ASA)." Doctoral thesis, Saechsische Landesbibliothek- Staats- und Universitaetsbibliothek Dresden, 2017. http://nbn-resolving.de/urn:nbn:de:bsz:14-qucosa-219620.
Full textGhosh, Tapajyoti. "Integrated sustainability assessment and design of processes, supply chains, ecosystems and economy using life cycle modeling methods." The Ohio State University, 2019. http://rave.ohiolink.edu/etdc/view?acc_num=osu1563480013206943.
Full textLemoine, Nava Jose Roberto [Verfasser]. "Online optimal design of experiments and parametrization of chemical processes: Application to the Simulated Moving Bed Process / Jose Roberto Lemoine Nava." Aachen : Shaker, 2018. http://d-nb.info/1188550543/34.
Full textMélykúti, Bence. "Theoretical advances in the modelling and interrogation of biochemical reaction systems : alternative formulations of the chemical Langevin equation and optimal experiment design for model discrimination." Thesis, University of Oxford, 2010. http://ora.ox.ac.uk/objects/uuid:d368c04c-b611-41b2-8866-cde16b283b0d.
Full textFernandez, Hanna, Tova Johansson, Pontus Renholm, and Alfredsson Malin Stauber. "Design och tillverkning av automatiserat bryggverk." Thesis, KTH, Skolan för kemivetenskap (CHE), 2016. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-208751.
Full textSaeed, Auday Esmail. "Integrated design of chemical plants with energy conservation (the design of an energy efficient styrene plant)." Thesis, University of South Wales, 1990. https://pure.southwales.ac.uk/en/studentthesis/integrated-design-of-chemical-plants-with-energy-conservation-the-design-of-an-energy-efficient-styrene-plant(27fb4dfc-5ed8-40ff-a747-c302c43415da).html.
Full textAbbas, A. "The integration of controllability into process design." Thesis, University of Bath, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.374607.
Full textLimin, Lin. "Concurrency in process engineering design." Thesis, University of Leeds, 1991. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.305517.
Full textSahin, Kemal Hunkar. "COMBINED SAFETY AND ECONOMIC OPTIMALITY IN CHEMICAL PROCESS DESIGN." University of Cincinnati / OhioLINK, 2000. http://rave.ohiolink.edu/etdc/view?acc_num=ucin973708026.
Full textAmar, Yehia. "Accelerating process development of complex chemical reactions." Thesis, University of Cambridge, 2019. https://www.repository.cam.ac.uk/handle/1810/288220.
Full text