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1

Galagali, Nikhil. "Bayesian inference of chemical reaction networks." Thesis, Massachusetts Institute of Technology, 2016. http://hdl.handle.net/1721.1/104253.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2016.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (pages 189-198).<br>The development of chemical reaction models aids system design and optimization, along with fundamental understanding, in areas including combustion, catalysis, electrochemistry, and biology. A systematic approach to building reaction network models uses available data not only to estimate unknown parameters, but to also learn the model structure. Bayesian inference provides a natural approach for
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2

Rowe, Stephen Michael. "The use of reaction inhibition techniques for control of runaway polymerisation reactions." Thesis, London South Bank University, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.336802.

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3

Keskin-Schneider, Aliye. "Engineering reaction kinetics in sulfite and sulfite-anthraquinone pulping." Thesis, McGill University, 1991. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=70207.

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In this study, engineering reaction kinetics of sulfite and sulfite-anthraquinone pulping of black spruce wood are investigated. The considered sulfite processes are neutral-sulfite (NS), neutral sulfite-anthraquinone (NS-AQ), neutral sulfite semichemical (NSSC) and neutral sulfite semichemical anthraquinone (NSSC-AQ).<br>In preliminary studies, an experimental design was tested and optimum kinetic conditions were found so that penetration and diffusion would not be the rate-controlling steps and the amount of anthraquinone would not be reaction limiting.<br>Delignification and carbohydrate de
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4

Gao, Connie W. (Connie Wu). "Automatic reaction mechanism generation :." Thesis, Massachusetts Institute of Technology, 2016. http://hdl.handle.net/1721.1/104205.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2016.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references.<br>Growing awareness of climate change and the risks associated with our society's dependence on fossil fuels has motivated global initiatives to develop economically viable, renewable energy sources. However, the transportation sector remains a major hurdle. Although electric vehicles are becoming more mainstream, the transportation sector is expected to continue relying heavily on combustion engines, particularly in
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5

Akintoye, Ayodele. "Continuous chromatographic biochemical reaction-separation." Thesis, Aston University, 1989. http://publications.aston.ac.uk/9739/.

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Combined bioreaction separation studies have been carried out for the first time on a moving port semi-continuous counter-current chromatographic reactor-separator (SCCR-S1) consisting of twelve 5.4cm id x 75cm long columns packed with calcium charged cross-linked polystyrene resin (KORELA V07C). The inversion of sucrose to glucose and fructose in the presence of the enzyme invertase and the biochemIcal synthesis of dextran and fructose from sucrose in the presence of the enzyme dextransucrase were investigated. A dilute stream of the appropriate enzyme in deionised water was used as the eluen
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6

Knight, Daniel William. "Reactor behavior and its relation to chemical reaction network structure." The Ohio State University, 2015. http://rave.ohiolink.edu/etdc/view?acc_num=osu1438274630.

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7

Serbetcioglu, Serpil. "Mass transfer and catalytic reaction in a three-phase monolith reactor." Thesis, University of Bath, 1993. https://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.332665.

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8

Lekakou, Constantina. "Simulation of flow, reaction and heat transfer in reaction injection moulding." Thesis, Imperial College London, 1987. http://hdl.handle.net/10044/1/47048.

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9

Mamtani, Kuldeep. "Carbon-based Materials for Oxygen Reduction Reaction (ORR) and Oxygen Evolution Reaction (OER) in Acidic Media." The Ohio State University, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=osu149376896628355.

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10

Nadeau, Patrice. "Study of the mixing with chemical reaction in a cross flow impinging jet aerosol reactor." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape3/PQDD_0029/NQ64625.pdf.

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11

Adhikari, Sudip. "Accelerating the Computation of Chemical Reaction Kinetics for Modeling Turbulent Reacting Flows." University of Akron / OhioLINK, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=akron1510259399348102.

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12

Holmes, R. "Reaction kinetics of oil coke particles." Thesis, University of Portsmouth, 1987. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.376048.

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13

Byrne, C. S. C. "The modelling of a reaction and reactor for the electrochemical production of geraniol and nerol." Thesis, University of Newcastle Upon Tyne, 1986. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.371252.

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14

Losey, Matthew W. "Novel multiphase chemical reaction systems enabled by microfabrication technology." Thesis, Massachusetts Institute of Technology, 2001. http://hdl.handle.net/1721.1/8634.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2001.<br>Includes bibliographical references (p. 237-251).<br>Advances in MEMS (micro-electromechanical systems) have enabled some of the "Lab-on-a-Chip" technologies and microfluidics that are pervasive in many of the current developments in analytical chemistry and molecular biology. Coinciding with this effort in micro-analytics has been research in chemical process miniaturization -- reducing the characteristic length scale of the unit operation to improve heat and mass transfer, and ultimately process p
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15

Stafford, Daniel Edward 1975. "System analysis and metabolic engineering of biocatalytic reaction networks : application to indene bioconversion." Thesis, Massachusetts Institute of Technology, 2002. http://hdl.handle.net/1721.1/8271.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2002.<br>Includes bibliographical references (leaves 149-165).<br>Metabolic engineering is a science concerned with the improvement of cellular properties through the application of recombinant DNA technology. To this point, the field has frequently been limited to methodological issues pertaining to gene introduction, expression and control by way of molecular biological techniques. While such methods are critical for the implementation of strategies for metabolic pathway design and modification, an equally
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16

Street, David Alan. "Computational modelling of the stirred reaction vessels." Thesis, University of Leeds, 1991. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.305422.

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17

Karaman, Mustafa. "Chemical Vapor Deposition Of Boron Carbide." Phd thesis, METU, 2007. http://etd.lib.metu.edu.tr/upload/3/12608778/index.pdf.

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Boron carbide was produced on tungsten substrate in a dual impinging-jet CVD reactor from a gas mixture of BCl3, CH4, and H2. The experimental setup was designed to minimise the effect of mass transfer on reaction kinetics, which, together with the on-line analysis of the reactor effluent by FTIR, allowed a detailed kinetic investigation possible. The phase and morphology studies of the products were made by XPS, XRD,micro hardness and SEM methods. XPS analysis showed the existence of chemical states attributed to the boron carbide phase, together with the existence of oxy-boron carbide speci
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18

Petway, Sarah V. (Sarah Victoria). "Uncertainty analysis in automatic reaction mechanism generation : neopentyl + O₂." Thesis, Massachusetts Institute of Technology, 2006. http://hdl.handle.net/1721.1/37580.

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Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2006.<br>Includes bibliographical references (leaves 38-44).<br>The process of building accurate chemical mechanisms for hydrocarbon oxidation systems is difficult since these mechanisms can have hundreds of species and thousands of reactions. Computer programs have recently been developed to construct these models automatically, but until this work, these programs did not include tools for the propagation of uncertainty. Rate constants and thermodynamic properties are not known precisely, and this can lead to
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19

Magoon, Gregory Russell. "Automated reaction mechanism generation : improving accuracy and broadening scope." Thesis, Massachusetts Institute of Technology, 2012. http://hdl.handle.net/1721.1/76484.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2012.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (p. 169-186).<br>Chemical kinetic modeling plays an important role in the study of reactive chemical systems. Thus, an automated means of constructing chemical kinetic models forms a useful tool in the engineering and science surrounding such systems. This document describes work to further develop one such tool, known as RMG (Reaction Mechanism Generator). Focus is placed on improving the accuracy of parameter estimation i
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20

Chen, Bo 1970. "Diffusion and reaction of nitric oxide in cell cultures." Thesis, Massachusetts Institute of Technology, 2001. http://hdl.handle.net/1721.1/8205.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2001.<br>Includes bibliographical references (leaves 196-212).<br>Nitric oxide (NO) is synthesized throughout the body and its intercellular signalling and other functions are necessary for health. However, its mutagenic effects make it a potential cause of cancer, if it is produced at a high enough rate for a sufficient time. Sustained overproduction of NO may occur, for example, in macrophages as part of the immune response to certain chronic infections. The mutagenic effects of NO are thought to be due la
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21

Schwan, Peter. "Transient analysis of diffusion and adsorption under reaction conditions." Doctoral thesis, University of Cape Town, 2001. http://hdl.handle.net/11427/5404.

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Bibliography: leaves 145-153.<br>The aim of this thesis is to measure diffusion and adsorption of hydrocarbons under reaction and non-reaction conditions in a jetloop reactor using a pulse technique. The jetloop is a recycle reactor approximating a CSTR. Cumene cracking to benzene and propene was chosen as test reaction. A key question in this thesis was, whether model parameters are theoretically measurable and what errors can be expected and how this information is applied in practice.
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22

Cook, Andrew Simon. "Chiral porphyrazines and the asymmetric Baylis-Hillman reaction." Thesis, Imperial College London, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.286227.

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23

O'Rourke, David John. "The use of calorimetry to study reaction kinetics." Thesis, London South Bank University, 1996. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.388168.

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24

Kim, Seok-Jhin. "High Temperature Water Gas Shift Reaction in Zeolite Membrane Reactors." University of Cincinnati / OhioLINK, 2011. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1321888491.

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25

Ciccolini, Rocco P. "Carbon-nitrogen bond-forming reactions in supercritical and expanded-liquid carbon dioxide media : green synthetic chemistry with multiscale reaction and phase behavior modeling." Thesis, Massachusetts Institute of Technology, 2008. http://hdl.handle.net/1721.1/43203.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2008.<br>Includes bibliographical references.<br>The goal of this work was to develop a detailed understanding of carbon-nitrogen (C-N) bond-forming reactions of amines carried out in supercritical and expanded-liquid carbon dioxide (CO2) media. Key motivations behind this study were the importance of nitrogen-containing compounds in the pharmaceutical and fine chemical industries and a growing commercial interest in utilizing environmentally-friendly syntheses and processing with cost-efficient, green solve
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26

Hannon, J. "Mixing and chemical reaction in tubular reactors and stirred tanks." Thesis, Cranfield University, 1992. http://dspace.lib.cranfield.ac.uk/handle/1826/11368.

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Fluid flow patterns and turbulence levels are instrumental in determining chemical reactor performance. Parameters such as stirrer type and size, fluid physical properties, chemical species concentrations and flow rates can strongly influence the safety, efficiency and reliability of reactors, with consequent cost implications. In this project, Computational Fluid Dynamics has been used to obtain insight into the characteristics of tubular and stirred tank chemical reactors. Attention is focused on single phase liquid isothermal turbulent flows. Turbulence theory is used to select and develop
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27

Flynn, Mary Patricia. "The settling characteristics of bauxite particles after acid reaction." Thesis, Queen's University Belfast, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.356914.

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28

Snow, Michael Jeffrey Hegarty. "The sulfation of limestone and calcium oxide : direct and series reaction." Thesis, Massachusetts Institute of Technology, 1985. http://hdl.handle.net/1721.1/60722.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1986.<br>MICROFICHE COPY AVAILABLE IN ARCHIVES AND SCIENCE.<br>Bibliography: leaves 211-218.<br>by Michael Jeffrey Hegarty Snow.<br>Ph.D.
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29

Anantharaman, Bharthwaj. "Reaction mechanisms for catalytic partial oxidation systems : application to ethylene epoxidation." Thesis, Massachusetts Institute of Technology, 2005. http://hdl.handle.net/1721.1/32328.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2005.<br>Includes bibliographical references.<br>With the rapid advances in kinetic modeling, building elementary surface mechanisms have become vital to understand the complex chemistry for catalytic partial oxidation systems. Given that there is selected experimental knowledge on surface species and a large number of unknown thermochemical, rate parameters, the challenge is to integrate the knowledge to identify all the important species and accurately estimate the parameters to build a detailed surface me
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30

Harper, Michael Richard Jr. "Automated reaction mechanism generation : data collaboration, Heteroatom implementation, and model validation." Thesis, Massachusetts Institute of Technology, 2011. http://hdl.handle.net/1721.1/65756.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2011.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (p. 281-292).<br>Nearly two-thirds of the United States' transportation fuels are derived from non-renewable fossil fuels. This demand of fossil fuels requires the United States to import ~ 60% of its total fuel consumption. Relying so heavily on foreign oil is a threat to national security, not to mention that burning all of these fossil fuels produces increased levels of CO₂, a greenhouse gas that contributes to global wa
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31

Yin, Wenbin. "Reaction Mechanism of Carbon and Methane on the Anode of SOFC." University of Akron / OhioLINK, 2014. http://rave.ohiolink.edu/etdc/view?acc_num=akron1398778152.

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32

Daya, Yatish Surendra. "Performance of gold reference catalysts in the water gas shift reaction." Master's thesis, University of Cape Town, 2007. http://hdl.handle.net/11427/5373.

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33

Jovanovic, Renata. "Butyl acrylate/vinyl acetate emulsion copolymerization: Reaction monitoring and property evaluation." Thesis, University of Ottawa (Canada), 2001. http://hdl.handle.net/10393/9102.

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Several aspects of butyl acrylate/vinyl acetate (BA/VAc) polymerizations were investigated in this thesis. Polymerization process monitoring is a key factor in obtaining high quality products with prespecified properties. Therefore, a considerable part of this work was devoted to the real-time monitoring of BA/VAc emulsion polymerization reactions. An Attenuated Total Reflectance - Fourier Transform Infrared (ATR-FTIR) spectroscopy sensor was used for monitoring conversion and copolymer composition. Due to the novelty of this technique, in the first part of the study, the suitability of this t
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34

Chan, Martin Siu Chun. "Chemical looping for selective oxidations." Thesis, University of Cambridge, 2019. https://www.repository.cam.ac.uk/handle/1810/290408.

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This Dissertation describes the development of chemical looping for selective oxidations. Chemical looping is a reactor technology that achieves simultaneous reaction and separation. For a large subset of reactions (viz. abstraction or insertion of oxygen), this technology is based upon the use of oxygen carriers. These materials, typically metal oxides, reversibly store and release oxygen, and there is growing interest in using these materials for selective oxidations. This Dissertation describes work on the development of oxygen carriers for selective oxidations, including foundational work
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35

Demeter, Ethan L. "The Promotion of Base Metal Catalysts for the Electrochemical Oxygen Evolution Reaction." Research Showcase @ CMU, 2013. http://repository.cmu.edu/dissertations/236.

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As the energy needs of society continue to grow, and pressure to produce fewer emissions continues to mount, clean alternatives will be utilized to meet these demands. Conventional renewable technologies (wind and solar, etc.) have great potential, but cannot be used as base-load power, at least not in the traditional sense. Rather, these technologies would require the further adoption of energy storage technologies, such as water splitting, to convert the energy produced into chemical bonds for later use to match demand. Water splitting currently suffers from large energetic barriers, on the
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36

McMullen, Jonathan Patrick. "Automated microreactor system for reaction development and online optimization of chemical processes." Thesis, Massachusetts Institute of Technology, 2010. http://hdl.handle.net/1721.1/62064.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2010.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (p. 162-175).<br>Developing the optimal conditions for chemical reactions that are common in fine chemical and pharmaceutics is a difficult and expensive task. Because syntheses in these fields have multiple reaction pathways, a significant number of experiments are required to determine the conditions that maximize the yield of the desired product. With few exceptions, these experiments have been performed in flask reactor
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37

Arnold, John Christopher 1964. "Material transport and reaction effects in surface typography evolution during plasma etching." Thesis, Massachusetts Institute of Technology, 1995. http://hdl.handle.net/1721.1/38041.

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38

Taylor, Joshua D. "Hydrothermal chemistry of methylene chloride and MTBE : experimental kinetics and reaction pathways." Thesis, Massachusetts Institute of Technology, 2001. http://hdl.handle.net/1721.1/16753.

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Thesis (Ph.D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2001.<br>Includes bibliographical references.<br>This electronic version was submitted by the student author. The certified thesis is available in the Institute Archives and Special Collections.<br>With the growing desire for sustainable technologies, reactions in benign solvents, such as hydrothermal water and supercritical fluids, have become the focus of many investigations. Hydrothermal water has been used as a medium for chemical reactions, where the enhanced dissociation constant of water led to both a
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39

Mihopoulos, Theodoros 1969. "Reaction and transport processes in OMCVD : selective and group III-nitride growth." Thesis, Massachusetts Institute of Technology, 1999. http://hdl.handle.net/1721.1/9655.

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Thesis (Ph.D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1999.<br>Includes bibliographical references.<br>Researchers have continued to explore light sources that are brighter, cheaper, more reliable, and emit light closer to natural sunlight than conventional incandescent and fluorescent lighting. The most recent advance in this direction is the fabrication of light emitting diodes (LEDs), and laser diodes that can emit in the short wavelength region of the visible spectrum (from green to violet). By using organometallic chemical vapor deposition (OMCVD) to fabric
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40

Allen, Andrew J. (Andrew John) 1978. "Green chemistry : dense carbon dioxide and water as environmentally benign reaction media." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/28656.

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Thesis (S.M.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2004.<br>Includes bibliographical references.<br>(cont.) was investigated in scCO₂, and the cycloaddition between cyclopentadiene and methyl vinyl ketone (MVK) was studied in an scCO₂/liquid water environment. Nitrogen chemistry, specifically the synthesis of nitrogen heterocycles from amines, was also studied in scCO₂ and scCO₂/liquid water systems. The objective of studying the Diels-Alder cycloaddition of 9-hydroxymethylanthracene with N-ethylmaleimide in scCO₂ was to demonstrate the ability of scCO₂ to dra
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41

Mahajan, Sayalee G. (Sayalee Girish). "Improving efficiency of ID thermopower wave devices and studying 2D reaction waves." Thesis, Massachusetts Institute of Technology, 2015. http://hdl.handle.net/1721.1/101509.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2015.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (pages 124-127).<br>With growing energy consumption, current research in the field is focused on improving and developing alternatives for energy storage and conversion. Factors such as efficiency of energy conversion, usability of this converted form of energy, power density, energy density etc. help us in determining the right energy source or conversion technology for any specific application. The main aim of this th
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42

Song, Jing 1972. "Building robust chemical reaction mechanisms : next generation of automatic model construction software." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/30058.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2004.<br>Includes bibliographical references (p. 308-319).<br>Building proper reaction mechanisms is crucial to model the system dynamic properties for many industrial processes with complex chemical reaction phenomena. Because of the complexity of a reaction mechanism, computer-aided reaction mechanism generation software appeared in recent years to help people efficiently build large reaction mechanisms. However, the limitations of those programs, such as not being able to model different types of reaction
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43

Trevino, Lisandro. "Mold Filling Analysis of Structural Reaction Injection Molding and Resin Transfer Molding." The Ohio State University, 1990. http://rave.ohiolink.edu/etdc/view?acc_num=osu1392736921.

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44

Fortuin, Adrian Charles. "Development of a semi–empirical reaction kinetic model for PEM fuel cells." Master's thesis, University of Cape Town, 2013. http://hdl.handle.net/11427/5334.

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In the drive to more sustainable energy production, polymer electrolyte fuel cells (PEFC) have been at the pinnacle of global research. One of the major drawbacks of PEFCs is therequirement for expensive noble metal catalysts (platinum and ruthenium). Furthermore 75% of the overpotential losses at the cathode are due to the activation of the oxygen reduction reaction (ORR). To reduce the platinum content requirements and understand the cause of the large overpotential of the ORR, a fundamental understanding of the reaction mechanism and the manner in which it proceeds under different operating
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45

Baig, Fakhir U. "Effects of interfacial reaction on oil displacement in a Hele-Shaw cell." Thesis, University of Ottawa (Canada), 1993. http://hdl.handle.net/10393/7666.

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An experimental study was conducted to examine the behaviour of reactive and non-reactive systems by displacement experiments of light paraffin oil/decane mixtures by water in a range of mobility ratios. Displacement experiments were performed in a Hele-Shaw cell, simulated a quarter of a reversed five-spot pattern. Displacement patterns produced by reactive and non-reactive systems were compared. It showed that the displacement patterns in the case of the reactive system were completely different from the non-reactive system. The recovery in the reactive system was always higher than in the n
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46

Lau, Ivan T. "Char particle reaction and attrition in fluidized bed combustors: Modelling and measurement." Thesis, University of Ottawa (Canada), 1995. http://hdl.handle.net/10393/10129.

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Two slightly different models for predicting combustion efficiency for burning coal chars in bubbling fluidized bed combustors are developed. The models proposed assume that char particles are consumed simultaneously by combustion reaction and attrition with the rates of both processes following the shrinking particle model. To solve the gas-solid reaction problem, an approach quite different from the traditional method has been attempted. Characteristic times are introduced based on mean residence time concepts to characterize the reaction and attrition kinetics and particle size of different
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47

Cenci, Steven Michael. "Acoustic agitation of dense carbon dioxide/water mixtures : emulsification, mass transfer, and reaction engineering." Thesis, University of Birmingham, 2014. http://etheses.bham.ac.uk//id/eprint/5381/.

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Acoustic agitation of a carbon dioxide/water mixture in a 1 dm3 cylindrical, high-pressure reactor led to the simultaneous formation of carbon dioxide/water (C/W) and water/carbon dioxide (W/C) emulsions, with the dispersed phase occupying up to 10% of the volume. These emulsions were stable for several minutes. Inclusion of 1% of the non-ionic surfactant Tween 80 led to the generation of C/W emulsions which were stable for over 1 hour after ceasing sonication, in which all of the carbon dioxide present in the system comprised the dispersed phase. The mixing capacity of pulsed ultrasound was a
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48

Timko, Michael T. 1974. "Acoustic emulsions of liquid, near-critical carbon dioxide and water : application to synthetic chemistry through reaction engineering." Thesis, Massachusetts Institute of Technology, 2004. http://hdl.handle.net/1721.1/29375.

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Thesis (Ph. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 2004.<br>Includes bibliographical references.<br>Supervised by The need to eliminate hazardous solvents, such as methanol, toluene, and dichloromethane, in specialty and pharmaceutical chemical synthesis applications has motivated the development of alternative approaches. Because of its environmental compatibility, low cost, and favorable physicochemical properties, supercritical carbon dioxide (scCO2) has been actively considered to replace conventional hydrocarbon solvents. Progress towards this objective
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49

Amanchukwu, Chibueze Vincent. "Probing of reaction mechanisms, and development of polymeric materials for lithium-air batteries." Thesis, Massachusetts Institute of Technology, 2017. http://hdl.handle.net/1721.1/111419.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2017.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (pages 184-194).<br>Limiting the use of fossil fuels is vital to stemming climate change. Incorporation of renewable energy technologies into the grid, and the shift to electric vehicles for transportation increases the need for better energy storage media. Lithium-air (O₂) batteries are of great interest because they have high theoretical energy densities. However, conventional Li-O₂ batteries face challenges such as t
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50

Reizman, Brandon Jacob. "Automated feedback in flow for accelerated reaction screening, optimization, and kinetic parameter estimation." Thesis, Massachusetts Institute of Technology, 2015. http://hdl.handle.net/1721.1/98712.

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Thesis: Ph. D., Massachusetts Institute of Technology, Department of Chemical Engineering, 2015.<br>Cataloged from PDF version of thesis.<br>Includes bibliographical references (pages 164-184).<br>With the cost to discover and develop a drug now estimated to exceed $2 billion, the pharmaceutical industry is in search of innovative and cost-effective ways to reduce process footprint, minimize lead times, and accelerate scale-up. One path to achieving these goals is in the adoption of continuous processing. Among the many advantages offered by the use of continuous flow systems is the ease of in
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