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Dissertations / Theses on the topic 'Process intensification technology'

Author: Grafiati

Published: 4 June 2021

Last updated: 28 January 2023

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1

Sulu, Michael. "The process intensification of biological hydrogen production by Escherichia coli HD701." Thesis, University of Birmingham, 2010. http://etheses.bham.ac.uk//id/eprint/873/.

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Hydrogen is seen as a potential fuel for the future; its choice is driven by the increasing awareness of the necessity for clean fuel. Together with the simultaneous development of “green technologies” and sustainable development, a current goal is to convert waste to energy or to create energy from a renewable resource. Biological processing [of renewables] or bioremediation of waste to create hydrogen as a product fulfils this goal and, as such, is widely researched. In this work, an already established process, using a hydrogenase up‐regulated strain ‐ was characterised and the important pr

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2

Jassim, Majeed Safar. "Process intensification : absorption and desorption of carbon dioxide from monoethanolamine solutions using Higee technology." Thesis, University of Newcastle Upon Tyne, 2002. http://hdl.handle.net/10443/647.

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Process intensification (PI) technologies are challenging the traditional unit operations in a wide range of engineering processes. The Rotating Packed Bed (RPB) or the Higee is a compact mass transfer machine that could challenge the conventional absorption/desorption columns especially in the off-shore oil facilities where space and weight are of great importance. This counter-current mass transfer operation between the gas and the liquid phases occurs at high rotational speed and with a short residence time. The objective of the project was to test the capability of the mass transfer machin

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3

Uwinez, Clarisse. "Intensification of lignocellulosic bioethanol production process using multi-staged membrane bioreactors." Thesis, Högskolan i Borås, Akademin för textil, teknik och ekonomi, 2019. http://urn.kb.se/resolve?urn=urn:nbn:se:hb:diva-21635.

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The exploitation of lignocellulosic materials with the aim of producing high value-added products will potentially counteract concerns related to the depletion of fossil resources or exponential population growth. Bioethanol produced from lignocellulosic agriculture residue exhibits promising alternative to the petroleum-based fossil fuel which reduces net emission of greenhouse gases (GHG). But, due to certain technological barriers, the large scale production of lignocellulosic bioethanol has not been successfully commercialized. In this thesis, membrane filtration as an energy efficient sep

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4

Hu, Xinqun. "Design of a microchannel reactor for gas phase heterogeneous reactions : enhanced mass and heat transfer for process intensification." Thesis, University of Sheffield, 2001. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.246984.

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5

Mazubert, Alex. "Selection, development and design of a continuous and intensified reactor technology to transform waste cooking oil in biodiesel and biosourced formulations." Phd thesis, Toulouse, INPT, 2014. http://oatao.univ-toulouse.fr/13673/1/Mazubert.pdf.

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The objective of this thesis is to propose a continuous and intensified reactor to transform waste cooking oil into products that will be used in applications in the building and public works sector. This work is part of the FUI AGRIBTP, a collaborative research project whose finality is to the creation of an industrial tool for the reuse of co-products from agroindustries. The reactor must be able to handle transesterification and esterification (with methanol or with glycerol) reactions efficiently with a total flow rate of 100 kg/h. To achieve this objective, a literature review has identif

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6

Ma, Rui. "Development and experimental validation of a CFD model for Pd-based membrane technology in H2 separation and process intensification." Digital WPI, 2018. https://digitalcommons.wpi.edu/etd-dissertations/544.

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Syngas production and hydrogen separation technologies are very mature, and also extremely important for energy and chemical industries. Furthermore, these processes are the most expensive elements for many applications such as hydrogen production from renewable sources. Enhancing or intensifying these very mature technologies is very challenging, but would have tremendous impact on the performance and economics of many processes. Traditional Integrated Gasification Combined Cycle (IGCC) for syngas production need to include a carbon capture process in order to regulate their carbon dioxide e

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7

Bamerni, Fanar. "Plant-based (Camelina Sativa) biodiesel manufacturing using the technology of Instant Controlled pressure Drop (DIC) : process performance and biofuel quality." Thesis, La Rochelle, 2018. http://www.theses.fr/2018LAROS004/document.

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La présente étude a eu pour objectif la comparaison de la fabrication du biodiesel à partir de graines de caméline suivant les procédés conventionnels ou assistés/intensifiés par Détente Instantanée Contrôlée (DIC). La caméline est l'une des matières premières les plus adaptées à la fabrication de biodiesel puisqu’elle ne présente aucune concurrence aux cultures alimentaires et/ou à l’utilisation des terres agricoles. Son intérêt réside en sa teneur élevée en huile, sa courte saison de culture, ainsi que sa grande capacité à enrichir les sols pauvres, arides ou semi-arides. L'insertion de la t

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8

Koc, Reyyan. "Technical and Economic Performance Assessment of Pd/Alloy Membrane Reactor Technology Options in the Presence of Uncertainty." Digital WPI, 2012. https://digitalcommons.wpi.edu/etd-dissertations/108.

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A comprehensive process intensification analysis was performed for the integration of the Pd-based membrane reactor technology into IGCC power plants by designing effective process control strategies as well as identifying and optimally characterizing inherently safe operational conditions to achieve the most favorable economic outcomes. Experimental results indicated that Pd-based composite membranes supported on porous stainless steel tubes, fabricated with H2 permeance values as high as ~50 m3/[m2.h.atm0.5] at 450°C were capable of extra purity H2 production (≥99.99%). Two illustrative proc

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9

Zabot, Giovani Leone 1988. "Obtaining bioactive compounds from clove and rosemary using supercritical technology: influence of the bed geometry, process intensification and cost of manufacturing of extracts = Obtenção de compostos bioativos de cravo-da-índia e alecrim utilizando tecnologia supercrítica: influência da geometria do leito, intensificação de processos de extração e custo de manufatura dos extratos." [s.n.], 2015. http://repositorio.unicamp.br/jspui/handle/REPOSIP/254901.

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Orientador: Maria Angela de Almeida Meireles<br>Tese (doutorado) - Universidade Estadual de Campinas, Faculdade de Engenharia de Alimentos<br>Made available in DSpace on 2018-08-26T17:00:04Z (GMT). No. of bitstreams: 1 Zabot_GiovaniLeone_D.pdf: 24740321 bytes, checksum: 93e515a410574c1037b0a53340db63d2 (MD5) Previous issue date: 2015<br>Resumo: Substâncias naturais extraídas de plantas têm propriedades funcionais que as tornam preferíveis em relação às substâncias sintéticas, havendo grande interesse para aplicação farmacológica e na elaboração de bioprodutos. Técnicas de extração, como a qu

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10

Kane, Abdoulaye. "Conception et caractérisation d’un microcontacteur à film tombant : concept de distillation microstructurée." Thesis, Vandoeuvre-les-Nancy, INPL, 2010. http://www.theses.fr/2010INPL086N/document.

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Il est démontré que dans de nombreux procédés de transformation de la matière, les dégradations entropiques (et les consommations énergétiques qui en découlent) peuvent être minimisées en répartissant les flux d’énergies dans le volume plutôt qu’aux bornes du système (exemple de la distillation diabatique). Cependant la réalisation et la gestion de profils thermiques contrôlés (tels que des gradients thermiques et des étagements de température maîtrisés) dans les appareils compactes ne sont pas très souvent réalisées parce que souvent complexes et coûteuses (batterie d’échangeurs, gestion des

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11

Teng, Sin Yong. "Intelligent Energy-Savings and Process Improvement Strategies in Energy-Intensive Industries." Doctoral thesis, Vysoké učení technické v Brně. Fakulta strojního inženýrství, 2020. http://www.nusl.cz/ntk/nusl-433427.

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S tím, jak se neustále vyvíjejí nové technologie pro energeticky náročná průmyslová odvětví, stávající zařízení postupně zaostávají v efektivitě a produktivitě. Tvrdá konkurence na trhu a legislativa v oblasti životního prostředí nutí tato tradiční zařízení k ukončení provozu a k odstavení. Zlepšování procesu a projekty modernizace jsou zásadní v udržování provozních výkonů těchto zařízení. Současné přístupy pro zlepšování procesů jsou hlavně: integrace procesů, optimalizace procesů a intenzifikace procesů. Obecně se v těchto oblastech využívá matematické optimalizace, zkušeností řešitele a pr

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12

Le, Page Mostefa Marie. "Développement, conception et mise au point d'un procédé de purification du bio-acide acrylique par cristallisation en milieu fondu." Thesis, Université de Lorraine, 2012. http://www.theses.fr/2012LORR0302/document.

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Actuellement produit à partir du pétrole, une voie de synthèse de l'acide acrylique (AA) à partir du glycérol est envisagée. Cependant, cet AA bio-sourcé contient davantage d'acide propionique (AP) que l'AA issu du propylène. Les techniques classiques de purification ne permettent pas de séparer les deux acides. Le diagramme de phases liquide-solide du binaire AA + AP est déterminé. Il présente un point eutectique à 25,65 % (mol) d'AA, un point péritectique à 50,00 % (mol) d'AA et donc, un large domaine dans lequel l'AA cristallise thermodynamiquement de façon pure. Les essais de purification

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13

Zaidiza, David Ricardo Albarracin. "Modelling of Hollow Fibre Membrane Contactors : Application to Post-combustion Carbon Dioxide Capture." Thesis, Université de Lorraine, 2016. http://www.theses.fr/2016LORR0035/document.

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La capture du dioxyde de carbone (CO2) en postcombustion est une stratégie importante pour la limitation de l’effet de serre. Le procédé de référence est l’absorption du CO2 dans des solutions aqueuses aminées, suivie par une étape de stripage du solvant. La technologie mature associée à ce procédé est la colonne à garnissage. Toutefois, afin de rendre le procédé plus attractif, il convient de l’intensifier en réduisant le volume des équipements et le coût énergétique associé. Les contacteurs membranaires à fibres creuses (CMFC) constituent une alternative aux colonnes à garnissage. Les CMFC p

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14

Dias, Lígia Beatriz Sá Azevedo. "Steam Methane Reforming: Process Intensification through NETmix® Technology." Master's thesis, 2018. https://hdl.handle.net/10216/113835.

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15

Dias, Lígia Beatriz Sá Azevedo. "Steam Methane Reforming: Process Intensification through NETmix® Technology." Dissertação, 2018. https://hdl.handle.net/10216/113835.

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16

Dias, Lígia Beatriz Sá Azevedo. "Steam Methane Reforming: Process Intensification through NETmix® Technology." Dissertação, 2002. https://repositorio-aberto.up.pt/handle/10216/113835.

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17

Liu, Yu-Bin, and 劉育儐. "Preliminary Study of Electrolysis System Development with Process Intensification Technology." Thesis, 2018. http://ndltd.ncl.edu.tw/handle/7wchsp.

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18

Coelho, Frederico Silva. "Intensification of the Fischer-Tropsch Process through the NETmix® Technology." Master's thesis, 2018. https://hdl.handle.net/10216/113877.

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19

Coelho, Frederico Silva. "Intensification of the Fischer-Tropsch Process through the NETmix® Technology." Dissertação, 2018. https://hdl.handle.net/10216/113877.

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20

Coelho, Frederico Silva. "Intensification of the Fischer-Tropsch Process through the NETmix® Technology." Dissertação, 2002. https://repositorio-aberto.up.pt/handle/10216/113877.

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21

Santos, Bruno André Vilela dos. "Process Intensification in the Synthesis of the Green Chemical Dimethyl Carbonate." Doctoral thesis, 2014. https://repositorio-aberto.up.pt/handle/10216/76949.

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22

Santos, Bruno André Vilela dos. "Process Intensification in the Synthesis of the Green Chemical Dimethyl Carbonate." Tese, 2014. https://repositorio-aberto.up.pt/handle/10216/76949.

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23

(8065976), Kanjakha Pal. "Process Intensification Enabling Direct Compression for Pharmaceutical Manufacturing: From Spherical Agglomeration to Precise Control of Co-Agglomeration." Thesis, 2019.

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Spherical agglomeration (SA) is a novel process intensification strategy for particulate manufacturing. In the context of pharmaceutical manufacturing, it has the potential to reduce the number of unit operations in downstream processing from seven to three, which significantly reduces the manufacturing cost. However, SA process development for a new API in the drug pipeline is still a challenging exercise, which has impeded its practical implementation. The major bottleneck lies in the lack of fundamental understanding of the mechanistic principles underlying agglomeration of primary crystals

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24

Constantino, Dânia Sofia Martins. "Process Intensification for Butyl Acrylate Synthesis based on Sorption-Enhanced Reaction and Pervaporation-based Hybrid Processes." Doctoral thesis, 2019. https://hdl.handle.net/10216/123266.

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25

Constantino, Dânia Sofia Martins. "Process Intensification for Butyl Acrylate Synthesis based on Sorption-Enhanced Reaction and Pervaporation-based Hybrid Processes." Tese, 2019. https://hdl.handle.net/10216/123266.

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