Literatura académica sobre el tema "Protein fouling"
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Artículos de revistas sobre el tema "Protein fouling"
Peiris, R. H., H. Budman, R. L. Legge y C. Moresoli. "Assessing irreversible fouling behavior of membrane foulants in the ultrafiltration of natural water using principal component analysis of fluorescence excitation-emission matrices". Water Supply 11, n.º 2 (1 de abril de 2011): 179–85. http://dx.doi.org/10.2166/ws.2011.025.
Texto completoYan, Linlin, Ruixue Li, Yu Song, Yanping Jia, Zheng Li, Lianfa Song y Haifeng Zhang. "Characterization of the Fouling Layer on the Membrane Surface in a Membrane Bioreactor: Evolution of the Foulants’ Composition and Aggregation Ability". Membranes 9, n.º 7 (16 de julio de 2019): 85. http://dx.doi.org/10.3390/membranes9070085.
Texto completoChen, Yian, Montserrat Rovira-Bru, Francesc Giralt y Yoram Cohen. "Hydraulic Resistance and Protein Fouling Resistance of a Zirconia Membrane with a Tethered PVP Layer". Water 13, n.º 7 (31 de marzo de 2021): 951. http://dx.doi.org/10.3390/w13070951.
Texto completoSun, Chunyi, Na Zhang, Fazhan Li, Guoyi Ke, Lianfa Song, Xiaoqian Liu y Shuang Liang. "Quantitative Analysis of Membrane Fouling Mechanisms Involved in Microfiltration of Humic Acid–Protein Mixtures at Different Solution Conditions". Water 10, n.º 10 (22 de septiembre de 2018): 1306. http://dx.doi.org/10.3390/w10101306.
Texto completoMiyoshi, Taro, Yuhei Nagai, Tomoyasu Aizawa, Katsuki Kimura y Yoshimasa Watanabe. "Proteins causing membrane fouling in membrane bioreactors". Water Science and Technology 72, n.º 6 (2 de junio de 2015): 844–49. http://dx.doi.org/10.2166/wst.2015.282.
Texto completoScudeller, Luisa A., Pascal Blanpain-Avet, Thierry Six, Séverine Bellayer, Maude Jimenez, Thomas Croguennec, Christophe André y Guillaume Delaplace. "Calcium Chelation by Phosphate Ions and Its Influence on Fouling Mechanisms of Whey Protein Solutions in a Plate Heat Exchanger". Foods 10, n.º 2 (27 de enero de 2021): 259. http://dx.doi.org/10.3390/foods10020259.
Texto completoBuchori, Luqman, Heru Susanto y Budiyono Budiyono. "SINTESIS MEMBRAN ULTRAFILTRASI NON FOULING UNTUK APLIKASI PEMPROSESAN BAHAN PANGAN". Reaktor 13, n.º 1 (3 de febrero de 2010): 10. http://dx.doi.org/10.14710/reaktor.13.1.10-15.
Texto completoBerg, Thilo H. A., Jes C. Knudsen, Richard Ipsen, Frans van den Berg, Hans H. Holst y Alexander Tolkach. "Investigation of Consecutive Fouling and Cleaning Cycles of Ultrafiltration Membranes Used for Whey Processing". International Journal of Food Engineering 10, n.º 3 (1 de septiembre de 2014): 367–81. http://dx.doi.org/10.1515/ijfe-2014-0028.
Texto completoPeiris, R. H., M. Jaklewicz, H. Budman, R. L. Legge y C. Moresoli. "Characterization of hydraulically reversible and irreversible fouling species in ultrafiltration drinking water treatment systems using fluorescence EEM and LC–OCD measurements". Water Supply 13, n.º 5 (1 de septiembre de 2013): 1220–27. http://dx.doi.org/10.2166/ws.2013.130.
Texto completoChaipetch, Wiparat, Arisa Jaiyu, Panitan Jutaporn, Marc Heran y Watsa Khongnakorn. "Fouling Behavior in a High-Rate Anaerobic Submerged Membrane Bioreactor (AnMBR) for Palm Oil Mill Effluent (POME) Treatment". Membranes 11, n.º 9 (25 de agosto de 2021): 649. http://dx.doi.org/10.3390/membranes11090649.
Texto completoTesis sobre el tema "Protein fouling"
Alharthi, Majed. "Fouling and cleaning studies of protein fouling at pasteurisation temperatures". Thesis, University of Birmingham, 2014. http://etheses.bham.ac.uk//id/eprint/4892/.
Texto completoGotham, Simon Martyn. "Mechanisms of protein fouling of heat exchangers". Thesis, University of Cambridge, 1990. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.357741.
Texto completoChan, Robert Chemical Engineering & Industrial Chemistry UNSW. "Fouling mechanisms in the membrane filtration of single and binary protein solutions". Awarded by:University of New South Wales. Chemical Engineering and Industrial Chemistry, 2002. http://handle.unsw.edu.au/1959.4/18832.
Texto completoHuang, Yunqi. "Design and Evaluation of a Laboratory-Scale System for Investigation of Fouling during Thermal Processing Operation". The Ohio State University, 2017. http://rave.ohiolink.edu/etdc/view?acc_num=osu1494245242027853.
Texto completoProdan, Bjorg Noah Radu. "Modifying Membrane Surfaces via Self-Assembled Monolayers to Reduce Protein Fouling". University of Cincinnati / OhioLINK, 2004. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1091133289.
Texto completoRAJAM, SRIDHAR. "TWO SURFACE MODIFICATION METHODS TO REDUCE PROTEIN FOULING IN MICROFILTRATION MEMBRANES". University of Cincinnati / OhioLINK, 2007. http://rave.ohiolink.edu/etdc/view?acc_num=ucin1172005034.
Texto completoRose, Ian C. "Model investigation of initial fouling rates of protein solutions in heat transfer equipment". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1999. http://www.collectionscanada.ca/obj/s4/f2/dsk1/tape8/PQDD_0026/NQ38965.pdf.
Texto completoHamilton-Brown, Paul Optometry & Vision Science Faculty of Science UNSW. "A surface forces and protein adsorption study of grafted PEO layers". Awarded by:University of New South Wales. School of Optometry and Vision Science, 2006. http://handle.unsw.edu.au/1959.4/25541.
Texto completoMagens, Ole Mathis. "Mitigating fouling of heat exchangers with fluoropolymer coatings". Thesis, University of Cambridge, 2019. https://www.repository.cam.ac.uk/handle/1810/287467.
Texto completoSuwal, Shyam y Shyam Suwal. "Fractionation of Peptides from Protein Hydrolysate by Electrodialysis with Filtration Membrane : process optimization, Fouling characterization and Control mechanisms". Doctoral thesis, Université Laval, 2015. http://hdl.handle.net/20.500.11794/26619.
Texto completoDes peptides bioactifs ont déjà été fractionnés par électrodialyse avec membrane de filtration (ÉDMF) à partir d’hydrolysats de sous-produits de crabe des neiges. L’optimisation des paramètres apparaît maintenant indispensable pour perfectionner le procédé. Ainsi, le taux de migration des peptides, leur sélectivité et l'évolution des paramètres électrodialytiques ont été étudiés pour différents paramètres (configuration, concentration en KCl et types de champ électrique). La configuration (2) de la cellule d’ÉDMF comprenant deux compartiments d'alimentation et un compartiment de récupération a démontré des valeurs de champ électrique local relativement stables par rapport à la configuration (1) constituée d’un compartiment d’alimentation et de deux compartiments de récupération. Des peptides contenant des glutamates, des aspartates, et des glycines ont été séparés avec la configuration 1 et des peptides composés d’arginines et de lysines avec la configuration 2. Un taux de migration peptidique de 13,76 ± 3,64 g/m2h a été obtenu par le maintien constant de la conductivité des solutions. La sélectivité a été accrue en augmentant la concentration en KCl de 1 à 5 g/L dans le compartiment de récupération. Une augmentation de la force ionique a amplifié la charge de surface, agrandissant ainsi la taille effective des pores et réduisant la couche d'hydratation de la membrane d’ultrafiltration. Toutefois, les membranes échangeuses d’anions et de cations ont été colmatées par des peptides et des acides aminés et détériorées pendant l’ÉDMF. Pour résoudre ces problèmes, l’effet de l’application du champ électrique pulsé (PEF) et de l'inversion de polarité (PR) a été étudié. Le taux de migration des peptides n'a pas été affecté sauf avec PR à 40 V. La sélectivité a été maximale avec PEF à 20 V. La dissociation de l'eau a été réduite tout en conservant les propriétés physico-chimiques des membranes grâce à l’application du PEF et de la PR par rapport au courant continu (DC). En outre, la plus faible quantité d'énergie a été consommée avec le PEF. Par conséquent, il a été possible d’optimiser la technologie d’ÉDMF du point de vue de l’efficacité énergétique, de la sélectivité peptidique et de l’encrassement membranaire grâce à l’application du PEF et tout en maintenant la conductivité électrique des solutions.
Bioactive peptides were efficiently separated by using electrodialysis with filtration membrane (EDFM) from snow crab byproduct hydrolysate. Meanwhile, optimization of parameters is indispensable for scaling-up. The peptide migration rate and selectivity as well as evolution of electrodialytic parameters were studied with different parameters such as EDFM cell configuration, KCl concentration and type of electric field. The EDFM stack with two feed and one recovery compartments (configuration 2) has relatively stable electric field strengths (local) than the configuration with one feed and two recovery compartments (configuration 1). Peptides containing anionic amino acids: glutamic and aspartic acid as well as glycine and cationic amino acids: arginine and lysine were fractionated using configuration 1 and 2, respectively. Maintenance of solution conductivity upheld the local electric field and peptide migration throughout the treatment resulting in a higher peptide migration rate of 13.76±3.64 g/m2.h never observed so far. The selectivity of cationic peptides containing arginine and lysine increased significantly with increase in KCl concentration from 1 to 5 g/L. An increase in ionic strength amplified the surface charge density of filtration membrane subsequently increasing effective pore size and reducing hydration layer. However, both anion- and cation-exchange membranes were fouled by peptides and amino acids and were deteriorated during EDFM treatment. To address these problems, the effect of applying pulsed electric field (PEF) and polarity reversal (PR) was studied. The peptide migration rate was unaffected among PEF, PR and DC modes except with PR at 40 V. The selectivity of cationic peptides was maximum with PEF at 20 V. Fouling and water dissociation were significantly reduced and physicochemical properties of IEMs were better-protected with PEF and PR than DC. Moreover, the least amount of energy was consumed with PEF mode. Therefore, the parameters affecting EDFM process were optimized in terms of energy efficiency, selectivity and lower deterioration of membranes by applying PEF regime with configuration 2 and maintaining the constant electrical conductivity of solutions.
Bioactive peptides were efficiently separated by using electrodialysis with filtration membrane (EDFM) from snow crab byproduct hydrolysate. Meanwhile, optimization of parameters is indispensable for scaling-up. The peptide migration rate and selectivity as well as evolution of electrodialytic parameters were studied with different parameters such as EDFM cell configuration, KCl concentration and type of electric field. The EDFM stack with two feed and one recovery compartments (configuration 2) has relatively stable electric field strengths (local) than the configuration with one feed and two recovery compartments (configuration 1). Peptides containing anionic amino acids: glutamic and aspartic acid as well as glycine and cationic amino acids: arginine and lysine were fractionated using configuration 1 and 2, respectively. Maintenance of solution conductivity upheld the local electric field and peptide migration throughout the treatment resulting in a higher peptide migration rate of 13.76±3.64 g/m2.h never observed so far. The selectivity of cationic peptides containing arginine and lysine increased significantly with increase in KCl concentration from 1 to 5 g/L. An increase in ionic strength amplified the surface charge density of filtration membrane subsequently increasing effective pore size and reducing hydration layer. However, both anion- and cation-exchange membranes were fouled by peptides and amino acids and were deteriorated during EDFM treatment. To address these problems, the effect of applying pulsed electric field (PEF) and polarity reversal (PR) was studied. The peptide migration rate was unaffected among PEF, PR and DC modes except with PR at 40 V. The selectivity of cationic peptides was maximum with PEF at 20 V. Fouling and water dissociation were significantly reduced and physicochemical properties of IEMs were better-protected with PEF and PR than DC. Moreover, the least amount of energy was consumed with PEF mode. Therefore, the parameters affecting EDFM process were optimized in terms of energy efficiency, selectivity and lower deterioration of membranes by applying PEF regime with configuration 2 and maintaining the constant electrical conductivity of solutions.
Libros sobre el tema "Protein fouling"
Office, General Accounting. Drinking water: Stronger efforts needed to protect areas around public wells from contamination : report to the chairman, Environment, Energy, and Natural Resources Subcommittee, Committee on Government Operations, House of Representatives. Washington, D.C: GAO, 1993.
Buscar texto completoCapítulos de libros sobre el tema "Protein fouling"
Le-Clech, Pierre. "Protein Fouling". En Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2014. http://dx.doi.org/10.1007/978-3-642-40872-4_1706-1.
Texto completoLe-Clech, Pierre. "Protein Fouling Mechanisms". En Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2014. http://dx.doi.org/10.1007/978-3-642-40872-4_1707-1.
Texto completoJohansson, J., H. K. Yasuda y R. K. Bajpai. "Fouling and Protein Adsorption". En Biotechnology for Fuels and Chemicals, 747–63. Totowa, NJ: Humana Press, 1998. http://dx.doi.org/10.1007/978-1-4612-1814-2_69.
Texto completoFuller, K. L. y S. G. Roscoe. "Surface adsorption of dairy proteins: Fouling of model surfaces". En Protein Structure-Function Relationships in Foods, 143–62. Boston, MA: Springer US, 1994. http://dx.doi.org/10.1007/978-1-4615-2670-4_7.
Texto completoZydney, Andrew L. "Non-Specific Protein-Membrane Interactions: Adsorption and Fouling". En Biofunctional Membranes, 279–88. Boston, MA: Springer US, 1996. http://dx.doi.org/10.1007/978-1-4757-2521-6_19.
Texto completoReed, I. M. y J. M. Sheldon. "Investigation of Protein Fouling Characteristics of Ultrafiltration Membranes". En Effective Industrial Membrane Processes: Benefits and Opportunities, 91–99. Dordrecht: Springer Netherlands, 1991. http://dx.doi.org/10.1007/978-94-011-3682-2_6.
Texto completoReed, I. M. y J. M. Sheldon. "Protein Fouling and its Implications for Selection for Ultrafiltration Membranes". En Separations for Biotechnology 2, 217–26. Dordrecht: Springer Netherlands, 1990. http://dx.doi.org/10.1007/978-94-009-0783-6_24.
Texto completoBenavente, Juana. "Use of Streaming Potential Measurements for Characterization of Both Membrane/Electrolyte Interface and Protein Fouling Effect". En Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2014. http://dx.doi.org/10.1007/978-3-642-40872-4_765-3.
Texto completoBenavente, Juana. "Use of Streaming Potential Measurements for Characterization of Both Membrane/Electrolyte Interface and Protein Fouling Effect". En Encyclopedia of Membranes, 1957–58. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-44324-8_765.
Texto completo"Membrane Fouling". En Protein Bioseparation Using Ultrafiltration, 47–55. PUBLISHED BY IMPERIAL COLLEGE PRESS AND DISTRIBUTED BY WORLD SCIENTIFIC PUBLISHING CO., 2003. http://dx.doi.org/10.1142/9781860949388_0005.
Texto completoActas de conferencias sobre el tema "Protein fouling"
Agarwal, Ashutosh, Parag Katira y Henry Hess. "Quantifying and understanding protein adsorption to non-fouling surfaces". En 2010 36th Annual Northeast Bioengineering Conference. IEEE, 2010. http://dx.doi.org/10.1109/nebc.2010.5458217.
Texto completoSmith, Karl J. P., Joshua Winans y James McGrath. "Ultrathin Membrane Fouling Mechanism Transitions in Dead-End Filtration of Protein". En ASME 2016 14th International Conference on Nanochannels, Microchannels, and Minichannels collocated with the ASME 2016 Heat Transfer Summer Conference and the ASME 2016 Fluids Engineering Division Summer Meeting. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/icnmm2016-7989.
Texto completoLee, Yi Jae, Jung Doo Kim y Jae Yeong Park. "Nafion coated enzyme free glucose micro-biosensors for anti-fouling of protein". En 2009 4th IEEE International Conference on Nano/Micro Engineered and Molecular Systems. IEEE, 2009. http://dx.doi.org/10.1109/nems.2009.5068590.
Texto completoLiu, Yanjun, Huiying Ma, Chunying Lv, Jia Yang y Xueqi Fu. "Protein absorption and fouling on poly(acrylic acid)-graft-polypropylene microfiltration membrane". En Second International Conference on Smart Materials and Nanotechnology in Engineering, editado por Jinsong Leng, Anand K. Asundi y Wolfgang Ecke. SPIE, 2009. http://dx.doi.org/10.1117/12.840154.
Texto completoHuang, Guobang, Yi Chen y Jin Zhang. "Nanocomposite coating produced by laser-assisted process to prevent bacterial contamination and protein fouling". En 2014 IEEE 14th International Conference on Nanotechnology (IEEE-NANO). IEEE, 2014. http://dx.doi.org/10.1109/nano.2014.6967984.
Texto completoAmeli, Forough, Bahram Dabir, Farzin Zokaee Ashtiani, Mehdad Mozaffarian y Kambiz Vafai. "Combined Models of Population Balance and Pore-Network to Explore the Mechanism of Protein Fouling in Porous Media". En POROUS MEDIA AND ITS APPLICATIONS IN SCIENCE, ENGINEERING, AND INDUSTRY: 3rd International Conference. AIP, 2010. http://dx.doi.org/10.1063/1.3453812.
Texto completoHsieh, Yi-Cheng, Huinan Liang y Jeffrey D. Zahn. "Microdevices for Microdialysis and Membrane Separations". En ASME 2003 International Mechanical Engineering Congress and Exposition. ASMEDC, 2003. http://dx.doi.org/10.1115/imece2003-55052.
Texto completoParsons, Edward L., Holmes A. Webb y Charles M. Zeh. "Assessment of Hot Gas Cleanup Technologies in Coal-Fired Gas Turbines". En ASME 1990 International Gas Turbine and Aeroengine Congress and Exposition. American Society of Mechanical Engineers, 1990. http://dx.doi.org/10.1115/90-gt-111.
Texto completoMody, Jaisen, Roman Saveliev, Ezra Bar-Ziv y Miron Perelman. "Selection of Biomass Feedstock for Production of Biocoal for Coal-Fired Boilers". En ASME 2014 Power Conference. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/power2014-32031.
Texto completoZhou, Dengji, Tingting Wei, Shixi Ma, Huisheng Zhang, Zhenhua Lu y Shilie Weng. "A Whole Operation Life Cycle Model of Gas Turbine Blades Under Multi-Physics Based on Variation of Blade Profile Parameters". En ASME 2018 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2018. http://dx.doi.org/10.1115/imece2018-87040.
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