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Artykuły w czasopismach na temat "Ultrafiltration"
Tay, Kirsty Luo-Yng, Abdel Rahman Osman, Esyn Ee Xin Yeoh, Jasmine Luangboriboon, Jie Fei Lau, Joanne Jia An Chan, Majed Yousif i in. "Ultrafiltration versus Diuretics on Prognostic Cardiac and Renal Biomarkers in Acute Decompensated Heart Failure: A Systematic Review and Meta-Analysis". Journal of Clinical Medicine 12, nr 8 (9.04.2023): 2793. http://dx.doi.org/10.3390/jcm12082793.
Pełny tekst źródłaPetterson, Craig M., Alfred H. Stammers, Ryan J. Kohtz, Scott A. Kmiecik, Jeffrey D. Nichols, Nancy J. Mills i Jun-Li Liu. "The Effects of Ultrafiltration on e-Aminocaproic Acid: An In Vitro Analysis". Journal of ExtraCorporeal Technology 34, nr 3 (wrzesień 2002): 197–202. http://dx.doi.org/10.1051/ject/2002343197.
Pełny tekst źródłaHan, You Qi, De Ming Zhu, Zhou Kong Su i Wen Xiang Ding. "Ultrafiltration in Pediatric Cardiac Surgical Procedures". Journal of ExtraCorporeal Technology 23, nr 3 (wrzesień 1991): 63–65. http://dx.doi.org/10.1051/ject/199123363.
Pełny tekst źródłaMing, Zhu De, Wang Wei, Chen Hong, Zhang Wei i Ding Wen Xiang. "Balanced Ultrafiltration, Modified Ultrafiltration, and Balanced Ultrafiltration with Modified Ultrafiltration in Pediatric Cardiopulmonary Bypass". Journal of ExtraCorporeal Technology 33, nr 4 (grudzień 2001): 223–26. http://dx.doi.org/10.1051/ject/2001334223.
Pełny tekst źródłaSoat, Marian. "Ultrafiltration". Nursing Management (Springhouse) 39, nr 1 (styczeń 2008): 48–49. http://dx.doi.org/10.1097/01.numa.0000305993.07980.51.
Pełny tekst źródłaBourge, Robert C., i José A. Tallaj. "Ultrafiltration". Journal of the American College of Cardiology 46, nr 11 (grudzień 2005): 2052–53. http://dx.doi.org/10.1016/j.jacc.2005.09.014.
Pełny tekst źródłaBabka, Ronald M., James Petress, Richard Briggs, Robert Helsel i John Mack. "Conventional haemofiltration during routine coronary bypass surgery". Perfusion 12, nr 3 (maj 1997): 187–92. http://dx.doi.org/10.1177/026765919701200307.
Pełny tekst źródłaBabenyshev, S. P., V. E. Zhidkov, D. S. Mamay, V. P. Utkin i N. A. Shapakov. "ULTRAFILTRATION OF MODIFIED MILK WHEY". Food and Raw Materials 4, nr 2 (30.12.2016): 101–10. http://dx.doi.org/10.21179/2308-4057-2016-2-101-110.
Pełny tekst źródłaLazarev, Sergey I., Yuri V. Golovin, Irina V. Khorokhorina, Sergey V. Kovalev i Alexandr A. Levin. "KINETIC AND STRUCTURAL CHARACTERISTICS OF ULTRAFILTRATIONAL MEMBRANES AT SEPARATION OF SOLUTIONS CONTAINING SODIUM LAURYLSULPHATE". IZVESTIYA VYSSHIKH UCHEBNYKH ZAVEDENII KHIMIYA KHIMICHESKAYA TEKHNOLOGIYA 62, nr 10 (29.10.2019): 89–95. http://dx.doi.org/10.6060/ivkkt.20196210.6031.
Pełny tekst źródłaLiu, Shu Xing, i Bei Wang. "Purification of Ferulic Acid from Wheat by Ultrafiltration Technology". Advanced Materials Research 524-527 (maj 2012): 2294–97. http://dx.doi.org/10.4028/www.scientific.net/amr.524-527.2294.
Pełny tekst źródłaRozprawy doktorskie na temat "Ultrafiltration"
Vaidya, A. M. "Ultrafiltration modelling". Thesis, University of Manchester, 1989. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.237688.
Pełny tekst źródłaRakotoarisoa, Herivola Henri. "Influence d'un promoteur de turbulence fluidisé en ultrafiltration et électro-ultrafiltration". Grenoble INPG, 1986. http://www.theses.fr/1986INPG0107.
Pełny tekst źródłaGhosh, Raja. "Protein fractionation using ultrafiltration". Thesis, University of Oxford, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.302133.
Pełny tekst źródłaBANZI, ALBERT. "Concentration de lactoserum par ultrafiltration". Toulouse 3, 1986. http://www.theses.fr/1986TOU30042.
Pełny tekst źródłaBanzi, Albert. "Concentration du lactosérum par ultrafiltration". Grenoble 2 : ANRT, 1986. http://catalogue.bnf.fr/ark:/12148/cb37595695f.
Pełny tekst źródłaFarzanehsa, Seyedeh Zahra. "Decolourisation of Molasses by Ultrafiltration". Thesis, The University of Sydney, 2018. http://hdl.handle.net/2123/18596.
Pełny tekst źródłaRamli, Nor Hanuni. "Ultrafiltration of polydisperse colloidal silica". Thesis, Swansea University, 2012. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.678552.
Pełny tekst źródłaDemessie, Berhanu. "Ultrafiltration of Partially Degraded Starch Solution". Doctoral thesis, Norwegian University of Science and Technology, Faculty of Natural Sciences and Technology, 2002. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-30.
Pełny tekst źródłaDesizing wastewater is largely responsible for the chemical oxygen demand (COD) load in the textile industry wastewater. A larger portion of COD comes from degraded starch in desizing wastewater. Removing the starch from the wastewater by an ultrafiltration process may reduce the environmental problem caused by the textile factory. If the treatment is made in such a way that all starch components are removed from the wastewater, the treated water can be reused by the factory. If the starch in the concentrate is stable, it can also be reused as a sizing agent. This will give the factory an economic advantage.
In this thesis we have studied the fouling mechanisms involved in the ultrafiltration of solution with partially degraded starch in order to find the treatibility of such solutions. The work has mainly been directed to uncover how the different fouling mechanisms depend on the operating parameters, and to find the performance of selected membranes. In addition, different models were evaluated for their validity in predicting the performance of the membranes and the data was fitted to the model that give the best prediction and are physically more meaningful. In addition, the starch solution was concentrated, and the flux, concentration, retention and rejection profiles as a function of concentrating time were investigated.
For the study, we used a partially degraded starch solution as a model solution. The solution was prepared in the laboratory by enzymatic degradation of potato starch to different levels. In order to evaluate the reproducibility of the degraded starch, three replicates were prepared. The reproducibility was determined by comparing the molar mass distribution from HPLSEC analysis and the concentration of reducing sugar from a DNS test for the replicates. The analyses show very good reproducibility. Three starch model solutions with three different degradation levels were chosen for our ultrafiltration experiments to investigate the effect of average molar mass of the starch.
For the ultrafiltration of the solution ES625 (from PCI) and MPT-U20 (from KOCH) membranes were used. Both membranes were used in the investigation of the contribution of different fouling mechanisms to the flux decline during ultrafiltration of the solution. In the evaluation of the performance of ultrafiltration of the starch solution, however, only the ES625 membrane was used. According to the manufacturers, both membranes have nearly equal pure water flux and MWCO. But in our test, we observed a higher and different pure water flux for each type of membrane. The ES625 had a lower flux (higher retention) than the MPTU20 membrane.
In the ultrafiltration of partially degraded starch solution the permeate flux declines very fast and, for a low feed concentration, it reaches a steady state in a very short time. The steady state time was observed to increase with concentration, molar mass and transmembrane pressure drop, and to decrease with cross flow velocity. All the three fouling mechanisms (concentration polarization, adsorption and deposition) were responsible for the flux decline. The major observed contributors are, however, adsorption and deposition. Adsorption is largely responsible at low-pressure operation while the deposition fouling effect is dominant at higher pressures, near or beyond the limiting flux.
For the ES625 membrane, the contribution of adsorptive fouling increases with concentration and decreases with molar mass of the starch, temperature and pH at a given transmembrane pressure and cross flow velocity. The effect of the operating parameters on the depositional fouling is in line with literature. It increases with pressure, concentration, molar mass and temperature, and decreases with cross flow velocity. Its dependence on pressure can be expressed by a power function with exponent larger than 1.0. This seems to due to an increase in thickness and compaction of the starch gel/deposit at the membrane surface as the transmembrane pressure drop is increased. The contribution of the concentration polarization is also dependent on concentration, cross flow velocity and pressure. Its relative contribution increases with concentration while it decreases with an increase in cross flow velocity. In the turbulent flow regime the relation between the resistance contributed by concentration polarization increases almost linearly with transmembrane pressure drop. In the laminar flow regime, however, the relative contribution of the resistance due to concentration polarization increases for the lower range of pressure and decreases for the higher range of pressure. Its relative contribution also increases with temperature and decreases with increasing molar mass. But the overall fouling resistance in the ultrafiltration of the starch solution increases with feed concentration, molar mass of the starch and transmembrane pressure drop and decreases with cross flow velocity and temperature.
The trend of the flux loss due to all fouling mechanisms for MPT-U20 membrane is similar to ES625 membrane except for adsorption and concentration polarization with changes in concentration and molar mass. The difference could be a result of the difference in morphological properties between the two membranes and the experimental procedures used in determining flux data that used for calculating the contributions. From the pure water flux and the retention data, the ES625 membrane seemed to have a smaller pore size than the MPT-U20 membrane.
Among the ultrafiltration models, the resistances-in-series model was chosen for its provision to include all the fouling mechanisms into the model. When our permeate flux data was fitted to the model, it gives a good fit. However, the model fails to give realistic estimates of the contribution of the individual fouling mechanisms. In order to improve this problem, the model was modified by introducing osmotic pressure across the membrane in such a way that the effect of concentration polarization is accounted for. This modified model is more physically meaningful and gives a realistic estimate of the contribution the reversible and irreversible fraction of the overall resistance.
In concentrating mode operation, the permeate was continuously withdrawn and hence, the concentration of starch in the feed tank was increased. At an early stage of ultrafiltration, the permeate flux appeared to increase slightly, which seems, a result a shear thinning of the starch solution when the solution was pumped through the system. For the rest of the operation, the flux was decreasing, the retention was increasing and the rejection of the membrane was shifted to a lower molar mass as the solution in the feed tank got more concentrated as expected. The shift of rejection to the lower molar mass region is due to the fouling layer that reduces the accessibility of the pores of the membrane.
Generally, the flux we obtained in ultrafiltration of a partially degraded starch solution with the ES625 tubular membrane is equal or better than the reported values from an existing ultrafiltration plant that has been used in the textile industry to recover a synthetic sizing agent (PVA) from the desizing wastewater. The retention is, however, rather low. Two or more stages of treatment are needed to get all starch components removed from the wastewater and make the treated water reusable (recycled).
Turkson, Abraham K. "Electro-ultrafiltration with rotating dynamic membranes". Thesis, McGill University, 1985. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=72036.
Pełny tekst źródłaFour dynamic membranes, Zr(IV) oxide, calcium oleate, poly-2-vinylpyridine and cadmium sulfide, were used to filter bovine serum albumin (BSA) in a disodium phosphate solution at pH = 8 and Prussian blue in distilled water. Prussian blue is a particle of 0.01(mu)m diameter with a zeta potential of -41mV while BSA is a macromolecule of 69,000 molecular weight, a Stokes-Einstein radius of 0.0038(mu)m and a zeta potential of -23.3mV at pH = 8. For BSA, the flux declined with time while the rejection increased. Filtrate fluxes increased with rotation rate and electric field and declined with concentration for both feeds. The flux declined beyond N = 2000rpm and was constant above C(,0) = 5.0wt%. For Prussian blue, the rejection was greater than 90% at all levels of E, N and C(,0). For BSA, the rejection increased with rotation rate and declined with concentration. The BSA rejection declined above N = 2000rpm and was constant beyond C(,0) = 0.5wt%.
A mathematical model was derived to predict the time variation of filtrate flux and a rejection model was used to predict the effect of surface concentration on BSA rejection.
Vasan, S. S. "Analysis of mass transfer in ultrafiltration". Thesis, University of Oxford, 2005. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.424738.
Pełny tekst źródłaKsiążki na temat "Ultrafiltration"
Sourirajan, S., i Takeshi Matsuura, red. Reverse Osmosis and Ultrafiltration. Washington, D.C.: American Chemical Society, 1985. http://dx.doi.org/10.1021/bk-1985-0281.
Pełny tekst źródłaMunir, Cheryan, red. Ultrafiltration and microfiltration handbook. Lancaster, Pa: Technomic Pub. Co., 1998.
Znajdź pełny tekst źródłaS, Sourirajan, Matsuura Takeshi 1936-, American Chemical Society. Division of Industrial and Engineering Chemistry. i American Chemical Society Meeting, red. Reverse osmosis and ultrafiltration. Washington, D.C: American Chemical Society, 1985.
Znajdź pełny tekst źródła1936-, Matsuura Takeshi, i National Research Council Canada, red. Reverse osmosis, ultrafiltration process principles. Ottawa, Canada: National Research Council Canada, 1985.
Znajdź pełny tekst źródłaSourirajan, S. Reverse osmosis/ultrafiltration process principles. Ottawa, Canada: National Research Council Canada, 1985.
Znajdź pełny tekst źródłaSourirajan, S. Reverse osmosis: Ultrafiltration process principles. Ottawa, [Ontario]: National Research Council Canada, 1985.
Znajdź pełny tekst źródłaHanft, Susan. Ultrafiltration membrane industry: Developments, markets. Norwalk, CT: Business Communications Co., 2002.
Znajdź pełny tekst źródłaBanzi, Albert. Concentration du lactoserum par ultrafiltration. Grenoble: A.N.R.T, Université Pierre Mendes France (Grenoble II), 1986.
Znajdź pełny tekst źródłaSourav, Mondal, red. Micellar enhanced ultrafiltration: Fundamentals & applications. Boca Raton, FL: Taylor & Francis, 2012.
Znajdź pełny tekst źródłaBryk, M. T. Ulʹtrafilʹtrat͡s︡ii͡a︡. Kiev: Nauk. dumka, 1989.
Znajdź pełny tekst źródłaCzęści książek na temat "Ultrafiltration"
Xirouchaki, Nektaria, Dimitrios Georgopoulos, Keith Boniface, Venkatesh Bellamkonda-Athmaram, Lindsay E. Nicolle, Sean M. Bagshaw, Ambica Parmar i in. "Ultrafiltration". W Encyclopedia of Intensive Care Medicine, 2345. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-00418-6_3359.
Pełny tekst źródłaLin, S. Y. "Ultrafiltration". W Methods in Lignin Chemistry, 518–23. Berlin, Heidelberg: Springer Berlin Heidelberg, 1992. http://dx.doi.org/10.1007/978-3-642-74065-7_37.
Pełny tekst źródłaAptel, Philippe, i Michael Clifton. "Ultrafiltration". W Synthetic Membranes: Science, Engineering and Applications, 249–305. Dordrecht: Springer Netherlands, 1986. http://dx.doi.org/10.1007/978-94-009-4712-2_10.
Pełny tekst źródłaShrikhande, A. J., i S. A. Kupina. "Ultrafiltration". W ACS Symposium Series, 197–218. Washington, DC: American Chemical Society, 1993. http://dx.doi.org/10.1021/bk-1993-0536.ch011.
Pełny tekst źródłaGooch, Jan W. "Ultrafiltration". W Encyclopedic Dictionary of Polymers, 930. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_15044.
Pełny tekst źródłaMishra, Munmaya, i Biao Duan. "Ultrafiltration". W The Essential Handbook of Polymer Terms and Attributes, 246–47. Boca Raton: CRC Press, 2024. http://dx.doi.org/10.1201/9781003161318-229.
Pełny tekst źródłaLutz, Herb. "Ultrafiltration (UF)". W Encyclopedia of Membranes, 1947–48. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-44324-8_1206.
Pełny tekst źródłaLutz, Herb. "Ultrafiltration Applications". W Encyclopedia of Membranes, 1948–49. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-44324-8_1207.
Pełny tekst źródłaDuke, Mikel, i Todor Vasiljevic. "Whey Ultrafiltration". W Encyclopedia of Membranes, 2035–36. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-44324-8_2053.
Pełny tekst źródłaMujais, S., i W. Smit. "Ultrafiltration Failure". W Nolph and Gokal’s Textbook of Peritoneal Dialysis, 505–22. Boston, MA: Springer US, 2009. http://dx.doi.org/10.1007/978-0-387-78940-8_17.
Pełny tekst źródłaStreszczenia konferencji na temat "Ultrafiltration"
Jordhamo, George M., Ian Melville i Ann M. Mewherter. "Photoresist ultrafiltration optimization". W 23rd Annual International Symposium on Microlithography. SPIE, 1998. http://dx.doi.org/10.1117/12.312475.
Pełny tekst źródłaBilstad, T., E. Espedal, A. H. Haaland i M. Madland. "Ultrafiltration of Oily Wastewater". W SPE Health, Safety and Environment in Oil and Gas Exploration and Production Conference. Society of Petroleum Engineers, 1994. http://dx.doi.org/10.2118/27136-ms.
Pełny tekst źródłaZhou, Nina, i A. G. Agwu Nnanna. "Parametric Study of Ultrafiltration". W ASME 2009 International Mechanical Engineering Congress and Exposition. ASMEDC, 2009. http://dx.doi.org/10.1115/imece2009-11696.
Pełny tekst źródłaDuignan, Mark R., i Si Y. Lee. "Cross-Flow Ultrafiltration Scaling Considerations". W ASME 2006 2nd Joint U.S.-European Fluids Engineering Summer Meeting Collocated With the 14th International Conference on Nuclear Engineering. ASMEDC, 2006. http://dx.doi.org/10.1115/fedsm2006-98492.
Pełny tekst źródłaAryanti, Nita, Vania Frimasgita Giraldi, Heru Susanto, Tutuk Djoko Kusworo, I. Nyoman Widiasa i Nur Rokhati. "Model of fouling mechanism in ultrafiltration and micellar-enhanced ultrafiltration membrane for reactive dye removal". W THE 2ND INTERNATIONAL SYMPOSIUM OF INDONESIAN CHEMICAL ENGINEERING 2021: Enhancing Innovations and Applications of Chemical Engineering for Accelerating Sustainable Development Goals. AIP Publishing, 2023. http://dx.doi.org/10.1063/5.0118033.
Pełny tekst źródłaDas, Supriyo, Elbir Jové Alvarez i Neville Lange. "Offshore Ultrafiltration with Multi Element Vessels". W Offshore Technology Conference. Offshore Technology Conference, 2016. http://dx.doi.org/10.4043/27116-ms.
Pełny tekst źródłaKresnowati, M. T. A. P., Ria Desiriani i I. G. Wenten. "Ultrafiltration of hemicellulose hydrolysate fermentation broth". W ENGINEERING INTERNATIONAL CONFERENCE (EIC) 2016: Proceedings of the 5th International Conference on Education, Concept, and Application of Green Technology. Author(s), 2017. http://dx.doi.org/10.1063/1.4976888.
Pełny tekst źródłaFarnand, Brian, i Tom Krug. "Oilfield Produced Water Treatment By Ultrafiltration". W Technical Meeting / Petroleum Conference of The South Saskatchewan Section. Petroleum Society of Canada, 1987. http://dx.doi.org/10.2118/ss-87-15.
Pełny tekst źródłaShanti Bhushan i Mark R Etzel. "Charged Ultrafiltration Membranes for Protein Separation". W 2007 Minneapolis, Minnesota, June 17-20, 2007. St. Joseph, MI: American Society of Agricultural and Biological Engineers, 2007. http://dx.doi.org/10.13031/2013.22870.
Pełny tekst źródłaAosai, Daisuke, Yuhei Yamamoto i Takashi Mizuno. "Development of New Ultrafiltration Techniques Maintaining In-Situ Hydrochemical Conditions for Colloidal Study". W ASME 2010 13th International Conference on Environmental Remediation and Radioactive Waste Management. ASMEDC, 2010. http://dx.doi.org/10.1115/icem2010-40074.
Pełny tekst źródłaRaporty organizacyjne na temat "Ultrafiltration"
Steffani, C., i M. Meltzer. Alkaline detergent recycling via ultrafiltration. Office of Scientific and Technical Information (OSTI), czerwiec 1995. http://dx.doi.org/10.2172/104336.
Pełny tekst źródłaFarnand, B., i T. Krug. Oilfield produced water treatment by ultrafiltration. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/302687.
Pełny tekst źródłaScamehorn, J., i S. Christian. A study of micellar-enhanced ultrafiltration. Office of Scientific and Technical Information (OSTI), listopad 1989. http://dx.doi.org/10.2172/5554436.
Pełny tekst źródłaRussell, Renee L., Justin M. Billing, Reid A. Peterson, Donald E. Rinehart i Harry D. Smith. Development and Demonstration of Ultrafiltration Simulants. Office of Scientific and Technical Information (OSTI), luty 2009. http://dx.doi.org/10.2172/963208.
Pełny tekst źródłaWeisbrod, K. R., A. R. Schake, A. N. Morgan, G. M. Purdy, H. E. Martinez i T. O. Nelson. Ultrafiltration evaluation with depleted uranium oxide. Office of Scientific and Technical Information (OSTI), marzec 1998. http://dx.doi.org/10.2172/658159.
Pełny tekst źródłaSmiley, G. T., i H. Dettman. Analysis of ultrafiltration permeate (centrifuged produced water sample). Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1991. http://dx.doi.org/10.4095/304487.
Pełny tekst źródłaSedath, R. H., S. F. Yates i N. N. Li. Reduced fouling of ultrafiltration membranes via surface fluorination. Office of Scientific and Technical Information (OSTI), marzec 1993. http://dx.doi.org/10.2172/6695060.
Pełny tekst źródłaZamecnik, J. R. AN-102 Simulant Sr/TRU Precipitation and Ultrafiltration. Office of Scientific and Technical Information (OSTI), kwiecień 2003. http://dx.doi.org/10.2172/810556.
Pełny tekst źródłaSedath, R. H., S. F. Yates i N. N. Li. Reduced fouling of ultrafiltration membranes via surface fluorination. Office of Scientific and Technical Information (OSTI), marzec 1993. http://dx.doi.org/10.2172/10130600.
Pełny tekst źródłaN. R. Mann, R. S. Herbst, T. G. Garn, M. R. Poirier i S. D. Fink. Alternative Ultrafiltration Membrane Testing for the SRS Baseline Process. Office of Scientific and Technical Information (OSTI), czerwiec 2004. http://dx.doi.org/10.2172/911211.
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