Literatura académica sobre el tema "Cumene"
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Artículos de revistas sobre el tema "Cumene"
Young, Jay A. "Cumene". Journal of Chemical Education 83, n.º 7 (julio de 2006): 989. http://dx.doi.org/10.1021/ed083p989.
Texto completoYang, Wei-Jun, Can-Cheng Guo, Neng-Ye Tao y Jun Cao. "Aerobic oxidation of cumene to cumene hydroperoxide catalyzed by metalloporphyrins". Kinetics and Catalysis 51, n.º 2 (marzo de 2010): 194–99. http://dx.doi.org/10.1134/s0023158410020047.
Texto completoShen, Hai M., Hong L. Ye, Qin Wang, Meng Y. Hu, Lei Liu y Yuan B. She. "Efficient oxidation of cumene to cumene hydroperoxide with ambient O2 catalyzed by metalloporphyrins". Journal of Porphyrins and Phthalocyanines 25, n.º 04 (31 de marzo de 2021): 314–22. http://dx.doi.org/10.1142/s1088424621500310.
Texto completoDi Somma, Ilaria, Raffaele Marotta, Roberto Andreozzi y Vincenzo Caprio. "Detailed thermal and kinetic modeling of cumene hydroperoxide decomposition in cumene". Process Safety and Environmental Protection 91, n.º 4 (julio de 2013): 262–68. http://dx.doi.org/10.1016/j.psep.2012.07.001.
Texto completoDuh, Y. S., C. S. Kao, C. Lee y S. W. Yu. "Runaway Hazard Assessment of Cumene Hydroperoxide From the Cumene Oxidation Process". Process Safety and Environmental Protection 75, n.º 2 (mayo de 1997): 73–80. http://dx.doi.org/10.1205/095758297528832.
Texto completoMatsui, S. y T. Fujita. "New cumene-oxidation systems". Catalysis Today 71, n.º 1-2 (noviembre de 2001): 145–52. http://dx.doi.org/10.1016/s0920-5861(01)00450-3.
Texto completoIshida, T. y T. Matsumoto. "Enantioselective metabolism of cumene". Xenobiotica 22, n.º 11 (enero de 1992): 1291–98. http://dx.doi.org/10.3109/00498259209053157.
Texto completoHou, Ching T., Thomas A. Seymour y Marvin O. Bagby. "Microbial oxidation of cumene". Journal of Industrial Microbiology 13, n.º 2 (marzo de 1994): 97–102. http://dx.doi.org/10.1007/bf01584105.
Texto completoHsu, Ying Fang y Cheu Pyeng Cheng. "Polymer supported catalyst for the effective autoxidation of cumene to cumene hydroperoxide". Journal of Molecular Catalysis A: Chemical 120, n.º 1-3 (junio de 1997): 109–16. http://dx.doi.org/10.1016/s1381-1169(96)00442-6.
Texto completoLiao, Shixia, Feng Peng, Hao Yu y Hongjuan Wang. "Carbon nanotubes as catalyst for the aerobic oxidation of cumene to cumene hydroperoxide". Applied Catalysis A: General 478 (mayo de 2014): 1–8. http://dx.doi.org/10.1016/j.apcata.2014.03.024.
Texto completoTesis sobre el tema "Cumene"
Lu, Yuan. "Reaction mechanism of cumene hydroperoxide decomposition in cumene and evaluation of its reactivity hazards". [College Station, Tex. : Texas A&M University, 2008. http://hdl.handle.net/1969.1/ETD-TAMU-2904.
Texto completoTuli, Leepika. "Proteome Profiling of Saccharomyces cerevisae stress response to Cumene Hydroperoxide (CHP)". Diss., Virginia Tech, 2008. http://hdl.handle.net/10919/28620.
Texto completoPh. D.
Hurgobin, Sooviraj. "The effect of synthesis and post-synthesis modifications on the activity of zeolite beta for cumene synthesis". Master's thesis, University of Cape Town, 1998. http://hdl.handle.net/11427/17951.
Texto completoThe isopropylation of benzene to produce cumene is an important petrochemical process since cumene is used as a chemical intermediate for the production of phenol and acetone. In recent years, the good performance of zeolite Beta for this particular reaction has often been reported in the literature (Reddy et al., 1993, Bellussi et al., 1995 and Perego et al., 1996). It is known, from the numerous studies that have been carried out on other zeolite types, that post synthesis modifications such as dealumination of the zeolite framework tend to enhance the activity of these zeolites for catalytic reactions. Moreover, the effect of synthesis parameters on the catalytic activity of zeolite Beta is an important issue that has not been thoroughly investigated in the literature. In this study, a commercial parent zeolite Beta catalyst (sample A) was modified by post synthesis modifications such as steaming, acid washing or steaming followed by acid washing. A series of zeolite Beta catalysts were also synthesised by different techniques. The samples were characterised with respect to structure, morphology, particle size, number of acid sites, co-ordination state of aluminium and the environment of silicon atoms. The isopropylation of benzene to cumene was used as a test reaction to evaluate the effect of post-synthesis modifications and synthesis procedure on the catalytic activity of the zeolite Beta catalysts.
Crites, Charles-Oneil. "Investigating the Interactions between Free Radicals and Supported Noble Metal Nanoparticles in Oxidation Reactions". Thesis, Université d'Ottawa / University of Ottawa, 2015. http://hdl.handle.net/10393/33404.
Texto completoCABRAL, Rucilana Patrícia Bezerra. "Síntese e avaliação de NiMo/Beta e NiMo/SAPO-5 no hidrocraqueamento do cumeno com piridina". Universidade Federal de Campina Grande, 2008. http://dspace.sti.ufcg.edu.br:8080/jspui/handle/riufcg/1695.
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Devido ao aumento na produção de óleo pesado, a indústria do refino voltou-se para os processos de hidrocraqueamento (HCC) que fornecem combustíveis básicos e leves atendendo as exigências da sociedade moderna. O processo HCC é realizado, geralmente, sob temperaturas e pressões elevadas na presença do hidrogênio e de um catalisador de hidrocraqueamento. As cargas de petróleo brasileiras inevitavelmente contêm muitas impurezas, como os compostos orgânicos nitrogenados. Estes compostos de nitrogênio presentes nas cargas de hidrocraqueamento atuam como venenos temporários dos catalisadores, resultando numa diminuição de atividade destes catalisadores. Normalmente, os catalisadores de HCC compreendem de um suporte ácido mais um componente hidrogenante selecionado do Grupo VIB e do grupo VIII da Tabela periódica dos Elementos, na forma de óxido ou sulfeto. Zeólita Beta e SAPO-5 foram propostos para serem usados como suportes ácidos. A respeito do componente hidrogenante, a combinação de metais usados, expressada como óxidos, foi NiO-MoO3. Uma série de catalisadores NiMo suportados em Zeólita Beta e SAPO-5, de diferentes composições, foram preparados por impregnação seqüencial úmida dos materiais utilizando soluções aquosas precursoras de Ni(NO3)2.6H2O e (NH4)6 Mo7O24. 4H2O. Os suportes e catalisadores foram analisados pelas técnicas: Difração de raios-X (DRX), Espectrometria de Emissão Atômica de Plasma Acoplado Induzido (ICPAES), Adsorção Física de N2 pelo método BET, Redução com Temperatura Programada (RTP), Microscopia Eletrônica de Transmissão (MET), Espectroscopia no Infravermelho de piridina adsorvida (IV), Espectroscopia de Refletância Difusa (DRS) e Espectroscopia de Ressonância Magnética Nuclear (RMN). Os catalisadores NiMo sulfetados foram avaliados usando um reator tubular de fluxo contínuo, no hidrocraqueamento do cumeno na presença e ausência de piridina. Foi verificado que os catalisadores suportados em zeólita Beta promoveram maiores conversões que os suportados em SAPO-5, principalmente o que usou zeólita Beta (Si/Al=8,2) com 4%NiO e 15%MoO3. A presença da piridina foi prejudicial à performance de todos os catalisadores, inclusive para os padrões cedidos pelo CENPES.
Due to the increasing of the heavier crude oil feedstocks production, the oil refining industry has turned to hydrocracking (HCK) processes to provide the lighter basic fuels which modern society demands. The HCK process is generally carried out under high temperatures and pressures in the presence of the hydrogen and a HCK catalyst. The feedstocks of the Brazilian crudes inevitably contain many impurities, such as organic nitrogen compounds. These nitrogen compounds present in the feeds of hydrocracking process act as, temporary poisons to the catalysts, thereby decreasing the catalyst activity. Usually, hydrocracking catalysts comprise of an acidic support plus a hydrogenating component selected from the Group VIB metals and Group VIII metals of the Periodic Table of the Elements, in their oxide or sulfide form. Beta zeolite and SAPO-5 are proposed as acidic support materials for hydrocracking. Regarding the hydrogenation component the combination of the metals used in the form of oxides, was NiO-MoO3. A series of NiMo catalysts supported on Beta zeolite and SAPO-5, of different compositions, were prepared by sequential incipient wetness impregnation of the materials with aqueous solutions of Ni(NO3)2 . 6H2O and (NH4)6 Mo7O24.4H2O. The supports and catalysts were analyzed by several techniques such as: X-ray diffraction (XRD), plasma-emission spectrometry (ICP-AES), N2 physical adsorption by BET method, temperature programmed reduction (TPR), transmission electronic microscopy (TEM), infrared spectroscopy of adsorbed pyridine (IR), diffuse reflectance spectroscopy (DRS) and nuclear magnetic resonance (NMR) spectroscopy. The sulfide NiMo catalysts were evaluated using a continuous-flow tubular reactor by the cumene hydrocracking in the presence and absence of pyridine. It was verified that the NiMo catalysts based on Beta zeolite produced the highest cumene conversion than those based on SAPO-5, particularly the one with Beta zeolite (Si/Al=8,2) containing 4%NiO and 15%MoO3. The presence of nitrogen as pyridine was detrimental for the performance of all catalysts, including the standards one, supplied for the CENPES.
VIMARD, FLORENCE. "Mecanismes d'action cytotoxique de l'hydroperoxyde de cumene sur la lignee pc12. Action protectrice du bfgf et des agents reducteurs des thiols". Caen, 1996. http://www.theses.fr/1996CAEN2051.
Texto completoBayle, Jérôme. "Etude du contact gaz-solide dans un reacteur a co-courant descendant par la mise en oeuvre du craquage catalytique du cumene". Paris 6, 1996. http://www.theses.fr/1996PA066815.
Texto completoSilva, Luciana Yumi Akisawa. "Determinação experimental e modelagem termodinamica de dados de equilíbrio de fases de misturas binarias e ternaria contendo acetona, agua e cumeno". [s.n.], 2007. http://repositorio.unicamp.br/jspui/handle/REPOSIP/266953.
Texto completoDissertação (mestrado) - Universidade Estadual de Campinas, Faculdade de Engenharia Quimica
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Resumo: No projeto de processos de separação é essencial o conhecimento do comportamento das fases que estão em equilíbrio. O presente trabalho consistiu no estudo do equilíbrio de fases de misturas contendo acetona, água e cumeno. Estes componentes são de grande importância para a indústria do fenol. Os componentes água e cumeno são parcialmente miscíveis e na destilação da mistura de acetona, água e cumeno ocorre a formação de três fases (líquido-líquido-vapor), por isso é muito importante a determinação de um único conjunto de parâmetros dos modelos de GE que possa representar adequadamente o equilíbrio líquido-líquido simultaneamente. Determinou-se dados de equilíbrio líquido-vapor dos sistemas acetona + água,acetona + cumeno e acetona + água+ cumeno e dados de equilíbrio líquido-líquido do sistema água + cumeno a 760 mmHg. O Princípio da Máxima Verossimilhança foi utilizado no ajuste dos parâmetros de interação binária dos modelos NRTL e UNIQUAC.Os parâmetros obtidos neste trabalho foram comparados em trabalho anterior,Mafra (2005,) no qual se procedeu ao ajuste de dados ternários de equilíbrio líquido-líquido a 50 °C, e buscou-se o conjunto de parâmetros que melhor representa o equilíbrio líquido-vapor e líquido-líquido simultaneamente. Os resultados obtidos revelaram que o modelo NRTL com parâmetros determinados a partir de dados binários representa satisfatoriamente os equilíbrios líquido-vapor e líquido-líquido de sistemas binários e ternário envolvendo acetona, água e cumeno
Abstract: On projecting separation processes it is essential the knowledge of the behavior of the phases in equilibrium. The present work involved the study of the phase equilibrium of mixtures containing acetone, water and cumene, which are very important in the phenol industry. The components water and cumene are partially miscible, and in the distillation of the mixture of acetone, water and cumene occurs the simultaneous formation of three phases, two liquids and one vapor. In such a way this it is important the determination of only one set of parameters for GE models that can represent appropriately the vapor-liquid and liquid-liquid equilibrium. It has been determined vapor-liquid equilibrium data of acetone + water, acetone + cumene and acetone + water -"o cumene systems and liquid-liquid equilibrium data of water + cumene system at 760 mmHg. The Maximum Likelihood Principle was used for the estimation of the interaction parameters for the NRTL and UNIQUAC models. The parameters obtained in this work were compared with the parameters found by Mafra (2005). who realized the reduction of ternary liquid-liquid equilibrium data at 50°C. and it has been analyzed which set of parameters gives the best representation of the vapor-liquid and the liquid-liquid equilibrium simultaneously. The results have shown that the NRTL model with parameters determined by binary data represents properly the vapor-liquid and liquid-liquid equilibrium of binary and ternary systems containing acetone, water and cumene
Mestrado
Desenvolvimento de Processos Químicos
Mestre em Engenharia Química
Camarasa, Eric. "Étude hydrodynamique et modélisation des réacteurs à gazosiphon d'oxydation du cumène". Vandoeuvre-les-Nancy, INPL, 2000. http://www.theses.fr/2000INPLA001.
Texto completoA complete model for prediction of cumene oxidation air-Iift reactors has been developed. The model includes reaction kinetics, mass transfer and hydrodynamics. The film model has been chosen to account for an eventual enhancement of the oxygen absorption rate. The flow configuration has been taken into account and the cell model approach is used to describe the liquid and gas phase mixing behavior. Hydrodynamic parameters as the gas hold-up and the liquid circulation velocity, are calculated with an adequate model based on momentum balance equations and adjusted to the industrial system with experimental data. Experimental work involving numerous measuring techniques has been conducted in several reactors (one simple bubble column and three air-lift reactors) equipped with different gas distributors and using water, water-alcohol solutions and the industrial organic mixture as the liquid phase. A better understanding of the influence of liquid properties (particularly the coalescing behavior) and of the gas distribution on bubble and hydrodynamic characteristics has been obtained. Flow regimes and regime transitions have also been examined using different techniques of signal analysis applied to pressure fluctuations. Finally, the complete model predicts the variations of concentration and hydrodynamic parameters along the reactor and so is able to provide a good description of the cumene oxidation reactors. By performing parameter sensitivity analysis and by incorporating the model into an optimization procedure, guidelines for design, operation and scale-up of such reactors are proposed
Silva, Marciéli. "Propagação de jamboleiro [Syzygium cumini (L.) Skeels]". Universidade Tecnológica Federal do Paraná, 2017. http://repositorio.utfpr.edu.br/jspui/handle/1/2358.
Texto completoSyzygium cumini (L.) Skeels is an exotic species native to Asia, but its is cultivated a lot of countries, including Brazil. Although there are few commercial plantations of this fruit tree, it has many possibilities of commercialization, market of fresh fruits to processing such as jams, liqueurs, vinegar, jellies, pies and sweets. The objective of the work was to test propagation techniques in order to obtain an appropriate protocol for this species. The experiments were carried out in the Laboratory of Plant Physiology and Unit of Teaching and Research Nursery, at Federal Technological University of Paraná - Câmpus Dois Vizinhos. The storage of S. cumini seeds was during 0, 30, 60, 90, 120, 150, 180, 210, 240, 270, 300, 330, 360 days. The storage followed by hydrocondicionamento in temperature of 25 °C during 0, 12, 24, 36, 48, 60, 72, 84, 96, 108, 120, 132, 144 and 156 hours. The germination percentage, germination speed index and average germination time after 60 days were evaluated, according each time. In the mini-cuttings, indole-butyric acid (IBA) concentrations (0, 2000, 3000, 4000 mg.L-1) and type of cuttings (apical, middle and basal) were tested. In the cutting experiment, IBA concentrations (0, 5000, 10000 mg.L-1) and Benzylaminopurine (BAP) concentrations (0, 250 and 500 mgL-1) were evaluated. In the second cutting experiment, conditioning techniques (control, ringing and etiolation), conditioning time (40, 60, 80 and 100 days) and IBA concentrations (0, 2000, 4000 mg.L-1) were tested. In the air layering we used types of coating (withoutcolor plastic, aluminum paper and black plastic), IBA concentrations (0, 2000 and 4000 mg.L-1), presence or not of cotton and seasons of the year. In order to evaluate the percentage of rooting, root number, length of the three largest roots, and presence of callus by cuttingFor the S. cumini it was recommended the storage followed by hydrocondicionamento for up to 156 hours, the use of middle and basal minicuttings without the IBA application. The air layering was the technique propagation that it was possible higher rooting values.
Libros sobre el tema "Cumene"
Gardner, R. Cumene: Criteria document for an occupational exposure limit. London: HSE Books, 1994.
Buscar texto completoLi, Kong. Deactivation of silica-alumina catalyst during the cumene cracking reaction. Salford: University of Salford, 1988.
Buscar texto completoTopp, LaRayne Meyer. Cuming County. Charleston, South Carolina: Arcadia Publishing, 2012.
Buscar texto completoMonzonis-Vilallonga, Jorge Fuentes. La cumbre. Burgos: Editorial Dossoles, 2006.
Buscar texto completoCapítulos de libros sobre el tema "Cumene"
Gooch, Jan W. "Cumene". En Encyclopedic Dictionary of Polymers, 186. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_3175.
Texto completoPatnaik, Pradyot. "Cumene". En Handbook of Environmental Analysis, 415–16. Third edition. | Boca Raton : Taylor & Francis, CRC Press, 2017.: CRC Press, 2017. http://dx.doi.org/10.1201/9781315151946-84.
Texto completoGooch, Jan W. "Cumene Hydroperoxide". En Encyclopedic Dictionary of Polymers, 186. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_3176.
Texto completoWeber, Manfred, Jan-Bernd Grosse Daldrup y Markus Weber. "Noncatalyzed Radical Chain Oxidation: Cumene Hydroperoxide". En Liquid Phase Aerobic Oxidation Catalysis: Industrial Applications and Academic Perspectives, 15–31. Weinheim, Germany: Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527690121.ch2.
Texto completoFedorov, A. Yu, E. V. Volchenko, T. A. Romanova, I. N. Singirtsev y A. P. Gumenyuk. "The treatment of cumene hydroperoxide containing wastewaters". En Global Environmental Biotechnology, 311–17. Dordrecht: Springer Netherlands, 1997. http://dx.doi.org/10.1007/978-94-017-1711-3_27.
Texto completoSharma, Shivom, Zi Chao Lim y Gade Pandu Rangaiah. "Process Design for Economic, Environmental and Safety Objectives with an Application to the Cumene Process". En Multi-Objective Optimization in Chemical Engineering, 449–77. Oxford, UK: John Wiley & Sons Ltd, 2013. http://dx.doi.org/10.1002/9781118341704.ch16.
Texto completoVinila, M. L., K. Aparna y S. Sreepriya. "Optimization of Parametric Model of Cumene Reactor Using Loop Shaping Methodology and Dynamic Modeling of Reactor". En Advances in Intelligent Systems and Computing, 201–8. Cham: Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-30465-2_23.
Texto completoRoss, Ivan A. "Syzygium cumini". En Medicinal Plants of the World, 445–54. Totowa, NJ: Humana Press, 2003. http://dx.doi.org/10.1007/978-1-59259-365-1_26.
Texto completoBährle-Rapp, Marina. "Eugenia cumini". En Springer Lexikon Kosmetik und Körperpflege, 195. Berlin, Heidelberg: Springer Berlin Heidelberg, 2007. http://dx.doi.org/10.1007/978-3-540-71095-0_3807.
Texto completoLim, T. K. "Syzygium cumini". En Edible Medicinal And Non Medicinal Plants, 745–59. Dordrecht: Springer Netherlands, 2011. http://dx.doi.org/10.1007/978-94-007-2534-8_100.
Texto completoActas de conferencias sobre el tema "Cumene"
Naegeli, David W. "The Role of Sulfur in the Thermal Stability of Jet Fuel". En ASME 1999 International Gas Turbine and Aeroengine Congress and Exhibition. American Society of Mechanical Engineers, 1999. http://dx.doi.org/10.1115/99-gt-298.
Texto completo"Supported transition metals oxides and N-hydroxyphthalimide in catalysis of the liquid-phase oxidation of cumene". En Chemical technology and engineering. Lviv Polytechnic National University, 2021. http://dx.doi.org/10.23939/cte2021.01.106.
Texto completoAyres, J. R. "Cument Status and Trends in Active Matrix LCD's". En Proceedings of European Meeting on Lasers and Electro-Optics. IEEE, 1996. http://dx.doi.org/10.1109/cleoe.1996.562423.
Texto completoCONSUL KASSARDJIAN, DANIEL, Flávio L. Schmidt y Bianca Souza da Costa. "Caracterização física e físico-química de Jambolão (Syzygium cumini)". En XXIV Congresso de Iniciação Científica da UNICAMP - 2016. Campinas - SP, Brazil: Galoa, 2016. http://dx.doi.org/10.19146/pibic-2016-51920.
Texto completoTretiakova, Svitlana. "RESISTANCE OF SUNFLOWER LINES AND HYBRIDS TO OROBANCHE CUMANA WALLR". En Relevant Issues of the Development of Science in Central and Eastern European Countries. Publishing House “Baltija Publishing”, 2019. http://dx.doi.org/10.30525/978-9934-588-11-2_8.
Texto completoNerys, Leylianne de Cássia Rodrigues, Maria Cristina Ribeiro da Silva, Marilia Grasielly de Farias Silva, Edson Renan Barros de Santana, Brunna Fernanda Lira Patriota, Ricardo Yara y Cláudia Sampaio de Andrade Lima. "AVALIAÇÃO DA ATIVIDADE ANTIOXIDADE DE Syzigium malaccense E Syzigium cumini". En Encontro Anual da Biofísica 2017. São Paulo: Editora Blucher, 2017. http://dx.doi.org/10.5151/biofisica2017-030.
Texto completoCORREIA, J. L. A., R. C. LEÃO, E. R. FLORENTINO, K. M. A. dos SANTOS, V. C. F. PIRES, O. M. MARQUES y I. M. FLORÊNCIO. "APROVEITAMENTO DO FRUTO JAMBOLÃO (SYZYGIUM CUMINI) PARA ELABORAÇÃO DE VINHO." En XX Congresso Brasileiro de Engenharia Química. São Paulo: Editora Edgard Blücher, 2015. http://dx.doi.org/10.5151/chemeng-cobeq2014-0100-27044-148163.
Texto completoBabkin, Alexander, Elena Neskoromnaya, Irina Burakova, Ananstasia Kucherova, Alexander Burakov y Elina Mkrtchyan. "Kinetic characteristics of Cu (II) adsorption on nano(poly)-cumulene". En PROSPECTS OF FUNDAMENTAL SCIENCES DEVELOPMENT (PFSD-2017): Proceedings of the XIV International Conference of Students and Young Scientists. Author(s), 2017. http://dx.doi.org/10.1063/1.5009827.
Texto completoAnton, Florin Gabriel y Luxiţa Rîşnoveanu. "Sunflower genotypes with resistance / tolerance at parasite Orobanche cumana Wallr". En XIth International Congress of Geneticists and Breeders from the Republic of Moldova. Scientific Association of Geneticists and Breeders of the Republic of Moldova, Institute of Genetics, Physiology and Plant Protection, Moldova State University, 2021. http://dx.doi.org/10.53040/cga11.2021.048.
Texto completo"Application of cumin in nutrition science and medicine". En International Conference on Medicine, Public Health and Biological Sciences. CASRP Publishing Company, Ltd. Uk, 2016. http://dx.doi.org/10.18869/mphbs.2016.107.
Texto completoInformes sobre el tema "Cumene"
JAREK, RUSSELL L., STEVEN M. THORNBERG, STACIA BARROW, DANIEL E. TRUDELL y TINA M. NENOFF. Energy Efficient Catalytic Reaction and Production of Cumene. Office of Scientific and Technical Information (OSTI), diciembre de 2001. http://dx.doi.org/10.2172/791886.
Texto completoMartínez del Pozo, Álvaro. La Biologia Molecular cumple 50 años. Sociedad Española de Bioquímica y Biología Molecular (SEBBM), enero de 2010. http://dx.doi.org/10.18567/sebbmdiv_rpc.2010.01.1.
Texto completoLanier, Nicholas Edward. La Cumbre Update: Motivation, Objectives, and Progress. Office of Scientific and Technical Information (OSTI), agosto de 2017. http://dx.doi.org/10.2172/1378914.
Texto completoHsu, Donald P., William M. Davis y Stephen L. Buchwald. Synthesis and Structure of a Seven Membered Cyclic Cumulene. Fort Belvoir, VA: Defense Technical Information Center, mayo de 1993. http://dx.doi.org/10.21236/ada265289.
Texto completoReporte de Estabilidad Financiera - I semestre 2021. Banco de la República, mayo de 2021. http://dx.doi.org/10.32468/rept-estab-fin.sem1-2021.
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