Academic literature on the topic 'Dehydrogenation'

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Journal articles on the topic "Dehydrogenation"

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Maji, Biplab, and Milan Barman. "Recent Developments of Manganese Complexes for Catalytic Hydrogenation and Dehydrogenation Reactions." Synthesis 49, no. 15 (July 13, 2017): 3377–93. http://dx.doi.org/10.1055/s-0036-1590818.

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Being the third most abundant transition metal in the Earth’s crust (after iron and titanium) and less toxic, reactions catalyzed by manganese are becoming very important. A large number of manganese complexes have been synthesized using bidentate and tridentate ligands. Such manganese complexes display excellent catalytic activities for various important organic transformations, such as hydrogenation, dehydrogenation, dehydrogenative coupling, transfer hydrogenation reactions, etc. In this short review, recent developments of such manganese-catalyzed reactions are presented.1 Introduction2 Well-Defined Manganese-Complex-Catalyzed Hydrogenation Reactions2.1 Hydrogenation of Nitriles2.2 Hydrogenation of Aldehydes and Ketones2.3 Hydrogenation of Esters2.4 Hydrogenation of Amides2.5 Hydrogenation of Carbon Dioxide3 Manganese-Catalyzed Dehydrogenation Reactions3.1 Selective Dehydrogenation of Methanol3.2 Dehydrogenative N-Formylation of Amines by Methanol3.3 Dehydrogenative Coupling Reactions of Alcohols3.4 Imine Synthesis via Dehydrogenative Coupling of Alcohols and Amines3.5 Synthesis of N-Heterocycles via Dehydrogenative Coupling4 Manganese-Catalyzed Dehydrogenation–Hydrogenation Cascades4.1 N-Alkylation of Amines with Primary Alcohols4.2 α-Alkylation of Ketones with Primary Alcohols4.3 Transfer Hydrogenation of Ketones5 Conclusion
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Luo, Zheng, Huayou Hu, Chao Wang, Zhen Yang, and Yefei Wang. "A domino reaction for the synthesis of pyrrolo[2,1-a]isoquinolines from 2-aryl-pyrrolidines and alkynes promoted by a four-component catalytic system under aerobic conditions." RSC Advances 13, no. 50 (2023): 35617–20. http://dx.doi.org/10.1039/d3ra07653a.

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Bossola, Filippo, and Nicola Scotti. "Editorial: Special Issue on “Advances on Catalysts Based on Copper”." Catalysts 13, no. 4 (April 4, 2023): 700. http://dx.doi.org/10.3390/catal13040700.

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Copper-based catalysts are very active in a wide range of different reactions, such as methanol synthesis, steam reforming/WGS, hydrogenation/dehydrogenation/transfer hydrogenation, oxidation, dehydrogenative coupling, acid-base reactions, etc [...]
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Zhang, Chang-Wu, Jing Wen, Lei Wang, Xin-Ge Wang, and Lei Shi. "Iron doping boosts the reactivity and stability of the γ-Al2O3 nanosheet supported cobalt catalyst for propane dehydrogenation." New Journal of Chemistry 44, no. 18 (2020): 7450–59. http://dx.doi.org/10.1039/d0nj00381f.

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This study describes a new iron-doping strategy to improve both the reactivity and stability of a cobalt catalyst in propane dehydrogenation, meanwhile, the defective γ-Al2O3 nanosheet synergistically boosted the dehydrogenating activity of that.
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Teng, Qing-Hu, Yan-Yan Chen, Yan Yao, and Xiu-Jin Meng. "Electrochemical Synthesis of Quinazolinones by the Metal-Free and Acceptor-Free Dehydrogenation of 2-Aminobenzamides." Synlett 31, no. 18 (August 19, 2020): 1795–99. http://dx.doi.org/10.1055/s-0040-1707248.

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An efficient approach has been developed for the construction of quinazolin-4(3H)-ones by the selective anodic dehydrogenative oxidation/cyclization of benzylic chlorides and 2-aminobenzamides. The method features acceptor-free and metal-free dehydrogenation of amines to imines; a subsequent intermolecular addition provides the products in moderate to good yields.
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Wang, Wan-Qiang, Hua Cheng, Ye Yuan, Yu-Qing He, Hua-Jing Wang, Zhi-Qin Wang, Wei Sang, Cheng Chen, and Francis Verpoort. "Highly Efficient N-Heterocyclic Carbene/Ruthenium Catalytic Systems for the Acceptorless Dehydrogenation of Alcohols to Carboxylic Acids: Effects of Ancillary and Additional Ligands." Catalysts 10, no. 1 (December 19, 2019): 10. http://dx.doi.org/10.3390/catal10010010.

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The transition-metal-catalyzed alcohol dehydrogenation to carboxylic acids has been identified as an atom-economical and attractive process. Among various catalytic systems, Ru-based systems have been the most accessed and investigated ones. With our growing interest in the discovery of new Ru catalysts comprising N-heterocyclic carbene (NHC) ligands for the dehydrogenative reactions of alcohols, we designed and prepared five NHC/Ru complexes ([Ru]-1–[Ru]-5) bearing different ancillary NHC ligands. Moreover, the effects of ancillary and additional ligands on the alcohol dehydrogenation with KOH were thoroughly explored, followed by the screening of other parameters. Accordingly, a highly active catalytic system, which is composed of [Ru]-5 combined with an additional NHC precursor L5, was discovered, affording a variety of acid products in a highly efficient manner. Gratifyingly, an extremely low Ru loading (125 ppm) and the maximum TOF value until now (4800) were obtained.
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Guo, Jia Neng, Jin Zhi Lin, Xin Liu, Qi Wei Wang, Ge Gao, Xiang Zhang, Xin Ge Shi, Bei Yang, and Hai Bo Jin. "The Progress of Catalyst for Cyclohexane Dehydrogenation Processes." Advanced Materials Research 953-954 (June 2014): 1261–68. http://dx.doi.org/10.4028/www.scientific.net/amr.953-954.1261.

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Cyclohexane dehydrogenation is an important process in the petrochemical industry, chemical raw material such as cyclohexanol, cyclohexanone,benzene and cyclohexene can be produced from which.Divided cyclohexane dehydrogenation into catalytic dehydrogenation or oxidative dehydrogenation, homogeneous or heterogeneous reaction. Summarized vary catalysts, active constituent and process conditions in dehydrogenation process.
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Möhrle, H., and M. Jeandrée. "1,3-Dioxolane von N-substituierten 4-Piperidonen als Dehydrierungssubstrat / 1,3-Dioxolanes of N-Substituted 4-Piperidones as Substrates for Dehydrogenations." Zeitschrift für Naturforschung B 52, no. 1 (January 1, 1997): 72–78. http://dx.doi.org/10.1515/znb-1997-0115.

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The applicability of ketals was examined for masking the carbonyl group in N-tertiary 4-piperidones during the dehydrogenation using mercury-edta. Various 1,3-dioxolanes showed a different behaviour in dependence on the N-substituent. With simple aliphatic moieties mainly dehydrogenated but hydrolyzed products were received. These enaminones were also available from the dehydrogenations of the corresponding 4-piperidones. Similar applied to para-acyl-aromatic substituted derivatives but with less yields. Aromatic substituents bearing a neighbour group on ortho-position with participation gave rise to different oxidation products partially with preservation of the ketal structure
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Zhang, Yanghuan, Meng Ji, Zeming Yuan, Wengang Bu, Yan Qi, and Shihai Guo. "Catalytic effect of MoS2 on hydrogen storage thermodynamics and kinetics of an as-milled YMg11Ni alloy." RSC Advances 7, no. 60 (2017): 37689–98. http://dx.doi.org/10.1039/c7ra05965e.

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Yuan, Zeming, Wei Zhang, Peilong Zhang, Yanghuan Zhang, Wengang Bu, Shihai Guo, and Dongliang Zhao. "Improvement in the hydrogen storage performance of the as-milled Sm–Mg alloys using MoS2 nano-particle catalysts." RSC Advances 7, no. 89 (2017): 56365–74. http://dx.doi.org/10.1039/c7ra10160k.

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Dissertations / Theses on the topic "Dehydrogenation"

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Herauville, Virginie Marie Therese. "Catalytic Dehydrogenation of Propane : Oxidative and Non-Oxidative Dehydrogenation of Propane." Thesis, Norges Teknisk-Naturvitenskaplige Universitet, 2012. http://urn.kb.se/resolve?urn=urn:nbn:no:ntnu:diva-21096.

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The dehydrogenation of propane has a great interest, due to a global growing demand in propene. This reaction needs a catalyst, high temperature and low propane partial pressure. During this work, platinum hydrotalcite-supported was used as catalyst. First, three different kinds of support were tested: the hydrotalcite 30 (30% MgO, 70% Al2O3), the hydrotalcite 63 and the hydrotalcite 70. The catalysts were prepared with 1 or 2 % mass platinum, by a kind of colloid method. They were characterized by BET, XRD, and chemisorption, and activity tests were performed. The catalytic tests were performed in a fix bed reactor in a temperature range from 350 °C to 650 °C. The propane conversion and selectivity were not really different between the three supports. For example, the selectivity to propene reached a maximum between 50 % and of 55 % at 550 °C for all the catalysts. Then, the catalyst HT 63 with 1 % Pt was selected for further experiments. The feed gas composition was varied, to see the influence of the ratio Propane/Oxygen/Hydrogen. Some experiments involved oxidative dehydrogenation of propane, whereas some others were non-oxidative dehydrogenation of propane. The propane conversion was better when the reaction took place simultaneous with oxidative reactions. The system is complex, but some feed gas compositions favor the conversion of propane and the selectivity of propane to propylene. The influence of pressure on the reaction was also investigated. Oxidative dehydrogenation of propane was studied at low (1.1 bar) and high pressure (above 3 bar). When the pressure in the reactor during the experiment was above 2 bar, the propane conversion, the propane selectivity to propene and the propene yield are improved.
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Jibril, Baba El-Yakubu. "Catalytic oxidative dehydrogenation of propane." Thesis, University of Salford, 2002. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.248905.

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Mandani, Faisal Mohammad. "Kinetic and deactivation studies during catalytic dehydrogenation." Thesis, University of Salford, 1991. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.305913.

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Mpuhlu, Batsho. "Vapour phase dehydrogenation of cyclohexane on microstructured reactors." Thesis, Nelson Mandela Metropolitan University, 2012. http://hdl.handle.net/10948/8661.

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The work that is described in this thesis forms part of the research and development projects at InnoVenton: NMMU Institute of Chemical Technology in collaboration with Sasol Technologies. The broader view of the project was testing on the so-called “Small Production Platforms” (SPP’s). In particular the main aim of this study was to investigate the effect of micro-structuring on the heterogeneous catalysed, vapour-phase oxidative dehydrogenation of cyclohexane in the presence of air. Ground work studies were done to provide a proper comparison of the micro-structured reactor with a traditional fixed-bed reactor. These included evaluation of a proper vanadium pyrophosphate catalyst for the reaction, testing of reaction parameters for the oxidative dehydrogenation reaction on a fixed-bed reactor and lastly comparing the performance of the micro-structured reactor to that of the fixed-bed reactor Various vanadium pyrophosphate catalysts that were tested for activity included: bulk (VO)2P2O7, bulk (VO)2P2O7 promoted with Fe, (VO)2P2O7 supported on -Al2O3 and Fe promoted (VO)2P2O7 supported on -Al2O3. These catalysts showed significant differences in TOF, however it was not conclusive from the results whether these differences may be traced to increased activity for dehydrogenation for different catalysts since all reactions were run under conditions of oxygen deficiency. It is, however, clear that Fe promotion significantly increase activity, irrespective of the relative degrees of oxidative dehydrogenation and normal dehydrogenation. The Fe promoted catalyst was further tested for long term stability in-view of using it as the catalyst in the micro-structured reactor. These studies showed the catalyst to have a high degree of stability with minimal structural changes under the reaction conditions used. Various response surface models describing the variation in each of the cyclohexane conversion, cyclohexene selectivity, and benzene selectivity, respectively when changing reaction condition, were derived by means of multiple regression. To obtain some idea of the degree and nature of the normal dehydrogenation reaction, the amount of deficit oxygen was estimated from the measured results for cyclohexane conversion and cyclohexene and benzene selectivities. These estimated values were also modelled as described above. The regression models were used to interpret specific trends in the responses for the oxidative dehydrogenation of cyclohexane and account for the oxygen deficit in the system. The performance of a fixed bed tubular reactor (FBR) and micro-structured sandwich reactor (MSSR) were compared over an Fe promoted vanadium pyrophosphate. Reactor performance was evaluated by varying specific reaction conditions (temperature and space velocity). Subsequently the turn-over frequencies, conversion and selectivities from the two reactors were compared. The conversion achieved in the micro-structured reactor was observed to be significantly higher than that achieved in the fixed-bed reactor at all reaction parameters. This is despite the fact that the total amount of catalyst in the micro-structured reactor is approximately 5 times less than that used in the fixed bed reactor. In addition, the contact time (1/MHSV) in the micro-structured reactor is also significantly shorter than in the fixed-bed reactor.
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Hiltzik, Laurence Howard. "Characterization of a catalyst regeneration process for metals fouled CoMo/Al[subscript]2O[subscript]3 catalysts." Diss., Georgia Institute of Technology, 1987. http://hdl.handle.net/1853/10974.

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Ismail, Manal. "Dehydrogenation of isobutane using a structured adsorptive reactor." Thesis, Imperial College London, 2006. http://hdl.handle.net/10044/1/8223.

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Levin, Doron P. "Novel transition metal molybdates for catalytic oxidative dehydrogenation." Thesis, Massachusetts Institute of Technology, 1997. http://hdl.handle.net/1721.1/37037.

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Talwar, Dinesh. "Hydrogenation and dehydrogenation with cyclometalated iridium (III) complexes." Thesis, University of Liverpool, 2014. http://livrepository.liverpool.ac.uk/2003856/.

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The selective hydrogenation and dehydrogenation of organic molecules is a fundamentally challenging and an attractive transformation for both, industry and academia. However, catalysts capable of undergoing both transformations under environmentally benign conditions are rare. In this thesis, our contribution to the development of a “universal” catalyst capable of achieving both hydrogenation and dehydrogenation of a wide range of organic compounds under mild conditions is presented. A general introduction covering the recent developments in the area of transfer hydrogenation of C=X (X = O, N) bonds, relevant applications of cyclometalated half-sandwich complexes and previous work in the area developed within our group is described in Chapter 1. In Chapter 2, Cyclometalated iridium complexes are shown to be highly efficient and chemoselective catalysts for the transfer hydrogenation of a wide range of carbonyl groups with formic acid in water. Examples include α-substituted ketones (α-ether, α-halo, α-hydroxy, α-amino, α-nitrile, α-ester), α-keto esters, β-keto esters, and α,β-unsaturated aldehydes. The reduction was carried out at substrate/catalyst ratios of up to 50000 at pH 4.5, requiring no organic solvent. The protocol provides a practical, easy and efficient way for the synthesis of β-functionalised secondary alcohols, such as β-hydroxyethers, β-hydroxyamines and β-hydroxyhalo compounds, which are valuable intermediates in pharmaceutical, fine chemical, perfume and agrochemical synthesis. In Chapter 3, the cyclometalated iridium complexes are shown to catalyse the transfer hydrogenation of various nitrogen heterocycles, including but not limited to quinolines, isoquinolines, indoles and pyridiniums, in aqueous solution under mild conditions. The catalyst shows excellent functional group compatibility and high turnover number (up to 7500), with loading as low as 0.01% being feasible. In Chapter 4, cyclometalated iridium complexes are found to be versatile catalysts for the direct reductive amination of carbonyls to give primary amines under transfer hydrogenation conditions with ammonium formate as both the nitrogen and hydrogen source. The activity and chemoselectivity of the catalyst towards primary amines is excellent, with a substrate to catalyst ratio of 1000 being feasible. Both aromatic and aliphatic primary amines were obtained in high yields. Moreover, a first example of a homogeneously catalysed transfer hydrogenative direct reductive amination (DRA) has been achieved for -keto ethers, leading to the corresponding -amino ethers. In addition, non-natural -amino acids could also be obtained in excellent yields with this method. Following the success of hydrogenation, cyclometalated iridium complexes were also found to be versatile catalysts for the oxidant-free, acceptorless dehydrogenation of various N-heterocycles, including tetrahydroquinolines, tetrahydroisoquinolines, tetrahydroquinoxalines and indolines. This protocol was also successfully applied to the total synthesis of alkaloids as presented in Chapter 5. Chapter 6 describes the development of a new strategy for the oxidant- and base-free dehydrogenative coupling of N-heterocycles at mild conditions. Under the action of an iridium cyclometalated catalyst, N-heterocycles undergo multiple sp3 C-H activation, generating a nucleophilic enamine that reacts in situ with various electrophiles to give highly functionalised products. The dehydrogenative coupling can be cascaded with Friedel-Crafts addition, resulting in double functionalisation of the N-heterocycles. The dehydrogenation products could also be saturated under either hydrogenation or transfer hydrogenation conditions, giving rise to structurally diverse products. Final conclusion and perspectives of the research covered in this PhD thesis are presented in Chapter 7.
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V, Ashok Kumar. "Oxidative dehydrogenation of hydrocarbons over mixed metal oxides." Thesis(Ph.D.), CSIR-National Chemical Laboratory, Pune, 2017. http://dspace.ncl.res.in:8080/xmlui/handle/20.500.12252/5889.

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Wang, Bo. "Applications of hydrogenation and dehydrogenation on noble metal catalysts." [College Station, Tex. : Texas A&M University, 2007. http://hdl.handle.net/1969.1/ETD-TAMU-1446.

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Books on the topic "Dehydrogenation"

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Sundararaju, Basker, ed. Dehydrogenation Reactions with 3d Metals. Cham: Springer Nature Switzerland, 2024. http://dx.doi.org/10.1007/978-3-031-48952-5.

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Mandani, Faisal Mohammad. Kinetic and deactivation studies during catalytic dehydrogenation. Salford: University of Salford, 1991.

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Shahabuddin, Syed, Rama Gaur, and Nandini Mukherjee. Chemistry of Dehydrogenation Reactions and Its Applications. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003321934.

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Ogonowski, Jan. Studium nad utleniającym odwodornieniem niektórych wybranych węglowodorów alifatycznych i alkiloaromatycznych. Kraków: Politechnika Krakowska, 1990.

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Risk Reduction Engineering Laboratory (U.S.), ed. Supercritical water oxidation. Cincinnati, OH: U.S. Environmental Protection Agency, Risk Reduction Engineering Laboratory, Office of Research and Development, 1992.

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Boiarsky, Alexandre. New high-temperature dehydrogenation processes using equilibrium shifting with CO2. Manchester: UMIST, 1994.

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Neary, Michelle Catherine. Molybdenum, Tungsten and Nickel Compounds as Catalysts for the Dehydrogenation of Formic Acid. [New York, N.Y.?]: [publisher not identified], 2016.

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Abdalla, Babiker K. Heterogeneous modelling of fixed bed and fluidized bed reactors without and with selective mambranes for the catalytic dehydrogenation of ethylbenzene to styrene. Salford: University of Salford, 1993.

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Srivastava, Ananya, and Chandan K. Jana, eds. Heterocycles via Cross Dehydrogenative Coupling. Singapore: Springer Singapore, 2019. http://dx.doi.org/10.1007/978-981-13-9144-6.

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Dehydrogenation Reactions with 3d Metals. Springer, 2024.

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Book chapters on the topic "Dehydrogenation"

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Gooch, Jan W. "Dehydrogenation." In Encyclopedic Dictionary of Polymers, 200. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_3394.

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Findlater, Michael, Jongwook Choi, Alan S. Goldman, and Maurice Brookhart. "Alkane Dehydrogenation." In Catalysis by Metal Complexes, 113–41. Dordrecht: Springer Netherlands, 2012. http://dx.doi.org/10.1007/978-90-481-3698-8_4.

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Caro, Juergen. "Dehydrogenation Reactions." In Encyclopedia of Membranes, 525–27. Berlin, Heidelberg: Springer Berlin Heidelberg, 2016. http://dx.doi.org/10.1007/978-3-662-44324-8_166.

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Sheintuch, Moshe, and David S. A. Simakov. "Alkanes Dehydrogenation." In Membrane Reactors for Hydrogen Production Processes, 183–200. London: Springer London, 2011. http://dx.doi.org/10.1007/978-0-85729-151-6_9.

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Gooch, Jan W. "Oxidative Dehydrogenation." In Encyclopedic Dictionary of Polymers, 511. New York, NY: Springer New York, 2011. http://dx.doi.org/10.1007/978-1-4419-6247-8_8318.

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Caro, Juergen. "Dehydrogenation Reactions." In Encyclopedia of Membranes, 1–2. Berlin, Heidelberg: Springer Berlin Heidelberg, 2015. http://dx.doi.org/10.1007/978-3-642-40872-4_166-3.

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Matar, Sami, Manfred J. Mirbach, and Hassan A. Tayim. "Hydrogenation—Dehydrogenation Processes." In Catalysis in Petrochemical Processes, 35–65. Dordrecht: Springer Netherlands, 1989. http://dx.doi.org/10.1007/978-94-009-1177-2_3.

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Li, Jie Jack. "Nicolaou IBX dehydrogenation." In Name Reactions, 438–39. Cham: Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-03979-4_194.

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Saini, Ankita, Monalisa Bourah, and Sunil Kumar Saini. "A Greener Dehydrogenation." In Chemistry of Dehydrogenation Reactions and Its Applications, 217–37. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003321934-15.

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Li, Jie Jack. "Nicolaou IBX dehydrogenation." In Name Reactions, 397–98. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-01053-8_181.

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Conference papers on the topic "Dehydrogenation"

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Irrazábal Moreda, Olvido, Olaf Magnussen, Jakub Drnec, and Andrea Sartori. "Catalytic Dehydrogenation in LOHC Technology." In The Future of Hydrogen: Science, Applications and Energy Transition. València: FUNDACIO DE LA COMUNITAT VALENCIANA SCITO, 2024. http://dx.doi.org/10.29363/nanoge.hfuture.2024.006.

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Liu, Yingze, and Chengxue Wang. "Thermodynamic calculation of isobutane dehydrogenation reaction." In 2014 IEEE Workshop on Advanced Research and Technology in Industry Applications (WARTIA). IEEE, 2014. http://dx.doi.org/10.1109/wartia.2014.6976182.

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Yan, Hao-Bing, Chan Wang, Rui-Xue Yuan, Zhao-Tie Liu, and Zhong-Wen Liu. "Oxidative Dehydrogenation of Ethylbenzene with CO2." In 14th Asia Pacific Confederation of Chemical Engineering Congress. Singapore: Research Publishing Services, 2012. http://dx.doi.org/10.3850/978-981-07-1445-1_146.

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Jamaleddine, Tarek J., and Ramsey M. Bunama. "CFD Modelling of the Dehydrogenation Reaction of Isobutane to Isobutylene in a Fixed Bed Reactor." In ASME 2016 Heat Transfer Summer Conference collocated with the ASME 2016 Fluids Engineering Division Summer Meeting and the ASME 2016 14th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2016. http://dx.doi.org/10.1115/ht2016-1071.

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The catalytic dehydrogenation reaction of isobutane to isobutylene is simulated in a commercial-scale heterogenous fixed bed reactor (FBR). The porous medium method in ANSYS Fluent combined with the reaction model capability was utilized to predict the flow behavior and species transport in a bed of spherical particles. Physical and material properties of a dehydrogenating catalyst of Chromium Oxide (Cr2O3) on Aluminum Oxide Support (Al2O3) were employed in the model. Several reaction models were implemented using a customized User-defined Function (UDF) subroutine. Simulation results were validated against literature data for a similar process. Good agreement was observed for the conversion of alkanes to alkenes within acceptable accuracy. It is concluded that the power-law model showed the least fit for the feed conversion and product selectivity compared to the other studied reaction models.
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LI, SA, and P. JENA. "DEHYDROGENATION MECHANISM FROM TITANIUM-ACTIVATED SODIUM ALANATE." In Proceedings of the International Symposium. WORLD SCIENTIFIC, 2009. http://dx.doi.org/10.1142/9789812838025_0009.

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Jones, Francis, Anand Kuppusamy, and Ai-Ping Zheng. "Dehydrogenation of cyclohexane to benzene in microreactors." In Symposium on Micromachining and Microfabrication, edited by Chong H. Ahn and A. Bruno Frazier. SPIE, 1999. http://dx.doi.org/10.1117/12.359333.

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Usman, Muhammad, and David Cresswell. "Dehydrogenation of Methylcyclohexane: Kinetics and Reactor Modeling." In 14th Asia Pacific Confederation of Chemical Engineering Congress. Singapore: Research Publishing Services, 2012. http://dx.doi.org/10.3850/978-981-07-1445-1_812.

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Uvarov, V. I., R. D. Kapustin, and A. O. Kirillov. "POWDER CONSOLIDATION USING TECHNOLOGICAL COMBUSTION FOR DEVELOPMENT OF CATALYTICALLY ACTIVE MEMBRANES FOR HYDROCARBON DEHYDROGENATION." In 9TH INTERNATIONAL SYMPOSIUM ON NONEQUILIBRIUM PROCESSES, PLASMA, COMBUSTION, AND ATMOSPHERIC PHENOMENA. TORUS PRESS, 2020. http://dx.doi.org/10.30826/nepcap9a-55.

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The work is devoted to the preparation of catalytically active membranes for the dehydrogenation of ethylbenzene to produce styrene which is necessary for the synthesis of numerous types of polymers, for example, polystyrene, styrene-modified polyesters, ABS (acrylonitrile-butadiene-styrene), and SAN (styrene-acrylonitrile) plastics. The global production of styrene in 2018 amounted to ~ 30 million tons, with up to 90% of styrene obtained by dehydrogenation of ethylbenzene in the presence of water vapor.
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Knyazheva, O. A., O. N. Baklanova, E. A. Buluchevskiy, M. V. Zhuravleva, and A. V. Lavrenov. "Propane dehydrogenation to propylene on oxidized carbon black." In INTERNATIONAL CONFERENCE ON PHYSICS AND CHEMISTRY OF COMBUSTION AND PROCESSES IN EXTREME ENVIRONMENTS (COMPHYSCHEM’20-21) and VI INTERNATIONAL SUMMER SCHOOL “MODERN QUANTUM CHEMISTRY METHODS IN APPLICATIONS”. AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0033079.

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Vicente Valverde, Isabel, Laia Gil Jiménez, Cyril Godard, and Aitor Gual Gozalbo. "Sustainable propene production by dehydrogenation with innovative nanocatalysts." In 15th Mediterranean Congress of Chemical Engineering (MeCCE-15). Grupo Pacífico, 2023. http://dx.doi.org/10.48158/mecce-15.t1-p-03.

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Reports on the topic "Dehydrogenation"

1

Heinekey, Dennis M. Catalysts for Dehydrogenation of ammonia boranes. Office of Scientific and Technical Information (OSTI), October 2009. http://dx.doi.org/10.2172/1165735.

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2

Stambuli, James P., and S. M. Whittemore. Site-selective Alkane Dehydrogenation of Fatty Acids. Fort Belvoir, VA: Defense Technical Information Center, December 2011. http://dx.doi.org/10.21236/ada566294.

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3

Sault, A. G., E. P. Boespflug, A. Martino, and J. S. Kawola. Selective dehydrogenation of propane over novel catalytic materials. Office of Scientific and Technical Information (OSTI), February 1998. http://dx.doi.org/10.2172/572628.

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SAULT, ALLEN G., JASON E. MUDD, JAMES E. MILLER, JUDITH A. RUFFNER, MARK A. RODRIGUEZ, and RALPH G. TISSOT, JR. Thin Film Models of Magnesium Orthovanadate Catalysts for Oxidative Dehydrogenation. Office of Scientific and Technical Information (OSTI), March 2001. http://dx.doi.org/10.2172/776352.

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Stepanenko, Sergey, Anton Koskin, Maria Alekseeva, Vasilii Kaichev, and Vadim Yakovlev. Nickel-tin alloy catalysts for liquid organic hydrogen carrier dehydrogenation. Peeref, July 2023. http://dx.doi.org/10.54985/peeref.2307p6337630.

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Cox, David. HYDROCARBON, OXIDATION, DEHYDROGENATION AND COUPLING OVER MODEL METAL OXIDE SURFACES. Office of Scientific and Technical Information (OSTI), January 2022. http://dx.doi.org/10.2172/1841755.

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7

Shamsuddin Ilias and Franklin G. King. Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor. Office of Scientific and Technical Information (OSTI), March 1997. http://dx.doi.org/10.2172/897396.

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Shamsuddin Ilias and Franklin G. King. Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor. Office of Scientific and Technical Information (OSTI), September 1997. http://dx.doi.org/10.2172/897398.

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Shamsuddin Ilias and Franklin G. King. Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor. Office of Scientific and Technical Information (OSTI), September 1998. http://dx.doi.org/10.2172/897406.

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Shamsuddin Ilias and Franklin G. King. Enhancement of Equilibriumshift in Dehydrogenation Reactions Using a Novel Membrane Reactor. Office of Scientific and Technical Information (OSTI), March 1999. http://dx.doi.org/10.2172/897407.

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