Relevant bibliographies by topics / Catalytic cracking

Academic literature on the topic 'Catalytic cracking'

Author: Grafiati
Published: 4 June 2021
Last updated: 1 March 2023

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Journal articles on the topic "Catalytic cracking"

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Herbst, J. A., H. Owen, and P. H. Schipper. "Catalytic cracking process." Zeolites 11, no. 3 (March 1991): 299. http://dx.doi.org/10.1016/s0144-2449(05)80249-0.

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Adewuyi, Y. G., P. M. Adornato, and J. S. Buchanan. "Fluidized catalytic cracking." Zeolites 15, no. 1 (January 1995): 84. http://dx.doi.org/10.1016/0144-2449(95)90250-3.

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Istadi, I., Teguh Riyanto, Luqman Buchori, Didi D. Anggoro, Andre W. S. Pakpahan, and Agnes J. Pakpahan. "Biofuels Production from Catalytic Cracking of Palm Oil Using Modified HY Zeolite Catalysts over A Continuous Fixed Bed Catalytic Reactor." International Journal of Renewable Energy Development 10, no. 1 (November 6, 2020): 149–56. http://dx.doi.org/10.14710/ijred.2021.33281.

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The increase in energy demand led to the challenging of alternative fuel development. Biofuels from palm oil through catalytic cracking appear as a promising alternative fuel. In this study, biofuel was produced from palm oil through catalytic cracking using the modified HY zeolite catalysts. The Ni and Co metals were impregnated on the HY catalyst through the wet-impregnation method. The catalysts were characterized using X-ray fluorescence, X-ray diffraction, Brunauer–Emmett–Teller (BET), Pyridine-probed Fourier-transform infrared (FTIR) spectroscopy, and Scanning Electron Microscopy (SEM) methods. The biofuels product obtained was analyzed using a gas chromatography-mass spectrometry (GC-MS) method to determine its composition. The metal impregnation on the HY catalyst could modify the acid site composition (Lewis and Brønsted acid sites), which had significant roles in the palm oil cracking to biofuels. Ni impregnation on HY zeolite led to the high cracking activity, while the Co impregnation led to the high deoxygenation activity. Interestingly, the co-impregnation of Ni and Co on HY catalyst could increase the catalyst activity in cracking and deoxygenation reactions. The yield of biofuels could be increased from 37.32% to 40.00% by using the modified HY catalyst. Furthermore, the selectivity of gasoline could be achieved up to 11.79%. The Ni and Co metals impregnation on HY zeolite has a promising result on both the cracking and deoxygenation process of palm oil to biofuels due to the role of each metal. This finding is valuable for further catalyst development, especially on bifunctional catalyst development for palm oil conversion to biofuels.
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Ryabov, V. D., M. A. Silin, O. B. Chernova, and I. A. Bronzova. "Catalytic cracking of triphenylethylene." Petroleum Chemistry 49, no. 4 (July 2009): 297–300. http://dx.doi.org/10.1134/s0965544109040069.

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Camblor, M. A., A. Corma, A. Martínez, F. A. Mocholí, and J. Pérez Pariente. "Catalytic cracking of gasoil." Applied Catalysis 55, no. 1 (November 1989): 65–74. http://dx.doi.org/10.1016/s0166-9834(00)82317-9.

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Wojciechowski, Bohdan W. "Dichotomies in Catalytic Cracking." Industrial & Engineering Chemistry Research 36, no. 8 (August 1997): 3323–35. http://dx.doi.org/10.1021/ie960642o.

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Dwyer, John, and David J. Rawlence. "Fluid catalytic cracking: chemistry." Catalysis Today 18, no. 4 (December 1993): 487–507. http://dx.doi.org/10.1016/0920-5861(93)80065-9.

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GONG, Jian-hong, Jun LONG, and You-hao XU. "Protolytic cracking in Daqing VGO catalytic cracking process." Journal of Fuel Chemistry and Technology 36, no. 6 (December 2008): 691–95. http://dx.doi.org/10.1016/s1872-5813(09)60005-0.

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Mannanova, G. I., and I. M. Gubaydullin. "Development of fifteen component kinetic model of catalytic cracking process." Computational Mathematics and Information Technologies 3, no. 2 (2019): 104–17. http://dx.doi.org/10.23947/2587-8999-2019-2-2-104-117.

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Wang, Yulong, Ruifang Zhao, Chun Zhang, Guanlong Li, Jing Zhang, and Fan Li. "The Investigation of Reducing PAHs Emission from Coal Pyrolysis by Gaseous Catalytic Cracking." Scientific World Journal 2014 (2014): 1–6. http://dx.doi.org/10.1155/2014/528413.

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The catalytic cracking method of PAHs for the pyrolysis gaseous products is proposed to control their pollution to the environment. In this study, the Py-GC-MS is used to investigate in situ the catalytic effect of CaO and Fe2O3on the 16 PAHs from Pingshuo coal pyrolysis under different catalytic temperatures and catalyst particle sizes. The results demonstrate that Fe2O3is effective than that of CaO for catalytic cracking of 16 PAHs and that their catalytic temperature corresponding to the maximum PAHs cracking rates is different. The PAHs cracking rate is up to 60.59% for Fe2O3at 600°C and is 52.88% at 700°C for CaO. The catalytic temperature and particle size of the catalysts have a significant effect on PAHs cracking rate and CaO will lose the capability of decreasing 16 PAHs when the temperature is higher than 900°C. The possible cracking process of 16 PAHs is deduced by elaborately analyzing the cracking effect of the two catalysts on 16 different species of PAHs.
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Dissertations / Theses on the topic "Catalytic cracking"

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Albahri, Tareq Abduljalil. "Mechanistic modeling of catalytic cracking chemistry /." Digital version accessible at:, 1999. http://wwwlib.umi.com/cr/utexas/main.

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Nazarudin, N. "Catalytic cracking of plastic waste using nanoporous materials." Thesis, University College London (University of London), 2012. http://discovery.ucl.ac.uk/1380400/.

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The catalytic cracking of linear low density polyethylene (lldPE), polypropylene (PP) and plastic waste were investigated using commercial zeolites (ZSM-5, zeolite β, Mordenite, and USY), USY modified by ion-exchange, mixed catalyst (ZSM-5/ zeolite β, ZSM-5/USY), and nanocrystaline-ZSM-5. USY was modified by ion-exchange with ammonium salt at two different temperatures (298K and 353K) and for various reaction times. The cracking of PP and lldPE was performed using mixed catalysts and in addition a detailed study was carried out employing statistical design of response surface methodology to obtain the optimum reaction condition to produce maximum products. Nano crystalline ZSM-5 catalysts were prepared with/without the presence of alcohol (ethanol and isopropanol) and sodium and statistical analysis of completely random design was used to determine the effect of these constituents in the reaction mixture on the characteristics of ZSM-5 material and on their catalytic performance. The catalytic studies using commercial zeolites revealed that the zeolite β and mordenite produced higher liquid yield from lldPE and plastic waste, respectively. However, by using a modified USY, by ion-exchange at temperature 298K for 48hours, a further improvement to the liquid yield was achieved. Using a mixer of ZSM-5/ zeolite β it was possible to achieve very good conversions for both lldPE and PP with least amount of coke formation. Further studies on catalytic cracking of lldPE using nanocrystalline ZSM-5 indicate that the highest liquid yield that could be achieved was by using the material synthesised in the presence of alcohol and sodium in the starting solution. The effect of constituents in the starting gel mixture for ZSM-5 synthesis appears to influence surface area, acidity and particle size; however it appears that this does not affect the catalytic performance for cracking of lldPE. However the study suggest that control of external surface area and particle size is highly significant.
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Sundaralingam, Ramasubramanian. "Optimization of a model IV fluidized catalytic cracking unit." Thesis, National Library of Canada = Bibliothèque nationale du Canada, 2001. http://www.collectionscanada.ca/obj/s4/f2/dsk3/ftp04/MQ58750.pdf.

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Idris, Muhammad Nuru. "Hydrodynamics and process modelling of fluid catalytic cracking reactors." Thesis, University of Leeds, 2010. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.531527.

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Crynes, Lawrence Lee. "Development of a novel monolith froth reactor for three-phase catalytic reactions /." Access abstract and link to full text, 1993. http://0-wwwlib.umi.com.library.utulsa.edu/dissertations/fullcit/9412289.

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Yu, Joyleene Ruth. "Bio-oil upgrading through biodiesel emulsification and catalytic vapour cracking." Thesis, University of British Columbia, 2014. http://hdl.handle.net/2429/46841.

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With our limited fuel supplies struggling to keep up with our ever-increasing demand for energy, and the rising trend towards sustainable and cleaner technologies, the need to harness the potential of bio-oil as an alternative source of energy has never been more compelling. Although crude bio-oil can already be utilized to supplement heating oils and boiler fuels, its greater value lies in its potential as a source of transportation fuels and chemicals after upgrading. In collaboration with Diacarbon Energy Inc., the main objectives of this project were twofold: (1) investigating the effect of extraction location from their proprietary pyrolysis unit on crude bio-oil quality prior to its emulsification with biodiesel, and characterizing the resulting biodiesel- and lignin-rich layers; and (2) designing and building a catalytic test unit to perform in situ cracking of slow pyrolysis vapours. Experimental results confirmed that extraction location does affect the crude bio-oil quality. The effect of the surfactant on the emulsification was minimal as the resulting biodiesel-rich layer from the emulsification without the surfactant showed similar improvements in terms of water content, viscosity, TAN and HHV. A water mass balance confirmed that the majority of the water (~97%) is retained in the lignin-rich phase after emulsification. This is significant because the solvency of biodiesel can be utilized to upgrade bio-oils by selectively extracting its desirable fuel components into a biodiesel-rich phase, which can then be easily separated from the lignin- rich phase where the higher molecular weight compounds, such as pyrolytic lignin, as well as the majority of the water, are retained. The bio-oil samples obtained from the non-catalytic and catalytic vapour cracking experiments separated into two distinct layers – an aqueous and organic layer. While the aqueous layers were fairly similar in nature, the organic layer from the catalytic experiment showed a significant decrease in viscosity (94.3% less) and water content (64.3% less). The organic layer from the catalytic pyrolysis remained homogeneous while that from the non-catalytic pyrolysis split into a hazy aqueous layer (with suspended oil droplets) sandwiched between a thin organic layer on top and a thicker organic layer at the bottom.
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Prado, Juan Luis Gomez. "Intergrated Methodology for the Modelling of Refinery Fluid Catalytic Cracking Units." Thesis, University of Manchester, 2009. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.505488.

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Galligan, Carrie. "Catalytic Cracking of Jet Propellant-10. For Pulse Detonation Engine Applications." Thesis, Université Laval, 2005. http://www.theses.ulaval.ca/2005/22529/22529.pdf.

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Le carburant hydrocarbure JP-10 est étudié comme agent propulsif destiné aux moteurs à détonation ainsi qu’à d’autres applications concernant les vols à vitesses élevées. La précraquage catalytique du JP-10 pourrait produire un mélange d’oléfines légères plus facile à détoner. Un mélange d’hydrocarbures aliphatiques, pour la plupart légers, présente l’avantage d’être moins enclin à la carbonisation que des mélanges comportant de fortes teneurs en hydrocarbures aromatiques. Cette réaction endothermique de précraquage offre le même potentiel que celui d’un puits de chaleur trouvé dans des applications de vols à vitesses élevées pour lesquelles toute hausse de la masse du système de refroidissement contrevient à une plus grande efficacité du moteur. Plusieurs essais de craquage catalytique hétérogène furent réalisés à l’aide d’un réacteur tubulaire et les gaz produits analysés par GC/MS et par GC. Deux formes de zéolithe nanocristalline (n) ZSM-5(24h) et nZSM-5 (6h) et trois formes de silico-aluminophosphate SAPO-5A, SAPO-5B et SAPO-11 furent testées. SAPO-5 et nZSM-5(24h) apparaissent être les candidats les plus propices au précraquage du JP-10. Ces dernières ont permis de convertir plus de 90 % de JP-10 en un mélange d’hydrocarbures principalement composé de molécules en C4 et moins (C3 à C1). nZSM-5(24h) ont procuré le plus petit rapport de masse de carbone, CR (C5+:C4−), à des températures situées entre 350 oC et 450 oC et le taux de conversion le plus élevé à des températures supérieures à 500 oC. SAPO-5A & B ont présenté le taux de conversion le plus élevé mais le plus petit CR entre 400 oC et 500 oC.
The hydrocarbon jet-fuel, JP-10, is being studied as a possible propellant for the Pulse Detonation Engine (PDE) and other high-speed flight applications. Catalytic pre-cracking of JP-10 could provide a more easily detonated mixture of light olefin products. A mixture of mostly light hydrocarbons has the added benefit of being less prone to coking than a product mixture heavy in aromatics. This endothermic reaction also offers potential as a heat sink in high-speed flight applications where the extra weight of an onboard cooling system would hinder engine efficiency. Several heterogeneous catalytic cracking tests have been done using a Bench Top Tubular Reactor and the products were analyzed with GC/MS and GC. Two forms of nanocrystalline zeolites, nZSM-5(24h) and nZSM-5(6h), and three forms of silico-alumino-phosphates, SAPO-5A, SAPO-5B, and SAPO-11 successfully catalyzed the cracking of JP-10; however, SAPO-5 and nZSM-5(24h) have proven to be the most promising catalyts. Both catalysts converted over 90 % of JP-10 (∼ 3s residence time) into a mixture of hydrocarbon products consisting mainly of C4 and lower chain hydrocarbons (C3 to C1). nZSM-5(24h) demonstrated the lowest carbon mass ratio, CR (C5+:C4−), between 350 oC and 450 oC and the highest conversion rates above 500 oC. SAPO-5A & B demonstrated the highest conversion rates and the lowest CR between 400 oC and 500 oC.
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Panpranot, Joongjai. "Hydrothermal aging of zeolite-based catalysts." Morgantown, W. Va. : [West Virginia University Libraries], 1998. http://etd.wvu.edu/templates/showETD.cfm?recnum=274.

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Thesis (M.S.)--West Virginia University, 1998.
Title from document title page. Document formatted into pages; contains xi, 84 p. : ill. Includes abstract. Includes bibliographical references (p. 64-67).
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Bayraktar, Oguz. "Effect of pretreatment on the performance of metal contaminated commercial FCC catalyst." Morgantown, W. Va. : [West Virginia University Libraries], 2001. http://etd.wvu.edu/templates/showETD.cfm?recnum=2071.

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Thesis (Ph. D.)--West Virginia University, 2001.
Title from document title page. Document formatted into pages; contains xvi, 214 p. : ill. (some col.). Includes abstract. Includes bibliographical references (p. 199-208).
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Books on the topic "Catalytic cracking"

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Occelli, Mario L., ed. Fluid Catalytic Cracking. Washington, DC: American Chemical Society, 1988. http://dx.doi.org/10.1021/bk-1988-0375.

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Occelli, Mario L., and Paul O'Connor, eds. Fluid Catalytic Cracking III. Washington, DC: American Chemical Society, 1994. http://dx.doi.org/10.1021/bk-1994-0571.

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Occelli, Mario L., ed. Fluid Catalytic Cracking II. Washington, DC: American Chemical Society, 1991. http://dx.doi.org/10.1021/bk-1991-0452.

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Sadeghbeigi, Reza. Fluid catalytic cracking handbook. Houston, Tex: Gulf Pub. Co., 1995.

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1942-, Occelli Mario L., O'Connor Paul 1956-, and American Chemical Society. Division of Petroleum Chemistry., eds. Fluid catalytic cracking III: Materials and processes. Washington, D.C: American Chemical Society, 1994.

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1948-, Young George W., Benslay Roger M. 1941-, and American Institute of Chemical Engineers., eds. Advanced fluid catalytic cracking technology. New York, N.Y: American Institute of Chemical Engineers, 1992.

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Wilson, Joseph W. Fluid catalytic cracking technolgy and operations. Tulsa, OK: PenWell Pub. Co., 1997.

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1942-, Occelli Mario L., and O'Connor Paul 1956-, eds. Fluid cracking catalysts. New York: M. Dekker, 1998.

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1951-, Corma Avelino, ed. Catalytic cracking: Catalysts, chemistry, and kinetics. New York: M. Dekker, 1986.

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Magee, J. S. Petroleum catalysis in nontechnical language. Tulsa, OK: PennWell, 1998.

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Book chapters on the topic "Catalytic cracking"

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Lloyd, Lawrie. "Catalytic Cracking Catalysts." In Handbook of Industrial Catalysts, 169–210. Boston, MA: Springer US, 2011. http://dx.doi.org/10.1007/978-0-387-49962-8_5.

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Avidan, Amos A. "Fluid catalytic cracking." In Circulating Fluidized Beds, 466–88. Dordrecht: Springer Netherlands, 1997. http://dx.doi.org/10.1007/978-94-009-0095-0_13.

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Speight, James G. "Catalytic Cracking Processes." In Thermal and Catalytic Processing in Petroleum Refining Operations, 185–240. Boca Raton: CRC Press, 2023. http://dx.doi.org/10.1201/9781003184904-5.

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Speight, James G. "Fluid-Bed Catalytic Cracking." In Springer Handbook of Petroleum Technology, 617–48. Cham: Springer International Publishing, 2017. http://dx.doi.org/10.1007/978-3-319-49347-3_19.

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"Catalytic Cracking." In Petroleum Refining Design and Applications Handbook, 259–304. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2018. http://dx.doi.org/10.1002/9781119257110.ch8.

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Speight, James G. "Catalytic Cracking." In Heavy and Extra-heavy Oil Upgrading Technologies, 39–67. Elsevier, 2013. http://dx.doi.org/10.1016/b978-0-12-404570-5.00003-x.

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Speight, James G. "Catalytic cracking." In The Refinery of the Future, 197–226. Elsevier, 2020. http://dx.doi.org/10.1016/b978-0-12-816994-0.00006-3.

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"Catalytic Cracking." In Petroleum Refining Processes, 388–438. CRC Press, 2001. http://dx.doi.org/10.1201/b17048-16.

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"Catalytic Cracking." In The Chemistry and Technology of Petroleum, 603–21. CRC Press, 1999. http://dx.doi.org/10.1201/9780824742119-19.

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"Catalytic Cracking." In Chemical Industries, 585–603. CRC Press, 1999. http://dx.doi.org/10.1201/9780824742119.ch15.

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Conference papers on the topic "Catalytic cracking"

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Jaimon, Anjusha P., and P. Subha Hency Jose. "Temperature control of catalytic cracking process." In 2015 International Conference on Innovations in Information,Embedded and Communication Systems (ICIIECS). IEEE, 2015. http://dx.doi.org/10.1109/iciiecs.2015.7192960.

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Zsemberi, Andor, Zoltán Siménfalvi, and Árpád Bence Palotás. "Thermal and Thermo Catalytic Co-Cracking." In MultiScience - XXX. microCAD International Multidisciplinary Scientific Conference. University of Miskolc, 2016. http://dx.doi.org/10.26649/musci.2016.107.

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Fan, Xuejun, Gong Yu, Jianguo Li, X. Lu, and Chih-Jen Sung. "Catalytic Cracking of Supercritical Aviation Kerosene." In 42nd AIAA/ASME/SAE/ASEE Joint Propulsion Conference & Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2006. http://dx.doi.org/10.2514/6.2006-4868.

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Najjar, Yousef S. H. "Energy Conservation With Catalytic Cracking in the Refinery." In ASME 1990 International Gas Turbine and Aeroengine Congress and Exposition. American Society of Mechanical Engineers, 1990. http://dx.doi.org/10.1115/90-gt-181.

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Fluidized-bed catalytic cracking is one of the most commonly used processes in petroleum refining to convert heavy high-boiling point components of crude oil into gasoline and distillate components. An energy conservation measure for such a process, utilizes an axial flow compressor which furnishes air for combustion in the regenerator where the coke deposits are burned off the catalyst and also drives the catalyst through the system. The flue gases from the regenerator are expanded in an expansion turbine which drives the compressor, whereas the excess energy is used to drive an electric generator. The exhaust gases are utilized further in a heat recovery boiler to produce process steam. A parametric study involving variation of air pressure and expander inlet temperature using specially devised computer program, was used to analyse the performance of the proposed system. Furthermore, the system is economically evaluated and compared with the conventional cracking system using a gas turbine engine. The proposed system offers leading performance and economic advantages in comparison with the conventional one.
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Ghosh, Sobhan, Swapan Paruya, Samarjit Kar, and Suchismita Roy. "Development Of Simulation Model For Fluid Catalytic Cracking." In INTERNATIONAL CONFERENCE ON MODELING, OPTIMIZATION, AND COMPUTING (ICMOS 20110). AIP, 2010. http://dx.doi.org/10.1063/1.3516347.

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Altynkovich, E. O., K. S. Plekhova, E. V. Gaifullina, O. V. Potapenko, T. P. Sorokina, and V. P. Doronin. "Catalytic cracking of butanols and butane-butylene fractions." In 21ST CENTURY: CHEMISTRY TO LIFE. AIP Publishing, 2019. http://dx.doi.org/10.1063/1.5122911.

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Puebla, Hector, Jesus Valencia, and Jose Alvarez-Ramirez. "Multivariable control configurations for fluid catalytic cracking units." In 2003 European Control Conference (ECC). IEEE, 2003. http://dx.doi.org/10.23919/ecc.2003.7085158.

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Cooper, Marcia, and Joseph Shepherd. "Experiments Studying Thermal Cracking, Catalytic Cracking, and Pre-Mixed Partial Oxidation of JP-10." In 39th AIAA/ASME/SAE/ASEE Joint Propulsion Conference and Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2003. http://dx.doi.org/10.2514/6.2003-4687.

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Wei Li, Hong-Ye Su, Ou-Guan Xu, and Jian Chu. "Eight lumps kinetic model for residual oil catalytic cracking." In 2010 8th World Congress on Intelligent Control and Automation (WCICA 2010). IEEE, 2010. http://dx.doi.org/10.1109/wcica.2010.5554714.

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Boum, Alexandre Teplaira, Abderrazak Latifi, and Jean-Pierre Corriou. "Model predictive control of a fluid catalytic cracking unit." In 2013 International Conference on Process Control (PC). IEEE, 2013. http://dx.doi.org/10.1109/pc.2013.6581433.

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Reports on the topic "Catalytic cracking"

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Ng, S., and E. Castellanos. Catalytic cracking of deasphalted non-conventional residues. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1992. http://dx.doi.org/10.4095/304564.

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Ng, S. H., L. E. Curts, and K. R. Dymock. Catalytic cracking of hydrotreated conventional and synthetic feedstocks. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1987. http://dx.doi.org/10.4095/302678.

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Larocca, M., S. Ng, and H. de Lasa. Fast catalytic cracking of heavy gas oils: modeling coke deactivation. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1990. http://dx.doi.org/10.4095/304414.

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Rappe, A. K. Theoretical modeling of catalytic processes: Hydrocarbon oxidation and cracking. Final report. Office of Scientific and Technical Information (OSTI), September 1996. http://dx.doi.org/10.2172/378799.

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Ng, S. H. Catalytic cracking of raw and hydrotreated gas oils from coprocessed distillate. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1993. http://dx.doi.org/10.4095/304586.

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Ng, S. H., H. Seoud, M. Stanciulescu, and Y. Sugimoto. Conversion of polyethylene to transportation fuels through pyrolysis and catalytic cracking. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1994. http://dx.doi.org/10.4095/304612.

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Ng, S., and M. Ternan. Fluid catalytic cracking microactivity tests (MAT) using ADVENT's catalyst no. 200-AS. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1988. http://dx.doi.org/10.4095/304387.

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Timpe, R. C. Energy and environmental research emphasizing low-rank coal: Task 3.9 catalytic tar cracking. Office of Scientific and Technical Information (OSTI), September 1995. http://dx.doi.org/10.2172/207044.

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Young, B. C., and R. C. Timpe. Task 3.9 -- Catalytic tar cracking. Semi-annual report, January 1--June 30, 1995. Office of Scientific and Technical Information (OSTI), December 1995. http://dx.doi.org/10.2172/650108.

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10

Schwartz, M. M., W. J. Reagon, J. J. Nicholas, and R. D. Hughes. The selective catalytic cracking of Fischer-Tropsch liquids to high value transportation fuels. Final report. Office of Scientific and Technical Information (OSTI), November 1994. http://dx.doi.org/10.2172/10190757.

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