Gotowe bibliografie tematyczne / Catalytic cracking

Gotowa bibliografia na temat „Catalytic cracking”

Autor: Grafiati
Data publikacji: 4 czerwca 2021
Data aktualizacji: 1 marca 2023

Utwórz poprawne odniesienie w stylach APA, MLA, Chicago, Harvard i wielu innych

Wybierz rodzaj źródła:

Spis treści

Zobacz listy aktualnych artykułów, książek, rozpraw, streszczeń i innych źródeł naukowych na temat „Catalytic cracking”.

Przycisk „Dodaj do bibliografii” jest dostępny obok każdej pracy w bibliografii. Użyj go – a my automatycznie utworzymy odniesienie bibliograficzne do wybranej pracy w stylu cytowania, którego potrzebujesz: APA, MLA, Harvard, Chicago, Vancouver itp.

Możesz również pobrać pełny tekst publikacji naukowej w formacie „.pdf” i przeczytać adnotację do pracy online, jeśli odpowiednie parametry są dostępne w metadanych.

Artykuły w czasopismach na temat "Catalytic cracking"

1

Herbst, J. A., H. Owen i P. H. Schipper. "Catalytic cracking process". Zeolites 11, nr 3 (marzec 1991): 299. http://dx.doi.org/10.1016/s0144-2449(05)80249-0.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

Adewuyi, Y. G., P. M. Adornato i J. S. Buchanan. "Fluidized catalytic cracking". Zeolites 15, nr 1 (styczeń 1995): 84. http://dx.doi.org/10.1016/0144-2449(95)90250-3.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
3

Istadi, I., Teguh Riyanto, Luqman Buchori, Didi D. Anggoro, Andre W. S. Pakpahan i 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, nr 1 (6.11.2020): 149–56. http://dx.doi.org/10.14710/ijred.2021.33281.

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
4

Ryabov, V. D., M. A. Silin, O. B. Chernova i I. A. Bronzova. "Catalytic cracking of triphenylethylene". Petroleum Chemistry 49, nr 4 (lipiec 2009): 297–300. http://dx.doi.org/10.1134/s0965544109040069.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
5

Camblor, M. A., A. Corma, A. Martínez, F. A. Mocholí i J. Pérez Pariente. "Catalytic cracking of gasoil". Applied Catalysis 55, nr 1 (listopad 1989): 65–74. http://dx.doi.org/10.1016/s0166-9834(00)82317-9.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

Wojciechowski, Bohdan W. "Dichotomies in Catalytic Cracking". Industrial & Engineering Chemistry Research 36, nr 8 (sierpień 1997): 3323–35. http://dx.doi.org/10.1021/ie960642o.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
7

Dwyer, John, i David J. Rawlence. "Fluid catalytic cracking: chemistry". Catalysis Today 18, nr 4 (grudzień 1993): 487–507. http://dx.doi.org/10.1016/0920-5861(93)80065-9.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

GONG, Jian-hong, Jun LONG i You-hao XU. "Protolytic cracking in Daqing VGO catalytic cracking process". Journal of Fuel Chemistry and Technology 36, nr 6 (grudzień 2008): 691–95. http://dx.doi.org/10.1016/s1872-5813(09)60005-0.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
9

Mannanova, G. I., i I. M. Gubaydullin. "Development of fifteen component kinetic model of catalytic cracking process". Computational Mathematics and Information Technologies 3, nr 2 (2019): 104–17. http://dx.doi.org/10.23947/2587-8999-2019-2-2-104-117.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
10

Wang, Yulong, Ruifang Zhao, Chun Zhang, Guanlong Li, Jing Zhang i 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.

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
Więcej źródeł

Rozprawy doktorskie na temat "Catalytic cracking"

1

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

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

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
3

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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
4

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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
5

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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

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.

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
7

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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

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.

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
9

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.

Pełny tekst źródła
Streszczenie:
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).
Style APA, Harvard, Vancouver, ISO itp.
10

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.

Pełny tekst źródła
Streszczenie:
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).
Style APA, Harvard, Vancouver, ISO itp.
Więcej źródeł

Książki na temat "Catalytic cracking"

1

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
3

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
4

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
5

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
7

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
9

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
10

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

Znajdź pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
Więcej źródeł

Części książek na temat "Catalytic cracking"

1

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
3

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
4

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
5

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
7

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
9

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
10

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.

Streszczenia konferencji na temat "Catalytic cracking"

1

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
3

Fan, Xuejun, Gong Yu, Jianguo Li, X. Lu i Chih-Jen Sung. "Catalytic Cracking of Supercritical Aviation Kerosene". W 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
4

Najjar, Yousef S. H. "Energy Conservation With Catalytic Cracking in the Refinery". W 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.

Pełny tekst źródła
Streszczenie:
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.
Style APA, Harvard, Vancouver, ISO itp.
5

Ghosh, Sobhan, Swapan Paruya, Samarjit Kar i Suchismita Roy. "Development Of Simulation Model For Fluid Catalytic Cracking". W INTERNATIONAL CONFERENCE ON MODELING, OPTIMIZATION, AND COMPUTING (ICMOS 20110). AIP, 2010. http://dx.doi.org/10.1063/1.3516347.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
7

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

Cooper, Marcia, i Joseph Shepherd. "Experiments Studying Thermal Cracking, Catalytic Cracking, and Pre-Mixed Partial Oxidation of JP-10". W 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
9

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
10

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.

Raporty organizacyjne na temat "Catalytic cracking"

1

Ng, S., i 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
2

Ng, S. H., L. E. Curts i 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
3

Larocca, M., S. Ng i 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
4

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
5

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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
6

Ng, S. H., H. Seoud, M. Stanciulescu i 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
7

Ng, S., i 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.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
8

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
9

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

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
10

Schwartz, M. M., W. J. Reagon, J. J. Nicholas i 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), listopad 1994. http://dx.doi.org/10.2172/10190757.

Pełny tekst źródła
Style APA, Harvard, Vancouver, ISO itp.
Możesz być także zainteresowany rozszerzonymi bibliografiami na temat „Catalytic cracking” dla poszczególnych typów źródeł:
Artykuły w czasopismach Rozprawy doktorskie Książki
Oferujemy zniżki na wszystkie plany premium dla autorów, których prace zostały uwzględnione w tematycznych zestawieniach literatury. Skontaktuj się z nami, aby uzyskać unikalny kod promocyjny!

Do bibliografii