Relevant bibliographies by topics / Spent catalytic cracking catalyst

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Spent catalytic cracking catalyst'

Author: Grafiati
Published: 29 September 2021
Last updated: 30 July 2025

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Journal articles on the topic "Spent catalytic cracking catalyst"

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Wang, Chuansheng, Xiaolong Tian, Baishun Zhao, Lin Zhu, and Shaoming Li. "Experimental Study on Spent FCC Catalysts for the Catalytic Cracking Process of Waste Tires." Processes 7, no. 6 (2019): 335. http://dx.doi.org/10.3390/pr7060335.

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Research on the synergistic high-value reuse of waste tires and used catalysts in spent fluid catalytic cracking (FCC) catalysts was carried out in this study to address the serious ecological and environmental problems caused by waste tires and spent FCC catalysts. The experiment, in which a spent FCC catalyst was applied to the catalytic cracking of waste tires, fully utilized the residual activity of the spent FCC catalyst and was compared with a waste tire pyrolysis experiment. The comparative experimental results indicated that the spent FCC catalyst could improve the cracking efficiency
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Sun, D., X. Z. Li, M. Brungs, and D. Trimm. "Encapsulation of heavy metals on spent fluid catalytic cracking catalyst." Water Science and Technology 38, no. 4-5 (1998): 211–17. http://dx.doi.org/10.2166/wst.1998.0625.

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Vanadium and nickel were found as major contaminants on spent FCC catalyst at levels of 3518 ppm and 3225 ppm, respectively. XPS results indicated that vanadium and nickel were in oxide form on spent FCC catalysts. Leaching tests (TCLP) showed that vanadium from spent FCC catalysts poses an environmental problem if disposed by landfill. It was found that encapsulation treatment with up to 60 wt % spent FCC catalyst in Portland cement, is an effective means of stabilization. The strength of standard specimens containing catalyst was much lower than that of standard specimens made with same weig
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Fu, Haihui, Yan Chen, Tingting Liu, Xuemei Zhu, Yufei Yang, and Haitao Song. "Research on Hazardous Waste Removal Management: Identification of the Hazardous Characteristics of Fluid Catalytic Cracking Spent Catalysts." Molecules 26, no. 8 (2021): 2289. http://dx.doi.org/10.3390/molecules26082289.

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Fluid catalytic cracking (FCC) spent catalysts are the most common catalysts produced by the petroleum refining industry in China. The National Hazardous Waste List (2016 edition) lists FCC spent catalysts as hazardous waste, but this listing is very controversial in the petroleum refining industry. This study collects samples of waste catalysts from seven domestic catalytic cracking units without antimony-based passivation agents and identifies their hazardous characteristics. FCC spent catalysts do not have the characteristics of flammability, corrosiveness, reactivity, or infectivity. Based
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Nasution, A. S., and E. Jasjfi. "THE MANAGEMENT OF SPENT CATALYST IN RCC/FCC UNITS IN ASEAN REFINERIES." Scientific Contributions Oil and Gas 28, no. 3 (2022): 10–15. http://dx.doi.org/10.29017/scog.28.3.1041.

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Catalytic cracking processes convert heavy feed- stock (heavy distillate, residue) into gasoline and light cycle stock for middle distillate components. Due to high impurity of feedstock and limited operating condition of catalyst regeneration, fresh catalyst must be added to replace a portion of spent catalyst continously, to maintain the activity of equilibrium catalyst in the reactor. Spent catalyst must be disposed properly so that it does not cause hazard or environmental concern. A survey was conducted on the management of spent catalyst in RCC/FCC unit in ASEAN refineries as an ASCOPE T
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Musa, Mohd Lukman, Ramli Mat, and Tuan Amran Tuan Abdullah. "Catalytic Conversion of Residual Palm Oil in Spent Bleaching Earth (SBE) By HZSM-5 Zeolite based-Catalysts." Bulletin of Chemical Reaction Engineering & Catalysis 13, no. 3 (2018): 456. http://dx.doi.org/10.9767/bcrec.13.3.1929.456-465.

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Bleaching earth is used to remove colour, phospholipids, oxidized products, metals and residual gums in the palm oil process refinery. Once adsorption process end, the spent bleaching earth (SBE) which contains approximately 20-40 wt. % of the adsorbed oil was usually disposed to landfills. The oil content in SBE was recovered by catalytic cracking using transition metal (Cu, Zn, Cr, and Ni) doped HZSM-5 zeolite in a batch reactor (pyrolysis zone) and fixed bed reactor (catalyst bed). The 5 wt. % of each metallic was introduced in HZSM-5 zeolite using incipient wetness impregnation method. The
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Al-Zubaidi, Isam, and Congning Yang. "Waste Management of Spent Petroleum Refinery Catalyst." European Journal of Engineering Research and Science 5, no. 8 (2020): 938–47. http://dx.doi.org/10.24018/ejers.2020.5.8.1929.

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Petroleum refinery uses many catalysts such as hydroprocessing catalyst HPC, fluid catalytic cracking catalyst FCCC, reforming catalyst RC, etc. During the refining processes, the catalysts are deactivated; the spent catalysts are regarded as hazardous toxic materials due to heavy metals, coke, other poisonous compounds, and hydrocarbons. Huge amount of spent catalysts SC is generated which is expected to increase with expansion capacities of available refineries processes. This paper is reviewing the mechanisms of refining catalyst and the deactivation processes and focusing on spent catalyst
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Al-Zubaidi, Isam, and Congning Yang. "Waste Management of Spent Petroleum Refinery Catalyst." European Journal of Engineering and Technology Research 5, no. 8 (2020): 938–47. http://dx.doi.org/10.24018/ejeng.2020.5.8.1929.

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Petroleum refinery uses many catalysts such as hydroprocessing catalyst HPC, fluid catalytic cracking catalyst FCCC, reforming catalyst RC, etc. During the refining processes, the catalysts are deactivated; the spent catalysts are regarded as hazardous toxic materials due to heavy metals, coke, other poisonous compounds, and hydrocarbons. Huge amount of spent catalysts SC is generated which is expected to increase with expansion capacities of available refineries processes. This paper is reviewing the mechanisms of refining catalyst and the deactivation processes and focusing on spent catalyst
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Istadi, Istadi, Luqman Buchori, Didi Dwi Anggoro, et al. "Effects of Ion Exchange Process on Catalyst Activity and Plasma-Assisted Reactor Toward Cracking of Palm Oil into Biofuels." Bulletin of Chemical Reaction Engineering & Catalysis 14, no. 2 (2019): 459. http://dx.doi.org/10.9767/bcrec.14.2.4257.459-467.

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Biofuels can be produced through a conventional catalytic cracking system and/or a hybrid catalytic-plasma cracking system. This paper was focused on studying effect of Na+ ion exchange to HY-Zeolite catalyst on catalyst performance to convert palm oil into biofuels over a conventional continuous fixed bed catalytic cracking reactor and comparing the catalytic cracking performance when carried out in a continuous hybrid catalytic-plasma reactor. The catalysts were characterized by X-ray Diffraction (XRD) and Bruneuer-Emmet-Teller (BET) surface area methods. The biofuels product were analyzed u
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Wang, Guangjian, Kai Lu, Chaoqun Yin та ін. "One-Step Fabrication of PtSn/γ-Al2O3 Catalysts with La Post-Modification for Propane Dehydrogenation". Catalysts 10, № 9 (2020): 1042. http://dx.doi.org/10.3390/catal10091042.

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The catalytic dehydrogenation of propane to propene is an alternative technique to supplement the traditional steam cracking and catalytic cracking process for satisfying the continuously increasing demand for propylene downstream products. In this study, the parent PtSn/γ-Al2O3 catalyst was fabricated via the one-step method for the subsequent La post-modification to prepare the catalysts for propane dehydrogenation. The prepared and spent catalysts were characterized by X-ray diffraction (XRD), N2 adsorption–desorption, scanning electron microscope (SEM), NH3 temperature-programmed desorptio
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Chen, Xiaopeng, Lu Ren, Muhammad Yaseen, et al. "Synthesis, characterization and activity performance of nickel-loaded spent FCC catalyst for pine gum hydrogenation." RSC Advances 9, no. 12 (2019): 6515–25. http://dx.doi.org/10.1039/c8ra07943a.

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Dissertations / Theses on the topic "Spent catalytic cracking catalyst"

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Martes, Hernández Leonela. "Catalytic cracking of tar model compounds using biochar as catalyst." Electronic Thesis or Diss., Normandie, 2025. http://www.theses.fr/2025NORMIR02.

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Cette thèse se concentre sur l'étude du craquage catalytique des goudrons, qui sont des substances pouvant être produites avec le gaz de synthèse et le biochar pendant la gazéification de la biomasse. Les goudrons constituent un des principaux obstacles à l’utilisation du gaz de synthèse dans certains procédés industriels en raison des difficultés techniques liées à leur présence (obstruction, condensation, réduction de l'efficacité énergétique, etc.). Le craquage catalytique est une technique de choix pour transformer ces goudrons, composés d’hydrocarbures lourds (C6, C7, C8, etc.) en espèces
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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.<br>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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Madadkhani, Shiva. "Red mud as an iron-based catalyst for catalytic cracking of naphthalene." Thesis, University of British Columbia, 2016. http://hdl.handle.net/2429/60118.

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Reducing the tar content in the producer gas of biomass gasification processes remains one of the main challenges in the commercialization of this technology and, hence, the development of clean and economical tar-removing technologies is becoming increasingly important. Catalytic tar removal has the advantage of avoiding expensive gas cleaning systems while maintaining the sensible heat in the producer gas. Commercial catalysts based on noble metals and metal oxides have shown good activity towards tar destruction, but are prone to rapid deactivation. This in addition to the high replacement
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Beskari, Mohamed Ali. "Dynamic analysis of diffusion and convection in porous catalysts." Thesis, University of Salford, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.244857.

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Villca, Pozo Ariel Rey. "Utilización de geopolímero para la mejora de las propiedades en morteros cal-puzolana y su empleo en países en desarrollo." Doctoral thesis, Universitat Politècnica de València, 2021. http://hdl.handle.net/10251/172663.

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[ES] El descubrimiento del cemento Portland ha cambiado nuestra forma de construir, pero también es el responsable de grandes emisiones de CO2 a la atmósfera durante su fabricación (~1450 ᴼC), agravando la crisis actual que está sufriendo nuestro planeta debido al cambio climático y sus consecuencias en todo el medio ambiente. Por lo tanto, una alternativa más sostenible en la construcción es la utilización de la cal que necesita menor temperatura para su fabricación (~900 ᴼC). Si bien la introducción de puzolanas naturales o artificiales en morteros de cal han mejorado sus propiedades mec
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Whitcombe, Joshua Matthew, and n/a. "Study of Catalyst Particle Emissions From a Fluidized Catalytic Cracker Unit." Griffith University. School of Environmental Engineering, 2003. http://www4.gu.edu.au:8080/adt-root/public/adt-QGU20031003.152200.

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The control of particle emissions from an oil refinery is often difficult, due to changing operational conditions and the limited range of available treatment options. Excessive particle emissions have often been attributed start up problems with Fluidized Catalytic Cracker Units (FCCU) and little information is available regarding the exact composition and nature of these excessive emissions. Due to the complex nature of a FCCU, it has in the past been difficult to identify and control emissions, without the use of expensive end of pipe technologies. An Australian Oil Refinery, concerned wi
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Whitcombe, Joshua Matthew. "Study of Catalyst Particle Emissions From a Fluidized Catalytic Cracker Unit." Thesis, Griffith University, 2003. http://hdl.handle.net/10072/367301.

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The control of particle emissions from an oil refinery is often difficult, due to changing operational conditions and the limited range of available treatment options. Excessive particle emissions have often been attributed start up problems with Fluidized Catalytic Cracker Units (FCCU) and little information is available regarding the exact composition and nature of these excessive emissions. Due to the complex nature of a FCCU, it has in the past been difficult to identify and control emissions, without the use of expensive end of pipe technologies. An Australian Oil Refinery, concerned wi
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Bruening, Christopher. "Decalin Dehydrogenation for In-Situ Hydrogen Production to Increase Catalytic Cracking Rate of n-Dodecane." University of Dayton / OhioLINK, 2018. http://rave.ohiolink.edu/etdc/view?acc_num=dayton1525100991525704.

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Al-Rubaye, Rana. "Generation and characterisation of catalytic films of zeolite Y and ZSM-5 on FeCrAlloy metal." Thesis, University of Manchester, 2013. https://www.research.manchester.ac.uk/portal/en/theses/generation-and-characterisation-of-catalytic-films-of-zeolite-y-and-zsm5-on-fecralloy-metal(de743286-52bd-4922-8de7-9a261283b6e5).html.

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The objective of this work was the development of structured zeolite catalysts by growing of ZSM-5 and Y zeolites layers on the pre-treated FeCrAlloy wires, which could now offer technical advantage in catalytic application. The advantages of implementation of zeolitic coatings in industrial applications are that they have; lower pressure drop, high heat and mass transfer rates compared to standard pelleted or extruded catalysts. The key focus of this research was the generation of thin films of zeolite ZSM–5 and Y zeolite catalysts on the surface of a FeCrAlloy metal substrate. Using in-situ
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Pashikanti, Kiran. "Predictive Modeling of Large-Scale Integrated Refinery Reaction and Fractionation Systems from Plant Data: Fluid Catalytic Cracking (FCC) and Continuous Catalyst Regeneration (CCR) Catalytic Reforming Processes." Diss., Virginia Tech, 2011. http://hdl.handle.net/10919/77181.

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This dissertation includes two accounts of rigorous modeling of petroleum refinery modeling using rigorous reaction and fractionation units. The models consider various process phenomena and have been extensively used during a course of a six-month study to understand and predict behavior. This work also includes extensive guides to allow users to develop similar models using commercial software tools. (1) Predictive Modeling of Large-Scale Integrated Refinery Reaction and Fractionation Systems from Plant Data: Fluid Catalytic Cracking (FCC) Process with Planning Applications: This work presen
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Books on the topic "Spent catalytic cracking catalyst"

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Fluid catalytic cracking II: Concepts in catalyst design. American Chemical Society, 1991.

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Occelli, Mario L. Fluid Catalytic Cracking II: Concepts in Catalyst Design (Acs Symposium Series). An American Chemical Society Publication, 1991.

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Book chapters on the topic "Spent catalytic cracking catalyst"

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O'Connor, Paul, E. Brevoord, A. C. Pouwels, and H. N. J. Wijngaards. "Catalyst Deactivation in Fluid Catalytic Cracking." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch010.

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Zhao, Xinjin, and Wu-Cheng Cheng. "Sodium Deactivation of Fluid Catalytic Cracking Catalyst." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch011.

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Ramakrishna, D. Venkata, Lakshmana Rao Jeeru, and Narayan C. Pradhan. "Cracking of Heavy Oil over a Catalyst Synthesized from Fly Ash." In Catalytic and Noncatalytic Upgrading of Oils. American Chemical Society, 2021. http://dx.doi.org/10.1021/bk-2021-1379.ch009.

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McGhee, B. J., J. M. Andresen, C. E. Snape, R. Hughes, C. L. Koon, and G. Hutchings. "Characterization of Fluid Catalytic Cracking Catalyst Coke by13C NMR and Mass Spectrometry." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch008.

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Murthy, V. L. N., S. Debnath, M. Rama Rao, S. K. Ray, A. K. Das, and S. Ghosh. "Development of a Test Procedure To Evaluate Fluid Catalytic Cracking Catalyst Regenerability." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch029.

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Moon, Gyeonghye, Jin-Hyung Kim, Yeon-Chul Cho, et al. "Production of High-Purity Titanium Dioxide from Spent Selective Catalytic Reduction (SCR) Catalyst." In Rare Metal Technology 2019. Springer International Publishing, 2019. http://dx.doi.org/10.1007/978-3-030-05740-4_13.

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Turlier, P., M. Forissier, P. Rivault, I. Pitault, and J. R. Bernard. "Catalyst Fouling by Coke from Vacuum Gas Oil in Fluid Catalytic Cracking Reactors." In ACS Symposium Series. American Chemical Society, 1994. http://dx.doi.org/10.1021/bk-1994-0571.ch008.

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Wojciechowski, B. W., and N. M. Rice. "Catalyst Decay as a Side Reaction of the Chain Processes of Catalytic Cracking." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch009.

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Zalioubovskaia, T., A. Gédéon, J. Fraissard, E. Radchenko, and B. Nefedov. "Effect of Support Texture on Pt Dispersion and CO-Oxidation Catalyst in Fluid Catalytic Cracking." In ACS Symposium Series. American Chemical Society, 1994. http://dx.doi.org/10.1021/bk-1994-0571.ch016.

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Lerner, Bruce, and Michel Deeba. "Improved Methods for Testing and Assessing Deactivation from Vanadium Interaction with Fluid Catalytic Cracking Catalyst." In ACS Symposium Series. American Chemical Society, 1996. http://dx.doi.org/10.1021/bk-1996-0634.ch022.

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Conference papers on the topic "Spent catalytic cracking catalyst"

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Takeda, Masashi, Tomoaki Kiso, and Keizo Hosoya. "Cracking of Metallic Bellows in Fluid Catalytic Cracking (FCC) Units." In CORROSION 2013. NACE International, 2013. https://doi.org/10.5006/c2013-02430.

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Abstract Metallic bellows have been applied to regenerated catalyst standpipes, spent catalyst standpipes and flue gas piping in fluid catalytic cracking (FCC) units mainly to absorb the axial movement of piping. Nickel-based alloys and nickel-iron-chromium alloys, such as UNS(1) N06626, alloy 625 (UNS N06625) and alloy 800H (UNS N08810), have been selected for the metallic bellows in recent FCC units. Insulation applied to metallic bellows in hot service is necessary to maintain the metal skin temperature within the desired range. Alloy 625, for instance, is not recommended for extended use a
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Nair, Jayant R., Asad Al Ghafri, Naif Al Abri, and Fahmi Al Mawali. "Accelerated Corrosion of UNS S30409 (304H SS) in RFCC Regenerators Involving High Temperature Eutectic Molten Salts." In CORROSION 2017. NACE International, 2017. https://doi.org/10.5006/c2017-08915.

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Abstract Residue Fluid Catalytic cracking (RFCC) is a valuable subset of the more conventional Fluid Catalytic cracking (FCC) process that generates most of the world’s gasoline pool. The critical distinction of RFCC involves the processing of “dirty” atmospheric residue (AR) directly from crude distillation and not just the more conventional use of relatively pure gasoil feedstocks. By direct catalytic cracking of “dirty” residue the refiner benefits economically by avoiding a whole intermediate process, namely vacuum distillation. Unfortunately direct FCC processing of atmospheric residue (A
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Roy, Shekhar, Q. M. Amir, S. P. Dubey, P. Deshmukh, and A. K. Lahiri. "Service Induced Damage Assessment of Reformer Feed Heater Tubes in Continuous Catalyst Reforming Unit (CCRU)." In CORROSION 2010. NACE International, 2010. https://doi.org/10.5006/c2010-10347.

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Abstract Substantial loss in tube wall thickness from the inside was observed in the first heater which is also called the charge heater. The tubes were 5 Cr 0.5 Mo and the thinning was primarily in the outlet end. Subsequently, six months later, pinhole leakage occurred in the same heater causing shutdown of the unit. Heater tube samples were collected from all three heaters and confirmed carburization of tubes after studies. The carburization mechanism has been experienced for the first time in Continuous Catalytic Reformer Unit (CCRU) of a petroleum refinery in India. Investigation carried
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Dean, Sheldon W. "Air Separation and Other Industrial Gas Corrosion Solutions in the Next Millennium." In CORROSION 2001. NACE International, 2001. https://doi.org/10.5006/c2001-01347.

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Abstract Air separation technology has continued to evolve from cryogenic distillation to a variety of adsorption and other types of processes. Corrosion problems are encountered in the front-end compression and cooling steps where moisture is removed from the air. Thereafter, the main materials concerns are assuring adequate strength and ductility at cryogenic temperatures and preventing fires when handling purified oxygen. Catalytic reforming and partial oxidation technology are used to form syngas from hydrocarbons. Caustic stress corrosion cracking of stainless steels has been a concern in
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Milton, Douglas, William Bresnahan, Christopher Smalley, Robert Botto, and William Zagrany. "FCCU Light Ends Plant Carbonate Stress Corrosion Cracking Experience." In CORROSION 2007. NACE International, 2007. https://doi.org/10.5006/c2007-07564.

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Abstract As a result of a Carbonate Stress Corrosion Cracking (CSCC) event at one refinery an investigation was made into the cause and mitigation of CSCC. At the specific refinery, the immediate cause was attributed to a change in catalyst type in the upstream cat cracker feed hydrotreater (CFHT) which reduced the feed sulfur/feed nitrogen (S/N) ratio in the feed, resulting in an increased carbonate concentration, and an increased likelihood of cracking. This paper outlines the information that was developed during the investigation and also outlines the development of tools that could be uti
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Aktaş, Fatih, Kiran G. Burra, Athi-enkosi Mavukwana, and Ashwani K. Gupta. "Temperature and Positioning Effects of Spent Fluid Catalytic Cracking Catalyst in the Reactor on Pyrolysis of Polyethylene Terephthalate." In ASME 2024 Power Conference. American Society of Mechanical Engineers, 2024. http://dx.doi.org/10.1115/power2024-138163.

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Abstract Results are presented on the influence of positioning of spent Fluid Catalytic Cracking (FCC) catalyst and reactor temperature in pyrolyzing of waste polyethylene terephthalate (PET). The catalyst bed was modified to be directly mixed with the feedstock bed (in-situ) for a solid-solid contact or separated but kept at the same temperature so that the catalyst encountered only the volatiles released from PET (quasi in-situ). The synthesis gas (syngas) evolved from the pyrolysis of PET was analyzed and compared. For in-situ position of the catalyst at 900 °C, the syngas yield and energy
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Niewiadomski, Paweł, Wong Seng, and Łukasz Sadowski. "RECYCLING OF SPENT FLUID CATALYTIC CRACKING CATALYST IN CEMENTITIOUS COMPOSITES." In Creative Construction e-Conference 2023. Budapest University of Technology and Economics, 2023. http://dx.doi.org/10.3311/ccc2023-019.

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Manrique, Herbert, Victor Pretell, Williams Ramos, and Carlos Ubillas. "Recovery of Cerium and Zeolite from Spent Fluidized Catalytic Cracking Catalyst." In 22nd LACCEI International Multi-Conference for Engineering, Education and Technology (LACCEI 2024): “Sustainable Engineering for a Diverse, Equitable, and Inclusive Future at the Service of Education, Research, and Industry for a Society 5.0.”. Latin American and Caribbean Consortium of Engineering Institutions, 2024. http://dx.doi.org/10.18687/laccei2024.1.1.990.

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Aktaş, Fatih, Kiran G. Burra, and Ashwani K. Gupta. "Polyethylene Terephthalate Gasification Using CO2: Impact of SFCC Catalyst Contact Mode and Amount." In ASME 2024 Power Conference. American Society of Mechanical Engineers, 2024. http://dx.doi.org/10.1115/power2024-138167.

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Abstract The influence of spent fluid catalytic cracking (sFCC) catalyst on CO2-assisted gasification of polyethylene terephthalate (PET) was investigated at 900 °C using a semi-batch fixed-bed reactor. The effects of catalyst amount and contact mode on the release of synthesis gas (syngas) and char yields were studied. sFCC catalysis increased the maximum syngas yield by about 45% and energy yield by 60% in comparison to non-catalytic gasification. High syngas energy was extracted during CO2-assisted catalytic gasification, revealing the efficacy of sFCC and CO2 in PET conversion. The efficie
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Wei, Jianming, Yanan Li, Meng Xu, Xingong Zhang, and Yuzhen Zhang. "Preliminary Study of Using Spent Fluid Catalytic Cracking (FCC) Catalyst in Asphalt Binders." In Transportation Research Congress 2016. American Society of Civil Engineers, 2018. http://dx.doi.org/10.1061/9780784481240.008.

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Reports on the topic "Spent catalytic cracking catalyst"

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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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