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Zuo C, Su Q. Research Progress on Propylene Preparation by Propane Dehydrogenation. Molecules 2023; 28:molecules28083594. [PMID: 37110826 PMCID: PMC10142202 DOI: 10.3390/molecules28083594] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 04/07/2023] [Revised: 04/18/2023] [Accepted: 04/19/2023] [Indexed: 04/29/2023] Open
Abstract
At present, the production of propylene falls short of the demand, and, as the global economy grows, the demand for propylene is anticipated to increase even further. As such, there is an urgent requirement to identify a novel method for producing propylene that is both practical and reliable. The primary approaches for preparing propylene are anaerobic and oxidative dehydrogenation, both of which present issues that are challenging to overcome. In contrast, chemical looping oxidative dehydrogenation circumvents the limitations of the aforementioned methods, and the performance of the oxygen carrier cycle in this method is superior and meets the criteria for industrialization. Consequently, there is considerable potential for the development of propylene production by means of chemical looping oxidative dehydrogenation. This paper provides a review of the catalysts and oxygen carriers employed in anaerobic dehydrogenation, oxidative dehydrogenation, and chemical looping oxidative dehydrogenation. Additionally, it outlines current directions and future opportunities for the advancement of oxygen carriers.
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Affiliation(s)
- Cheng Zuo
- College of Chemistry & Chemical and Environmental Engineering, Weifang University, Weifang 261000, China
| | - Qian Su
- College of Chemistry & Chemical and Environmental Engineering, Weifang University, Weifang 261000, China
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The CREC Fluidized Riser Simulator a Unique Tool for Catalytic Process Development. Catalysts 2022. [DOI: 10.3390/catal12080888] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022] Open
Abstract
The CREC Riser Simulator is a mini-fluidized bench scale unit invented and implemented in 1992, at the CREC (Chemical Reactor Engineering Centre), University of Western Ontario The CREC Riser Simulator can be operated at short reaction times, in the 3 s to 20 s range. The present review describes and evaluates the original basic concept of the 1992-CREC Riser Simulator Unit, and the improved design of the 2019-CREC Riser Simulator. Both the initial and the enhanced units are specially engineered to allow the rigorous assessment of both catalyst performance and catalytic reaction kinetics. Kinetic parameters of relatively simple and accurate mathematical models can be calculated using experimental data from the CREC Riser Simulator. Since its inception in 1992, the CREC Riser Simulator has been licensed to and manufactured for a significant number of universities and companies around the world. Several examples of scenarios where the CREC Riser Simulator can be employed to develop fluidized bed catalytic and heterogeneous reactor simulations are reported in this review. Among others, they include (a) hydrocarbon catalytic cracking, (b) the catalytic conversion of tar derived biomass chemical species, (c) steam and dry catalytic methane reforming, (d) the catalytic oxydehydrogenation of light paraffins, (e) the catalytic desulfurization of gasoline, and (f) biomass derived syngas combustion via chemical looping. In this review, special emphasis is given to the application of the CREC Riser Simulator to TIPB (tri-iso-propyl-benzene) catalytic cracking and the light paraffins catalytic oxydehydrogenation (PODH).
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Ullah Z, Khan M, Khan I, Jamil A, Sikandar U, Mehran MT, Mubashir M, Tham PE, Khoo KS, Show PL. Recent Progress in Oxidative Dehydrogenation of Alkane (C2–C4) to Alkenes in a Fluidized Bed Reactor Under Mixed Metallic Oxide Catalyst. J Inorg Organomet Polym Mater 2022. [DOI: 10.1007/s10904-022-02433-7] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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Liu B, Yan L, Zhao H, Yang J, Zhao J, Song H, Chou L. Role of cerium dopants in MoVNbO multi-metal oxide catalysts for selective oxidation of ethane. J RARE EARTH 2022. [DOI: 10.1016/j.jre.2021.04.016] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
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Amusa HK, Adamu S, Arjah AS, Al-Bogami SA, Al-Ghamdi S, Razzak SA, Hossain MM. Kinetics of Oxidative Cracking of n-Hexane to Light Olefins using Lattice Oxygen of a VO x /SrO-γAl 2 O 3 Catalyst. Chem Asian J 2021; 16:1792-1806. [PMID: 34107160 DOI: 10.1002/asia.202100209] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/01/2021] [Revised: 04/15/2021] [Indexed: 11/06/2022]
Abstract
The kinetics of oxidative cracking of n-hexane to light olefins using the lattice oxygen of VOx /SrO-γAl2 O3 catalysts has been investigated. Kinetic experiments were conducted in a CREC Riser Simulator (CERC: Chemical Reactor Engineering Center), which mimics fluidized bed reactors. The catalyst's performance is partly attributed to the moderate interaction between active VOx species and the SrO-γAl2 O3 support. This moderate interaction serves to control the release of lattice oxygen to curtail deep oxidation. The incorporation of basic SrO component in the support also helped to moderate the catalyst's acidity to checkmate excessive cracking. Langmuir-Hinshelwood model was applied to formulate the rate equations. The intrinsic kinetic parameters were obtained by fitting the experimental data to the kinetic model using a nonlinear regression algorithm at a 95% confidence interval, implemented in MATLAB. n-Hexane transforms to olefins at a specific reaction rate of 1.33 mol/gcat.s and activation energy of 119.2 kJ/mol. These values when compared with other duplets (i. e., ki° and EA ) for paraffins to olefins, show that indeed olefins are stable products of the oxidative conversion of n-hexane over VOx /SrO-γAl2 O3 under a fluidized bed condition. Values of activation energy for all COx formation routes indicate that intermediate paraffins are likely to be cracked to form CH4 than to be converted directly to COx . On the other hand, olefins may transform partly, and directly to COx (E9 =9.65 kJ/mol) than to form CH4 (E8 =89.1 kJ/mol) in the presence of excess lattice oxygen. Overall, olefins appear to be stable to deep oxidation due to the role of SrO in controlling the amount of lattice oxygen of the catalyst at the reaction temperature.
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Affiliation(s)
- Hussein K Amusa
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia
| | - Sagir Adamu
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia
| | - Abeer S Arjah
- Research & Development Center, Saudi Aramco Oil Company, Dhahran, Saudi Arabia
| | - Saad A Al-Bogami
- Research & Development Center, Saudi Aramco Oil Company, Dhahran, Saudi Arabia
| | - Sameer Al-Ghamdi
- Research & Development Center, Saudi Aramco Oil Company, Dhahran, Saudi Arabia
| | - Shaikh A Razzak
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia
| | - Mohammad M Hossain
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia.,Interdisciplinary Research Center for, Refining & Advanced Chemicals (IRC-RAC), King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia.,Interdisciplinary Research Center for, Hydrogen and Energy Storage (IRC-HES), King Fahd University of Petroleum & Minerals, Dhahran, 31261, Saudi Arabia
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Promotional effects of CO2 on the oxidative dehydrogenation of propane over mesoporous VOX/γAl2O3 catalysts. J IND ENG CHEM 2021. [DOI: 10.1016/j.jiec.2020.12.022] [Citation(s) in RCA: 11] [Impact Index Per Article: 3.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/02/2023]
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Najari S, Saeidi S, Concepcion P, Dionysiou DD, Bhargava SK, Lee AF, Wilson K. Oxidative dehydrogenation of ethane: catalytic and mechanistic aspects and future trends. Chem Soc Rev 2021; 50:4564-4605. [DOI: 10.1039/d0cs01518k] [Citation(s) in RCA: 47] [Impact Index Per Article: 15.7] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/21/2022]
Abstract
Ethane oxidative dehydrogenation (ODH) is an attractive, low energy, alternative route to reduce the carbon footprint for ethene production, however, the commercial implementation of ODH processes requires catalysts with improved selectivity.
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Affiliation(s)
- Sara Najari
- Department of Energy Engineering
- Budapest University of Technology and Economics
- Budapest
- Hungary
| | - Samrand Saeidi
- Institute of Energy and Process Systems Engineering
- Technische Universität Braunschweig
- 38106 Braunschweig
- Germany
| | - Patricia Concepcion
- Instituto de Tecnología Química
- Universitat Politècnica de València-Consejo Superior de Investigaciones Científicas (UPV-CSIC)
- Valencia
- Spain
| | - Dionysios D. Dionysiou
- Environmental Engineering and Science Program
- Department of Chemical and Environmental Engineering
- University of Cincinnati
- Cincinnati
- USA
| | - Suresh K. Bhargava
- Centre for Applied Materials and Industrial Chemistry (CAMIC)
- School of Science
- RMIT University
- Melbourne
- Australia
| | - Adam F. Lee
- Centre for Applied Materials and Industrial Chemistry (CAMIC)
- School of Science
- RMIT University
- Melbourne
- Australia
| | - Karen Wilson
- Centre for Applied Materials and Industrial Chemistry (CAMIC)
- School of Science
- RMIT University
- Melbourne
- Australia
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Balogun ML, Adamu S, Bakare IA, Ba-Shammakh MS, Hossain MM. CO2 Assisted Oxidative Dehydrogenation of Propane to Propylene over Fluidizable MoO3/La2O3-γAl2O3 Catalysts. J CO2 UTIL 2020. [DOI: 10.1016/j.jcou.2020.101329] [Citation(s) in RCA: 8] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/23/2022]
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Hurtado Cotillo M, Unsihuay D, Santolalla-Vargas C, Paredes Doig A, Sun Kou R, Picasso G. Catalysts based on Ni-Fe oxides supported on γ-Al2O3 for the oxidative dehydrogenation of ethane. Catal Today 2020. [DOI: 10.1016/j.cattod.2019.05.044] [Citation(s) in RCA: 12] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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10
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Lucky RA, Adamu S, Khan MY, Razzak SA, Hossain MM. Kinetics of Oxidative Dehydrogenation of n-Butane to C4-Olefins over a VOx/CeO2–γAl2O3 Catalyst in Gas-Phase Oxygen-Free Conditions. Ind Eng Chem Res 2020. [DOI: 10.1021/acs.iecr.0c03850] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Rahima A. Lucky
- Department of Chemical and Biochemical Engineering, The University of Western Ontario, London, Ontario N6A 3K7, Canada
| | - Sagir Adamu
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
| | - Muhammad Y. Khan
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
| | - Shaikh A. Razzak
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
| | - Mohammad M. Hossain
- Department of Chemical Engineering, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
- Center of Research Excellence in Nanotechnology, King Fahd University of Petroleum & Minerals, Dhahran 31261, Saudi Arabia
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Amusa HK, Adamu S, Bakare IA, Arjah AS, Al-Bogami SA, Al-Ghamdi S, Razzak SA, Hossain MM. High-performance VOx on SrO-γAl2O3 catalyst for oxidative cracking of n-hexane to light olefins under anaerobic environment. J IND ENG CHEM 2020. [DOI: 10.1016/j.jiec.2020.06.001] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/24/2022]
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Propane Oxidative Dehydrogenation on Vanadium-Based Catalysts under Oxygen-Free Atmospheres. Catalysts 2020. [DOI: 10.3390/catal10040418] [Citation(s) in RCA: 13] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/26/2023] Open
Abstract
Catalytic propane oxidative dehydrogenation (PODH) in the absence of gas phase oxygen is a promising approach for propylene manufacturing. PODH can overcome the issues of over-oxidation, which lower propylene selectivity. PODH has a reduced environmental footprint when compared with conventional oxidative dehydrogenation, which uses molecular oxygen and/or carbon dioxide. This review discusses both the stoichiometry and the thermodynamics of PODH under both oxygen-rich and oxygen-free atmospheres. This article provides a critical review of the promising PODH approach, while also considering vanadium-based catalysts, with lattice oxygen being the only oxygen source. Furthermore, this critical review focuses on the advances that were made in the 2010–2018 period, while considering vanadium-based catalysts, their reaction mechanisms and performances and their postulated kinetics. The resulting kinetic parameters at selected PODH conditions are also addressed.
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Kharlamova TS, Urazov KK, Vodyankina OV. Effect of Modification of Supported V2O5/SiO2 Catalysts by Lanthanum on the State and Structural Peculiarities of Vanadium. KINETICS AND CATALYSIS 2019. [DOI: 10.1134/s0023158419040050] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
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Bakare IA, Adamu S, Qamaruddin M, Al-Bogami SA, Al-Ghamdi S, Hossain MM. Oxidative Dehydrogenation of Propane to Propylene over VOx on Mixed θ-Al2O3/Alkaline Earth Metal Oxide Supports. Ind Eng Chem Res 2019. [DOI: 10.1021/acs.iecr.9b01144] [Citation(s) in RCA: 10] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
Affiliation(s)
| | | | | | - Saad A. Al-Bogami
- Research & Development Center, Saudi Aramco Oil Company, Dhahran 31261, Saudi Arabia
| | - Sameer Al-Ghamdi
- Research & Development Center, Saudi Aramco Oil Company, Dhahran 31261, Saudi Arabia
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Lopez-Zamora S, Alkhlel A, de Lasa H. Monitoring the progress of catalytic cracking for model compounds in the mid-infrared (MIR) 3200–2800 cm−1 range. Chem Eng Sci 2018. [DOI: 10.1016/j.ces.2018.08.021] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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