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Chauhan V, Chavan PD, Singh RK, Saha S, Datta S, Dhaigude ND, Sahu G, Saw SK. Estimating the requirements of pressure drop during fluidization-bubbling regimes in fluidized bed with different conical distributors. PARTICULATE SCIENCE AND TECHNOLOGY 2023. [DOI: 10.1080/02726351.2023.2168223] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 01/24/2023]
Affiliation(s)
- Vishal Chauhan
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Prakash D. Chavan
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Rupesh K. Singh
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Sujan Saha
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Sudipta Datta
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Nilesh D. Dhaigude
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Gajanan Sahu
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
| | - Shiva K. Saw
- Gasification and Catalysis Research Group, CSIR-Central Institute of Mining and Fuel Research (Digwadih Campus), Dhanbad, India
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State-of-the-Art Review of Fluid Catalytic Cracking (FCC) Catalyst Regeneration Intensification Technologies. ENERGIES 2022. [DOI: 10.3390/en15062061] [Citation(s) in RCA: 2] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 01/10/2023]
Abstract
Fluid catalytic cracking (FCC) is the workhorse of modern crude oil refinery. Its regenerator plays a critical role in optimizing the overall profitability by efficiently restoring the catalyst activity and enhancing the heat balance in the riser reactor. Improvement in the device metallurgy and process operations have enabled industrial regenerators to operate at high temperatures with a better coke burning rate and longer operating cycle. Today, the carbon content of regenerated catalyst has drastically reduced to less than 0.1 wt.%. However, the unit is still plagued with operational complexities and insufficient understanding of the underlying dynamic, multiscale intricacies. Recent process-intensification strategies provide insights into regenerator performance improvement potentials. In this review, the importance of the uniform distribution of spent catalysts through structural modification and operational manipulations of the catalyst distributor is discussed. The knowledge of the role of baffles in enhancing excellent gas–solid interaction has been increasing, but skepticism due to its complex hydrodynamic effects on gas–solid flows fends off operators from its application, a critical evaluation of its implication in the regenerators is covered. The understanding of the contribution of air/steam distributor design and feed gas injection techniques for even contact with spent catalyst leading to the improvement in FCC performance is also investigated. The reliability of FCC components is equally a big concern, as unplanned shutdown and enormous economic losses are being witnessed due to device failure. To this end, mitigation approaches to damaging afterburn and high-temperature erosion problems with respect to process control and geometric adjustment in the bed, freeboard, cyclone separators and collection ducts are explored. Emission limits for fluid catalytic cracking unit (FCCU) and products are consistently ratcheting downward; the commingled turnkey solutions to reducing pollutants generation are also reviewed.
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Oloruntoba A, Zhang Y, Xiao H. Study on effect of gas distributor in fluidized bed reactors by hydrodynamics-reaction-coupled simulations. Chem Eng Res Des 2022. [DOI: 10.1016/j.cherd.2021.10.031] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/01/2022]
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Xing X, Zhang C, Jiang B, Sun Y, Zhang L, Briens C. Numerical study of the effect of the inlet gas distributor on the bubble distribution in a bubbling fluidized bed. Chem Eng Res Des 2022. [DOI: 10.1016/j.cherd.2021.10.021] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 12/20/2022]
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Sano K, Koshiba Y, Ohtani H. Emergency shutdown of fluidized bed reaction systems. J Loss Prev Process Ind 2020. [DOI: 10.1016/j.jlp.2020.104277] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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Lv B, Luo Z, Deng X, Chen J, Fang C, Zhu X. Hydrodynamics and subsequent separation of gas-solid separation fluidized bed with secondary air injection. POWDER TECHNOL 2020. [DOI: 10.1016/j.powtec.2020.02.070] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/24/2022]
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Liu R, Zhou Z, Xiao R, Yu A. CFD-DEM modelling of mixing of granular materials in multiple jets fluidized beds. POWDER TECHNOL 2020. [DOI: 10.1016/j.powtec.2019.08.002] [Citation(s) in RCA: 14] [Impact Index Per Article: 3.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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