[1] BI X, LIU X. High density and high solids flux CFB risers for steam gasification of solids fuels[J]. Fuel Processing Technology, 2010, 91(8): 915-920 [2] GRACE J R, ISSANGYA A S, BAI D, et al. Situating the high-density circulating fluidized bed[J]. AIChE Journal, 1999, 45(10): 2108-2116 [3] KIM S W, KIRBAS G, BI H, et al. Flow behavior and regime transition in a high-density circulating fluidized bed riser[J]. Chemical Engineering Science, 2004, 59(18): 3955-3963 [4] YAN Z, FAN Y, BI X, et al. Dynamic behaviors of feed jets and catalyst particles in FCC feed injection zone[J]. Chemical Engineering Science, 2018, 189: 380-393 [5] XIE D, BOWEN B D, GRACE J R, et al. Two-dimensional model of heat transfer in circulating fluidized beds. Part II: Heat transfer in a high density CFB and sensitivity analysis[J]. International Journal of Heat and Mass Transfer, 2003, 46(12): 2193-2205 [6] PÄRSSINEN J H, ZHU J. Axial and radial solids distribution in a long and high-flux CFB riser[J]. AIChE Journal, 2001, 47(10): 2197-2205 [7] YAN A, ZHU J. Scale-up effect of riser reactors: Particle velocity and flow development[J]. AIChE Journal, 2005, 51(11): 2956-2964 [8] SUN Z, ZHU J, ZHANG C. Numerical study on the hydrodynamics in high-density gas-solid circulating fluidized bed downer reactors[J]. Powder Technology, 2020, 370: 184-196 [9] WANG C, WANG G, LI C, et al. Catalytic ozone decomposition in a high density circulating fluidized bed riser[J]. Industrial & Engineering Chemistry Research, 2014, 53(16): 6613-6623 [10] WEI F, LU F, JIN Y, et al. Mass flux profiles in a high density circulating fluidized bed[J]. Powder Technology, 1997, 91(3): 189-195 [11] WEI F, WAN X, HU Y, et al. A pilot plant study and 2-D dispersion-reactor model for a high-density riser reactor[J]. Chemical Engineering Science, 2001, 56(2): 613-620 [12] LI Z Q, WU C, WEI F, et al. Experimental study of high-density gas-solids flow in a new coupled circulating fluidized bed[J]. Powder Technology, 2004, 139(3): 214-220 [13] SU X, WANG C, LAN X, et al. Axial flow structure of solids holdup in an 18 m high-density CFB riser based on pressure measurements[J]. Particuology, 2021, 54: 116-125 [14] SU X, WANG C, PEI H, et al. Experimental study of solids motion in an 18 m gas-solids circulating fluidized bed with high solids flux[J]. Industrial & Engineering Chemistry Research, 2019, 58(51): 23468-23480 [15] CHEN J. Experiments that address phenomenological issues of fast fluidization[J]. Chemical Engineering Science, 1999, 54(22): 5529-5539 [16] SEO M W, SUH Y H, KIM S D, et al. Cluster and bed-to-wall heat transfer characteristics in a dual circulating fluidized bed[J]. Industrial & Engineering Chemistry Research, 2012, 51(4): 2048-2061 [17] MCMILLAN J, SHAFFER F, GOPALAN B, et al. Particle cluster dynamics during fluidization[J]. Chemical Engineering Science, 2013, 100: 39-51 [18] GÓMEZ N, MOLINA A, MARIN G B, et al. From 3D to 1D: Capturing the effect of particle clusters in Downers in the fluid catalytic cracking of gasoil[J]. Chemical Engineering Research and Design, 2021, 170: 366-379 [19] CARLOS VARAS Á E, PETERS E A J F, KUIPERS J A M. Computational fluid dynamics-discrete element method (CFD-DEM) study of mass-transfer mechanisms in riser flow[J]. Industrial & Engineering Chemistry Research, 2017, 56(19): 5558-5572 [20] WANG C, LI C, LAN X, et al. Particle clustering (mesoscale structure) of high-flux gas-solid circulating fluidized bed[J]. Particuology, 2020, 48: 144-159 [21] MANYELE S V, PÄRSSINEN J H, ZHU J. Characterizing particle aggregates in a high-density and high-flux CFB riser[J]. Chemical Engineering Journal, 2002, 88(1/2/3): 151-161 [22] WEI X, ZHU J. A comprehensive characterization of aggregative flow in a circulating fluidized bed (1): High-density riser[J]. Industrial & Engineering Chemistry Research, 2020, 59(22): 10315-10327 [23] YIN S, ZHONG W, SONG T, et al. Clusters identification and meso-scale structures in a circulating fluidized bed based on image processing[J]. Advanced Powder Technology, 2019, 30(12): 3010-3020 [24] 曾鑫, 阳绍军, 王圣典, 等. 密相输运床的团聚物频率和持续时间[J]. 化工学报, 2013, 64(5):1614-1620 ZENG Xin, YANG Shaojun, WANG Shengdian, et al. Cluster frequency and existence time in dense transport bed[J]. CIESC Journal, 2013, 64(5): 1614-1620(in Chinese) [25] WU G, YANG X, HE Y. Experimental exploration of particle cluster characteristics in the gas-solid diameter-varying fluidized bed[J]. Powder Technology, 2023, 429: 118948 [26] ZHANG H, JOHNSTON P M, ZHU J, et al. A novel calibration procedure for a fiber optic solids concentration probe[J]. Powder Technology, 1998, 100(2/3): 260-272 [27] DENG B, ZHANG Y, ZHANG M, et al. Identification and dynamic properties of clusters for Geldart group B particles in a circulating fluidized bed[J]. Chemical Engineering Science, 2022, 248: 117265 [28] SHARMA A K, TUZLA K, MATSEN J, et al. Parametric effects of particle size and gas velocity on cluster characteristics in fast fluidized beds[J]. Powder Technology, 2000, 111(1/2): 114-122 [29] LIU Y, DAI Q, QI H. Cluster identification criterion with experimental validation for the cluster solid holdup model during fluidization[J]. Powder Technology, 2020, 373: 459-467 [30] WANG C, LUO M, SU X, et al. A sliding-window based signal processing method for characterizing particle clusters in gas-solids high-density CFB reactor[J]. Chemical Engineering Journal, 2023, 452: 139141 [31] XU J, ZHU J. A new method for the determination of cluster velocity and size in a circulating fluidized bed[J]. Industrial & Engineering Chemistry Research, 2012, 51(4): 2143-2151
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