[1] |
TAYIBI H, CHOURA M, LÓPEZ F A, et al. Environmental impact and management of phosphogypsum[J]. Journal of Environmental Management, 2009, 90(8):2377-2386.
|
[2] |
HWAITI M A, KHASHMAN O A. Health risk assessment of heavy metals contamination in tomato and green pepper plants grown in soils amended with phosphogypsum waste materials[J]. Environmental Geochemistry & Health, 2015, 37(2):287-304.
|
[3] |
RASHAD A M. Potential use of phosphogypsum in alkali-activated fly ash under the effects of elevated temperatures and thermal shock cycles[J]. Journal of Cleaner Production, 2014, 87(1):717-725.
|
[4] |
WANG F, DREISINGER D B, JARVIS M, et al. The technology of CO2 sequestration by mineral carbonation:current status and future prospects[J]. Canadian Metallurgical Quarterly, 2017, 2017(1):1-13.
|
[5] |
LEE M G, JANG Y N, RYU K W, et al. Mineral carbonation of flue gas desulfurization gypsum for CO2 sequestration[J]. Energy, 2012, 47(1):370-377.
|
[6] |
XIAO Q, YANG N, ZHU J H, et al. Modeling of cavern formation in yield stress fluids in stirred tanks[J]. AIChE Journal, 2014, 60(8):3057-3070.
|
[7] |
Lu S Q, Lan P Q, Wu S F. Preparation of nano-CaCO3 from phosphogypsum by gas-liquid-solid reaction for CO2 sorption[J]. Industrial & Engineering Chemistry Research, 2016, 55(38):10172-10177.
|
[8] |
鲁厚芳. 杂质对石膏-碳酸铵转化过程的影响[D]. 成都:四川大学, 2002. Lu H F. Effect of impurities on gypsum conversion to ammonium sulfate with ammonium carbonate[D]. Chengdu:Sichuan University, 2002.
|
[9] |
王子宁, 周加贝, 朱家骅, 等. 二水硫酸钙溶解动力学[J]. 化工学报, 2015, 66(3):1001-1006. WANG Z N, ZHOU J B, ZHU J H, et al. Dissolution kinetics of calcium sulfate dihydrate[J]. CIESC Journal, 2015, 66(3):1001-1006.
|
[10] |
RAINES M A, DEWERS T A. Mixed transport/reaction control of gypsum dissolution kinetics in aqueous solutions and initiation of gypsum karst[J]. Chemical Geology, 1997, 140(1/2):29-48.
|
[11] |
Colombani J. Measurement of the pure dissolution rate constant of a mineral in water[J]. Geochimicaet Cosmochimica Acta, 2008, 72(23):5634-5640.
|
[12] |
Jeschke A A, Vosbeck K, Dreybrodt W. Surface controlled dissolution rates of gypsum in aqueous solutions exhibit nonlinear dissolution kinetics[J]. Geochimica et Cosmochimica Acta, 2001, 65(1):27-34.
|
[13] |
LASAGA A C. Kinetic Theory in the Earth Sciences[M]. Princeton, New Jersey:Princeton University Press, 1998:683-686.
|
[14] |
LIU S T, NANCOLLAS G H. The kinetics of dissolution of calcium sulfate dihydrate[J]. Journal of Inorganic & Nuclear Chemistry, 1971, 33(8):2311-2316.
|
[15] |
RANDOLPH A D, LARSON M A. Theory of Particulate Processes[M]. 2 ed. United States:Academic Press, 1988:11-13.
|
[16] |
PANGARKAR V G, YAWALKAR A A, SHARMA M M, et al. Particle-liquid mass transfer coefficient in two-/three-phase stirred tank reactors[J]. Industrial & Engineering Chemistry Research, 2002, 41(17):4141-4167.
|
[17] |
HARRIOTT P. Mass transfer to particles(I):Suspended in agitated tanks[J]. AIChE Journal, 1962, 8(1):93-101.
|
[18] |
SHAN G, IGARASHI K, OOSHIMA H. Dissolution kinetics of crystals in suspension and its application to L-aspartic acid crystals[J]. Chemical Engineering Journal, 2002, 88(1/2/3):53-58.
|
[19] |
LEBLANC S E, FOGLER H S. Population balance modeling of the dissolution of polydisperse solids:rate limiting regimes[J]. AIChE Journal, 1987, 33(1):54-63.
|
[20] |
王子宁. 磷石膏与二氧化碳矿化反应体系钙离子转移过程研究[D]. 成都:四川大学, 2014. WANG Z N. Research on process of Ca2+ transfer in multi-phase reaction system of CO2 mineralized by phosphogypsum[D]. Chengdu:Sichuan University, 2014.
|
[21] |
XU D, LIU Z, CAI L, et al. A CFD-PBM approach for modeling ice slurry flow in horizontal pipes[J]. Chemical Engineering Science, 2018, 176(2):546-559.
|
[22] |
关润铎, 刘涛, 张方坤, 等. 基于PBM的L-谷氨酸粒度分布控制优化[J]. 化工学报, 2017, 68(3):956-963. GUAN R D, LIU T, ZHANG F K, et al. Optimal control of L-glutamic acid crystal size distribution based on population balance model[J]. CIESC Journal, 2017, 68(3):956-963.
|
[23] |
HÄNCHEN M, KREVOR S, MAZZOTTI M, et al. Validation of a population balance model for olivine dissolution[J]. Chemical Engineering Science, 2007, 62(22):6412-6422.
|
[24] |
MANGIN D, GARCIA E, GERARD S, et al. Modeling of the dissolution of a pharmaceutical compound[J]. Journal of Crystal Growth, 2006, 286(286):121-125.
|
[25] |
ASAI S, KONISHI Y, SASAKI Y. Mass transfer between fine particles and liquids in agitated vessels[J]. Journal of Chemical Engineering of Japan, 1988, 21(2):107-112.
|
[26] |
SHINNAR R, CHURCH J M. Statistical theories of turbulence in predicting particle size in agitated dispersions[J]. Ind. Eng. Chem., 1960, 52(3):253-256.
|
[27] |
GARCIA-OCHOA F, GOMEZ E. Theoretical prediction of gas-liquid mass transfer coefficient, specific area and hold-up in sparged stirred tanks[J]. Chemical Engineering Science, 2004, 59(12):2489-2501.
|
[28] |
朱有庭, 曲文海, 于浦义. 化工设备设计手册:上册[M]. 北京:化学工业出版社, 2005:859-862. ZHU Y T, QU W H, YU P Y. Design Handbook for Chemical Equipment:Volume One[M]. Beijing:Chemical Industry Press, 2005:859-862.
|
[29] |
BRAVO R, CAMACHO R, MOYA V, et al. Desulphurization of SO2-N2 mixtures by limestone slurries[J]. Chemical Engineering Science, 2002, 57(11):2047-2058.
|
[30] |
MCGRAW R. Description of aerosol dynamics by the quadrature method of moments[J]. Aerosol Science and Technology, 1997, 27(2):255-265.
|
[31] |
HOUNSLOW M J, REYNOLDS G K. Product engineering for crystal size distribution[J]. AIChE Journal, 2006, 52(7):2507-2517.
|
[32] |
GORDON R G. Error bounds in equilibrium statistical mechanics[J]. Journal of Mathematical Physics, 1968, 9(5):655-663.
|
[33] |
NAGY Z K, AAMIR E, RIELLY C D. Internal fines removal using population balance model based control of crystal size distribution under dissolution, growth and nucleation mechanisms[J]. Crystal Growth & Design, 2011, 11(6):2205-2219.
|