基于表面化学性质,泡沫浮选已成为一种分离非均质固体混合物的有效手段,并被广泛应用于原矿分离及其他化学工业。在浮选过程中,捕收剂往往对矿物表面进行选择性吸附以调控矿物表面的亲疏水性。目前,大部分可溶盐的生产,尤其是钾盐工业生产,主要采用泡沫浮选的方法。尽管可溶盐实际浮选体系很复杂,但主要包含矿物晶体、捕收剂、气泡和高离子强度的饱和盐溶液四种组分。实际上,浮选能否完成是这四种组分相互作用的结果。因此,大量的可溶盐浮选机理研究工作都集中于浮选体系中各组分之间的相互作用。本文对高离子强度下可溶盐浮选机理的主要研究成果进行了综述,重点介绍了可溶盐的溶液化学性质,捕收剂在饱和盐溶液中的胶体性质,捕收剂在矿物晶体表面的选择性吸附机制和吸附行为,矿物晶体/饱和盐溶液界面性质以及气泡在浮选过程中作用机理,并对高离子强度下可溶盐浮选机理研究的发展趋势进行了展望。
[1] Marcus Y. Biophys. Chem., 1994, 51:111.
[2] Chalikian T V. J. Phys. Chem. B, 2001, 105:12566.
[3] Du H, Rasaiah J C, Miller J D. J. Phys. Chem. B, 2007, 111:209.
[4] Max J J, Chapados C. J. Chem. Phys., 2001, 115:2664.
[5] Dillon S R, Dougherty R C. J.Phys. Chem. A, 2002, 106:7647.
[6] Dang L X. J. Am. Chem. Soc., 1995, 117:6954.
[7] Hancer M, Celik M S, Miller J D. J. Colloid Interface Sci., 2001, 235:150.
[8] Koneshan S, Rasaiah J C, Lynden-Bell R M, Lee S H. J. Phys. Chem. B, 1998, 102:4193.
[9] Licheri G, Piccaluga G, Pinna G. Chem. Phys. Lett., 1975, 35:119.
[10] Lawrence R M, Kruh R F. J. Chem. Phys., 1967, 47:4758.
[11] Yamagami M, Wakita H, Yamaguchi T. J. Chem. Phys., 1995, 103:8174.
[12] Du H, Ozdemir O, Wang X, Cheng F, Celik M S, Miller J D. Miner. Metall. Proc., 2014, 31:1.
[13] Nickolov Z S, Miller J D. J. Colloid Interface Sci., 2005, 287:572.
[14] Cheng F, Cao Q, Guan Y, Cheng H, Wang X, Miller J D. Int. J. Miner. Process., 2013, 122:36.
[15] Hancer M. Doctoral Dissertation of The University of Utah, 2000.
[16] Desnoyers J E, Perron G. J. Solution Chem., 1972, 1:199.
[17] Ozdemir O, Celik M S, Nickolov Z S, Miller J D. J. Colloid Interf. Sci., 2007, 314:545.
[18] Marcus Y. Chem. Rev., 2009, 109:1346.
[19] Broome F K, Hoerr C W, Harwood H J. J. Am. Chem. Soc., 1951, 73:3350.
[20] Eggenberger D N, Harwood H J. J. Am. Chem. Soc., 1951, 73:3353.
[21] Brandrup J, Immergut E H. Polymer Handbook. 2nd ed. Wiley, 1975.
[22] Dai Q, Laskowski J S. Langmuir, 1991, 7:1361.
[23] Laskowski J S, Pawlik M, Ansari A. Can. Metall. Quart., 2007, 46:295.
[24] Cao Q, Du H, Miller J D, Wang X, Cheng F. Miner. Eng., 2010, 23:365.
[25] 段平梅(Duan P M), 杜志平(Du Z P), 李达(Li D), 李恩泽(Li E Z), 程芳琴(Cheng F Q). 精细化工(Fine Chemicals), 2015, 32:1.
[26] Roman R J, Fuerstenau M C, Seidel D C. Transactions of the American Institute of Mining, Metallurgical, and Petroleum Engineers, 1968, 1:56.
[27] Burdukova E, Laskowski J. Can. J. Chem. Eng., 2009, 87:441.
[28] Gaudin A. Flotation.2nd ed. NY:McGraw-Hill, 1957.
[29] Fuerstenau D W, Fuerstenau M C. Transactions of the American Institute of Mining, Metallurgical and Petroleum Engineers, 1956, 205:302.
[30] Rogers J, Schulman J H. Electrical Phenomena and Solid/Liquid Interface, Proceedings of the Second International Congress of Surface Activity Ⅲ, 1957. 243.
[31] Rogers J. Institution of Mining and Metallurgy Bulletin, 1957, 607:439.
[32] Bichowsky F R, Rossini F D. Thermochemistry of the substances. New York:Reinhold, 1936.
[33] Miller J D, Yalamanchili M R, Kellar J J. Langmuir, 1992, 8:1464.
[34] Hancer M, Miller J D. Miner. Eng., 2000, 13:1483.
[35] Ozdemir O, Du H, Karakashev S I, Nguyen A V, Celik M S, Miller J D. Adv. Colloid Interf. Sci., 2011, 163:1.
[36] Du H, Miller J D. J.Phys. Chem. C, 2007, 111:10013
[37] Li E, Du Z, Yuan S, Cheng F. Miner. Eng., 2015, 83:53.
[38] Ozdemir O, Karaguzel C, Nguyen A V, Celik M S, Miller J D. Miner. Eng., 2009, 22:168.
[39] Veeramasuneni S, Hu Y, Miller J D. Surf. Sci., 1997, 382:127.
[40] Yalamanchili M R, Kellar J J, Miller J D. Int. J. Miner. Process., 1993, 39:137.
[41] Schubert H. Eng. Min. J., 1967, 168:94.
[42] Schubert H. Aufbereitungs Technik, 1988, 29:427.
[43] Miller J, Veeramasuneni S, Yalamanchili M. Int. J. Miner. Process., 1997, 51:111.
[44] Smolders C A. Recueil, 1961, 80:650.
[45] Leja J, Schulman J H. Trans. AIME, 1954, 199:221.
[46] Gaines G L. Insoluble Monolayers at Liquid-Gas Interfaces. New York:Interscience, 1966.
[47] Gaines G L. Nature, 1982, 298:544.
[48] Laskowski J S. Miner. Eng., 2013, 45:170.
[49] Laskowski J S, Cho Y S, Ding K. Can. J. Chem. Eng., 2003, 81:63.