[1] Huang W. Progress in the field of purifying wet-process phosphoric acid by solvent precipitation[J]. Chemical Industry & Engineering Progress, 1997, 6(9):39-43
[2] Huang T H. Making strong phosphoric acid by a modified wet-process using solvent extraction[J]. Industrial & Engineering Chemistry, 1961, 53(1):31-32
[3] Monser L, Amor M B, Ksibi M. Purification of wet phosphoric acid using modified activated carbon[J]. Chemical Engineering & Processing, 1999, 38(3):267-271
[4] Touaibia D, Kerdjoudj H, Cherif A T. Concentration and purification of wet industrial phosphoric acid by electrodialysis[J]. Journal of Applied Electrochemistry, 1996, 26(10):1071-1073
[5] Polenske D, Lorenz H. Solubility and metastable zone width of the methionine enantiomers and their mixtures in water[J]. Journal of Chemical & Engineering Data, 2009, 54(8):2277-2280
[6] Ma Y, Zhou W, Zhou J. Effects of impurity ions on the metastable zone width of phosphoric acid in tributyl phosphate[J]. Journal of Chemical & Engineering Data, 2014, 59(9):2909-2913
[7] Dang L, Wang Z, Liu P. Measurement of the metastable zone width of phosphoric acid hemihydrate in the presence of impurity ions[J]. Journal of Chemical Engineering Data, 2007, 52(5):1545-1547
[8] Jin Y, An L, Chen X, et al. Experimental determination of metastable zone width, induction period, and primary nucleation kinetics of cytidine 5'-monophosphate disodium salt in an ethanol-aqueous mixture[J]. Journal of Chemical & Engineering Data, 2013, 58(5):1244-1248
[9] Zhang D, Wang Y, Ma S, et al. Determination of solubility and induction time of ceftazidime[J]. Journal of Chemical & Engineering Data, 2013, 58(1):176-182
[10] Peng J, Dong N, Dong Y, et al. Solubility, metastable zone width, and nucleation kinetics of boric acid in the Na-KCl-CaCl2-H2O system[J]. Journal of Chemical & Engineering Data, 2015, 60(11):3341-3346
[11] Rajesh N P, Kannan V, Raghavan P S, et al. Nucleation studies and crystal growth of (NH4)H2PO4, doped with thiourea in supersaturated aqueous solutions[J]. Materials Chemistry & Physics, 2002, 76(2):181-186
[12] Bromberg L, Rashba-Step J, Scott T. Insulin particle formation in supersaturated aqueous solutions of poly(ethylene glycol)[J]. Biophysical Journal, 2005, 89(5):3424-3433
[13] Zheng X, Fu J, Lu X. Solubility and induction period study of asiaticoside and madecassoside in a methanol+water mixture[J]. Journal of Chemical & Engineering Data, 2012, 57(11):3258-3263
[14] Wang J, Zhang X, Liu Y, et al. Interfacial tensions of imidazolium-based ionic liquids with N-alkanes and cyclohexane[J]. Journal of Chemical & Engineering Data, 2011, 56(10):3734-3737
[15] 林晶, 党亚固, 费德君, 等. 磷酸二氢铵结晶介稳区的研究[J]. 无机盐工业, 2007, 39(10):21-23 Lin Jing, Dang Yagu, Fei Dejun, et al. Metastable zone study of ammonium dihydrogen phosphate[J]. Inorganic Chemicals Industry, 2007, 39(10):21-23(in Chinese)
[16] Nielsen A E, Sarig S. Homogeneous nucleation of droplets and interfacial tension in the liquid system methanol water-tribromomethane[J]. Journal of Crystal Growth, 1971, 8(1):1-7
[17] Sangwal K, Mielniczek-Brzóska E. Effect of impurities on metastable zone width for the growth of ammonium oxalate monohydrate crystals from aqueous solutions[J]. Journal of Crystal Growth, 2004, 267(3/4):662-675
[18] Rauls M, Bartosch K, Kind M, et al. The influence of impurities on crystallization kinetics:A Case study on ammonium sulfate[J]. Journal of Crystal Growth, 2000, 213(1/2):116-128
[19] Sangwal K. Effect of impurities on the metastable zone width of solute-solvent systems[J]. Journal of Crystal Growth, 2009, 311(16):4050-4061
[20] Buchfink R, Schmidt C, Ulrich J. Fe3+ as an example of the effect of trivalent additives on the crystallization of inorganic compounds, here ammonium sulfate[J]. Cryst Eng Comm, 2011, 13(4):1118-1122
[21] Kulkarni S A, Kadam S S, Meekes H, et al. Crystal nucleation kinetics from induction times and metastable zone widths[J]. Crystal Growth & Design, 2013, 13(6):40-49
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