[1] W. Wang, H. Han, M. Yuan, H. Li, F. Fang, K. Wang, Treatment of coal gasification wastewater by a two-continuous UASB system with step-feed for COD and phenols removal, Bioresour. Technol. 102(2011) 5454-5460. [2] Z. Wang, X. Xu, Z. Gong, F. Yang, Removal of COD, phenols and ammonium from Lurgi coal gasification wastewater using A2O-MBR system, J. Hazard. Mater. 235-236(2012) 78-84. [3] Z. Yu, Y. Chen, D. Feng, Y. Qian, Process development, simulation, and industrial implementation of a new coal-gasification wastewater treatment installation for phenol and ammonia removal, Ind. Eng. Chem. Res. 49(2010) 2874-2881. [4] W. Wang, H. Han, M. Yuan, H. Li, Enhanced anaerobic biodegradability of real coal gasification wastewater with methanol addition, J. Environ. Sci. 22(2010) 1868-1874. [5] W. Shen, Y. Ren, T. Wang, C. Hai, Stable (solid + liquid) phase equilibrium for the ternary systems (K2SO4 + KH2PO4 + H2O), (K2SO4 + KCl + H2O) at T=313.15 K, J. Chem. Thermodyn. 90(2015) 15-23. [6] C. Du, S. Zheng, H. Li, Y. Zhang, Solid-liquid equilibria of K2CO3 + K2CrO4 + H2O system, J. Chem. Eng. Data 51(2006) 104-106. [7] J. Hu, S. Sang, Q. Liu, Phase equilibria in the ternary systems KBr-MgBr2-H2O and NaBr-MgBr2-H2O at 348.15 K, Fluid Phase Equilibr. 392(2015) 127-131. [8] S. Sang, Y. Hu, R. Cui, J. Hu, Y. Wang, Measurements of solid-liquid equilibria in the ternary system NaCl-NaBr-H2O at 373 K, Russ. J. Phys. Chem. 89(2015) 1152-1157. [9] H. Schott, A mathematical extrapolation for the method of wet residues, J. Chem. Eng. Data 3(1961) 324. [10] Y. Su, B. Lu, X. Wang, Phase Diagram Analyses of Inorganic Chemical Production:Basic Theory, Chemical Industry Press, Beijing, 1985136-137. [11] Z. Niu, F. Cheng, The Phase Diagram of Salt-Water System and its Application, second ed. Tianjin University Press, Tianjin, 2002. [12] H. Stephen, T. Stephen, Solubilities of Inorganic and Organic Compounds, Pergamon Press Ltd., Oxford, 1979. |