[1] H. Gai, Y. Jiang, Y. Qian, A. Kraslawski, Conceptual design and retrofitting of the coalgasification wastewater treatment process, Chem. Eng. J. 138(2008) 84-94. [2] G. Yang, L.I. Bai chun, J.D. Liu, L.I.C. L, Simulation calculation of sour water, Acta. Petrolei Sinica. (2002) 18. [3] E. Díez, P. Langston, G. Ovejero, M.D. Romero, Economic feasibility of heat pumps in distillation to reduce energy use, Appl. Therm. Eng. 29(2009) 1216-1223. [4] H.K. Engelien, S. Skogestad, Multi-effect distillation applied to an industrial case study, Chem. Eng. Process. Process Intensif. 44(2005) 819-826. [5] X. Gao, Z. Ma, L. Yang, J. Ma, Simulation and optimization of distillation processes for separating the methanol-chlorobenzene mixture with separate heat-pump distillation, Ind. Eng. Chem. Res. 52(2013) 11695-11701. [6] A. Ming, J. He, Q. Zhang, Discussion on sour water stripping process, Guangdong, Chem. Ind. 42(2015) 154-155. [7] H. Gai, H. Song, M. Xiao, Y. Feng, Y. Wu, H. Zhou, B. Chen, Conceptual design of a modified phenol and ammonia recovery process for the treatment of coal gasification wastewater, Chem. Eng. J. 304(2016) 621-628. [8] W. Hou, H. SU, Y. Hu, J. Chu, Modeling, simulation and optimization of a whole industrial catalytic naphtha reforming process on Aspen plus platform, Chin. J. Chem. Eng. 14(2006) 584-591. [9] A. Kazemi, M. Hosseini, A. Mehrabani-Zeinabad, V. Faizi, Evaluation of different vapor recompression distillation configurations based on energy requirements and associated costs, Appl. Therm. Eng. 94(2016) 305-313. [10] S. Xu, L. Yanli, Z. Lisong, Performance research of self regenerated absorption heat transformer cycle using TFE-NMP as working fluids, Inter. J. Refr. 24(6) (2001) 510-518. [11] S.E. Ogbeide, S.A.K. El-Meniawy, S. Devotta, F.A. Watson, F.A. Holland, An experimental evaluation of R11 as a heat pump working fluid in comparison with some other working fluids, Inter. J. Energy. Res. 7(2) (1983) 129-135. [12] C.C. Chen, H.I. Britt, J.F. Boston, L.B. Evans, Local composition model for excess Gibbs energy of electrolyte systems, AIChE J 28(1982) 588-596. [13] D. Feng, Z. Yu, Y. Chen, Y. Qian, Novel single stripper with side-draw to remove ammonia and sour gas simultaneously for coal-gasification wastewater treatment and the industrial implementation, Ind. Eng. Chem. Res. 48(2009) 5816-5823. [14] 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. [15] G.C. Hoogendoorn, R. Abellon, P.J.M. Essens, J.A. Wesselingh, Desorption of volatile electrolytes in a tray column (sour water stripping), Chem. Eng. Res. Des. 66(1988) 483-502. [16] H. Luo, C.S. Bildea, A.A. Kiss, Novel heat-pump-assisted extractive distillation for bioethanol purification, Ind. Eng. Chem. Res. 54(2015) 2208-2213. [17] D. Feng, H. Lu, Z. Yu, Removal of sour gas and ammonia from single pressurized stripper for coal-gasification wastewater treatment, Chem. Eng. 38(2010) 93-97. [18] M. Garbs, Pinch analysis and process integration:a user guide on process integration for the efficient use of energy, J. Clean. Prod. 110(2016) 203. [19] M. Bartholomew-Biggs, Optimization with Restrictions, Springer, Switzerland, 2008. [20] A.A. Kiss, R.M. Ignat, Optimal economic design of an extractive distillation process for bioethanol dehydration, Energy. Technol. 1(2013) 166-170. |