Godorr S, Hildebrandt D,Glasser D. The attainable region for system mixing and multiple rate processes: finding optimal reactor structures[J]. Chem. Eng. J., 1994, 54(3): 175-186
[2]
Hopley F D, Glasser D, Hildebrandt D. Optimal reactor structures for exothermic reversible reactions with complex kinetics[J]. Chem. Eng. Sci., 1996, 51(10): 2399-2407
[3]
Glasser D, Hildebrandt D. Reactor and process synthesis[J]. Comp. Chem. Eng., 1997, 21(suppl. 1): 775-783
[4]
Hu Yangdong(胡仰栋),Wu Lianying(伍联营), Hua Ben(华贲), Han Fangyu(韩方煜). The reactor network synthesis method based on derivative analysis[J]. J. Chem. Eng. Chinese Univ.(高校化学工程学报), 2002, 16(3): 331-334
[5]
Hu Yangdong(胡仰栋). Study on derivative analysis based approach to reaction process[D]. Guangzhou: South China University of Technology, 2000
[6]
Chitra S P, Govind R. Yield optimization for complex reactor system[J]. Chem. Eng. Sci., 1981, 36(7): 1219-1225
[7]
Chitra S P, Govind R. Synthesis of optimal serial reactor structures for homogeneous reactions(Ⅰ): Isothermal reactors[J]. AIChE J., 1985, 31(2): 177-184
[8]
Chitra S P, Govind R. Synthesis of optimal serial reactor structures for homogeneous reactions(Ⅱ): Nonisothermal reactors[J]. AIChE J., 1985, 31(2): 185-193
[9]
Zhao Wen(赵文). Reactor network synthesis research based on the least amount of waste[D]. Beijing: Beijing University of Chemical Technology, 1998
[10]
Zhao Wen, Zhou Chuanguang, Zhang Zhishan. Strategy of an attainable region partition for reactor network synthesis[J]. Ind. Eng. Chem.Res., 2002, 41(2): 190
[11]
Hu Yangdong(胡仰栋), Hua Ben(华贲), Han Fangyu(韩方煜). Optimal design of reactor network based on derivative analysis(Ⅰ): Simple reaction system[J]. Journal of Qingdao Institute of Chemical Technology (青岛化工学院学报), 2000, 21(2): 143-155
[12]
Kokossis A C, Floudas C A. Optimization of complex reactor networks-isothermal operation[J]. Chem. Eng. Sci., 1990, 45(3): 595-614
[13]
Kokossis A C, Floudas C A. Optimization of complex reactor networks-nonisothermal operation[J]. Chem. Eng. Sci., 1994, 49(7): 1037-1051
[14]
Horn F J M. Attainable and non-attainable regions in chemical reaction technique//Third European Symposium on Chemical Reaction Engineering[C]. London: Pergamon Press, 1964:1-10
[15]
Glasser D, Hildebrandt D, Crowe C. A geometric approach to steady flow reactors: the attainable region and optimization in concentration space[J]. Ind. Eng. Chem. Res., 1987, 26(9):1803-1810
[16]
Glasser D, Hildebrandt D. The attainable region and optimal reactor structures[J]. Chem. Eng. Sci., 1990, 45(8): 2161-2168
[17]
Glasser D, Hildebrandt D, Crowe C. Geometry of the attainable region generated by reaction and mixing: with and without constraints[J]. Ind. Eng. Chem. Res., 1989, 29(1):49-58
[18]
Glasser D, Hildebrandt D, Godorr S. The attainable region for segregated, maximum mixed and other reactor models[J]. Ind. Eng. Chem. Res., 1994, 33(5):1136-1144
[19]
Feinberg M, Hildebrandt D. Optimal reactor design from a geometric viewpoint(Ⅰ):Universal properties of the attainable region[J].Chem. Eng. Sci., 1997, 52(10): 1637-1665
[20]
Glasser D, Hildebrandt D. Optimal mixing for exothermic reversible reactions[J]. Ind. Eng. Chem. Res., 1992, 31(6):1541-1549
