1 |
DHOLE V R, LINNHOFF B. Distillation column targets[J]. Computers & Chemical Engineering, 1993, 17(5/6): 549-560.
|
2 |
ATASHPAZ GARGARI E, HASHEMZADEH F, RAJABIOUN R, et al. Colonial competitive algorithm: A novel approach for PID controller design in MIMO distillation column process[J]. International Journal of Intelligent Computing & Cybernetics, 2008, 1(3): 337-355.
|
3 |
李春利, 田昕, 李浩,等. 高沸点热敏体系精馏过程的研究进展[J]. 化工进展, 2022, 41(4): 1704-1714.
|
|
LI Chunli, TIAN Xin, LI Hao, et al. Research progress on distillation process in high boiling point and thermal sensitive system[J]. Chemical Industry and Engineering Progress, 2022, 41(4): 1704-1714.
|
4 |
纪智玲, 王志恒, 廖丽华, 等. 具有最低共沸点难分离物系变压精馏分离[J]. 化工进展, 2014, 33(S1): 85-88.
|
|
JI Zhiling, WANG Zhiheng, LIAO Lihua, et al. Pressure-swing distillation separation of liquid mixture with lowest azeotropic point[J]. Chemical Industry and Engineering Progress, 2014, 33(S1): 85-88.
|
5 |
张莘, 高伟, 齐鸣, 等. 基于多目标优化精馏系统综述[J]. 化工进展, 2019, 38(S1): 1-9.
|
|
ZHANG Shen, GAO Wei, QI Ming, et al. A review of optimization rectification systems based on multi-objective[J]. Chemical Industry and Engineering Progress, 2019, 38(S1): 1-9.
|
6 |
DOHERTY M F, CALDAROLA G A. Design and synthesis of homogeneous azeotropic distillations. 3. The sequencing of columns for azeotropic and extractive distillations[J]. Industrial & Engineering Chemistry Fundamentals, 1985, 24(4): 474-485.
|
7 |
VAZQUEZ-ESPARRAGOZA J J, MCLAUGHLIN B E, NAUGLE N W, et al. Solution of difficult distillation problems by use of a combination of the Newton—Raphson and functional transformation methods[J]. Computers & Chemical Engineering, 1988, 12(11): 1167-1169.
|
8 |
刘广杰, 孙晓岩, 毕荣山, 等. 复杂炼油塔模拟的改进联立方程内外层算法[J]. 化工学报, 2020, 71(5): 2118-2127.
|
|
LIU Guangjie, SUN Xiaoyan, BI Rongshan, et al. Improved equation oriented inside-out method of complex crude distillation column simulation[J]. CIESC Journal, 2020, 71(5): 2118-2127.
|
9 |
BIEU A S. Modeling a nonlinear binary distillation column[J]. Control Engineering and Applied Informatics, 2011, 13(1): 49-53.
|
10 |
荣本光, 郭天民, 利梅, 等. 用序贯模块法模拟多组分完全复杂的精馏流程:(I)模型与算法策略[J]. 计算机与应用化学, 1996, 13(3): 161-166.
|
|
RONG Benguang, GUO Tianmin, LI Mei, et al. Simulation of multicomponent complex distillation flowsheets with sequential modular approach (I) models and algorithm[J]. Computers and Applied Chemistry, 1996, 13(3): 161-166.
|
11 |
BOSTON J F, SULLIVAN JR S L. A new class of solution methods for multicomponent, multistage separation processes[J]. The Canadian Journal of Chemical Engineering, 1974, 52(1): 52-63.
|
12 |
VENKATARAMAN S, LUCIA A. Solving distillation problems by Newton-like methods[J]. Computers & Chemical Engineering, 1988, 12(1): 55-69.
|
13 |
IVAKPOUR J, KASIRI N. Developing a new initialization procedure for distillation column simulation[J]. Journal of Petroleum Science and Technology, 2014, 4(1): 41-46.
|
14 |
EDMISTER W C. Absorption and stripping-factor functions for distillation calculation by manual- and digital-computer methods[J]. AIChE Journal, 1957, 3(2): 165-171.
|
15 |
IVAKPOUR J, KASIRI N. Synthesis of distillation column sequences for nonsharp separations[J]. Industrial & Engineering Chemistry Research, 2009, 48(18): 8635-8649.
|
16 |
BROYDEN, C G. A class of methods for solving nonlinear simultaneous equations[J]. Mathematics of Computation, 1965, 19(92): 577-593.
|
17 |
RABEAU P, GANI R, LEIBOVICI C. An efficient initialization procedure for simulation and optimization of large distillation problems[J]. Industrial & Engineering Chemistry Research, 1997, 36(10): 4291-4298.
|
18 |
FLETCHER R, MORTON W. Initializing distillation column models[J]. Computers & Chemical Engineering, 2000, 23(11/12): 1811-1824.
|
19 |
BARTTFELD M, AGUIRRE P A. Optimal synthesis of multicomponent zeotropic distillation processes. 1. Preprocessing phase and rigorous optimization for a single unit[J]. Industrial & Engineering Chemistry Research, 2002, 41(21): 5298-5307.
|
20 |
UNDERWOOD A J V. Fractional distillation of ternary mixtures. Part II[J]. Journal of the Institute of Petroleum, 31: 111-118.
|
21 |
UNDERWOOD A J V. Fractional distillation of multi-component mixtures—calculation of minimum reflux ratio[J]. Chemical Engineering Progress, 1948, 44: 603-614.
|
22 |
UNDERWOOD A J V. Fractional distillation of multicomponent mixtures[J]. Chemical Engineering Progress, 1949, 41(12): 51-56.
|
23 |
REV E. The constant heat transport model and design of distillation columns with one single distributing component[J]. Industrial & Engineering Chemistry Research, 1990, 29(9): 1935-1943.
|
24 |
FELBAB N. An efficient method of constructing pinch point curves and locating azeotropes in nonideal distillation systems[J]. Industrial & Engineering Chemistry Research, 2012, 51(20): 7035-7055.
|
25 |
MAIER R W, BRENNECKE J F, STADTHERR M A. Reliable computation of homogeneous azeotropes[J]. AIChE Journal, 1998, 44(8): 1745-1755.
|