- 面向本质安全化的化工过程设计:多稳态及其稳定性分析
- 王杭州
- 740字
- 2020-11-28 22:34:47
参考文献
[1] Seider W D, Brengel D D, Provost A M, Widagdo S.Nonlinear analysis in process design.Why overdesign to avoid complex nonlinearities? [J]Industrial&Engineering Chemistry Research,1990,29(5):805-818.
[2] Kuhlmann A, Bogle D.Study on nonminimum phase behaviour and optimal operation [J].Computers&Chemical Engineering,1997,21(Supplement 1):S397-S402.
[3] Gritton K S, Seader J D, Lin W-J.Global homotopy continuation procedures for seeking all roots of a nonlinear equation[J].Computers&Chemical Engineering,2001,25(7-8):1003-1019.
[4] Jalali F, Seader J D, Khaleghi S.Global solution approaches in equilibrium and stability analysis using homotopy continuation in the complex domain[J].Computers&Chemical Engineering,2008,32(10):2333-2345.
[5] Wayburn T L, Seader J D.Homotopy continuation methods for computer-aided process design[J].Computers&Chemical Engineering,1987,11(1):7-25.
[6] Kiva V N, Alukhanova B M.Multiple steady states of distillation and its realisation[J]. Computers&Chemical Engineering,1997,21(Supplement 1):S541-S546.
[7] Wang C J, Wong D S H, Chien I L, Shih R F, Wang S J, Tsai C S.Experimental investigation of multiple steady states and parametric sensitivity in azeotropic distillation [J].Computers&Chemical Engineering,1997,21(Supplement 1):S535-S540.
[8] 蔡大用,白峰杉.现代科学计算[M].研究生数学教学系列.北京:科学出版社,2000.
[9] 陈传淼,谢资清.非线性微分方程多解计算的搜索延拓法[M].北京:科学出版社,2005.
[10] Hestenes M R, Stiefel E.Methods of conjugate gradients for solving linear systems [M].Vol.49.1952:National Bureau of Standards Washington, DC.
[11] 胡家赣,线性代数方程组的迭代解法[M].北京:科学出版社,1997.
[12] 李庆扬,莫孜中,祁力群.非线性方程组的数值解法[M].北京:科学出版社,1997.
[13] Ambrosetti A, Rabinowitz P H.Dual variational methods in critical point theory and applications[J].Journal of functional Analysis,1973,14(4):349-381.
[14] Seydel R, Hlavacek V.Role of continuation in engineering analysis[J].Chemical Engineering Science,1987,42(6):1281-1295.
[15] Scarf H.The Approximation of Fixed Points of a Continuous Mapping[J].SIAM Journal on Applied Mathematics,1967,15(5):1328-1343.
[16] 蔡大用,白峰杉.高等数值分析[M].北京:清华大学出版社,1998.
[17] 李艳,康卓,刘溥.郭涛算法及其应用[M].武汉汽车工业大学学报,2000(03):101-104.
[18] He J, Kang L.On the convergence rates of genetic algorithms[J].Theoretical Computer Science,1999,229(1-2):23-39.
[19] Uppal A, Ray W H, Poore A B.On the dynamic behavior of continuous stirred tank reactors[J].Chemical Engineering Science,1974,29(4):967-985.
[20] Antonelli R, Astolfi A.Continuous stirred tank reactors:easy to stabilise? [J] Automatica,2003,39(10):1817-1827.
[21] Razon L F.Effect of reactor heat capacity on the stability and start-up time of a diabatic controlled-cycled stirred tank reactor[J].Chemical Engineering Communications, 2005,192(9):1194-1203.
[22] Meel A, Seider W D, Soroush M.Game theoretic approach to multiobjective designs:Focus on inherent safety[J].AIChE journal,2006,52(1):228-246.
[23] Gamboa-Torres A E, Flores-Tlacuahuac A.Effect of process modeling on the nonlinear behaviour of a CSTR Reactions A--> B--> C[J].Chemical Engineering Journal,2000,77(3):153-164.
[24] Bhattacharya D, Guba D, Rooy N.Liquid phase air-oxidation of toluene to benzoic acid(II)Kinetics and mechanism[J].Chemical Age of India,1973,24(2):87-90.
[25] Borgaonkar H, Raverkar S, Chandalia S.Liquid phase oxidation of toluene to benzaldehyde by air[J].Industrial & Engineering Chemistry Product Research and Development,2002,23(3):455-458.
[26] Wu X, Chen S.Synthesis and Refining of benzoic acid[J].Modern Chemical Industry, 2000,20(8):10-14.
[27] Guo C, Liu Q, Wang X, Hu H.Selective liquid phase oxidation of toluene with air[J]. Applied Catalysis A, General,2005,282(1-2):55-59.
[28] Zhang Y, Li C, He X, Chen B.Simulation and Optimization in the Process of Toluene Liquid-phase Catalytic Oxidation[J].Chinese Journal of Chemical Engineering,2008, 16(1):36-38.
[29] Wang H, Chen B, He X, Zhao J, Qiu T.Analysis of steady state multiplicity of chemical reaction systems[J].Huagong Xuebao/CIESC Journal,2009,61(1):127-133.