[1] 徐林, 黄杰军, 俞磊, 等. 丙酮缩合法合成甲基异丁基酮的研究进展[J]. 化学通报, 2016, 79(7):584-588 Xu Lin, Huang Jiejun, Yu Lei, et al. Research progress in synthesis of methyl isobutyl ketone by acetone condensation method[J]. Chemical Bulletin. 2016, 79(7):584-588(in Chinese)
[2] 何志勇. 甲基异丁基酮生产技术现状及国内外市场分析[J]. 化学工业, 2018, 36(2):30-34, 43 He Zhiyong. Synthesis technical progress and analysis market of methyl isobutyl ketone[J]. Chemical Industry, 2018, 36(2):30-34, 43(in Chinese)
[3] 屈叶青. 甲基异丁基酮的生产与市场分析[J]. 石油化工技术与经济, 2017, 33(2):11-16 Qu Yeqing. Production and market analysis of methyl isobutyl ketone[J]. Technology & Economics in Petrochemicals, 2017, 33(2):11-16(in Chinese)
[4] 孟子涵. 丙酮二步法甲基异丁基酮工艺技术[J]. 辽宁化工, 2016, 45(12):1506-1508 Meng Zihan. The two-step process of preparing MIBK from acetone[J]. Liaoning Chemical Industry, 2016, 45(12):1506-1508(in Chinese)
[5] Podrebarac G G, Ng F T T, Rempel G L. A kinetic study of the aldol condensation of acetone using an anion exchange resin catalyst[J]. Chemical Engineering Science, 1997, 52(17):2991-3002
[6] Thotla S, Agarwal V, Mahajani S M. Simultaneous production of diacetone alcohol and mesityl oxide from acetone using reactive distillation[J]. Chemical Engineering Science, 2007, 62(18/20):5567-5574
[7] Thotla S, Agarwal V, Mahajani S M. Aldol condensation of acetone with reactive distillation using water as a selectivity enhancer[J].Industrial & Engineering Chemistry Research, 2007, 46(25):8371-8379
[8] 孙卓, 逯洋, 杨雪晴. MATLAB在化学化工中的应用[J]. 计算机与应用化学, 2018, 35(12):1012-1025 Sun Zhuo, Lu Yang, Yang Xueqing. MATLAB in chemistry and chemical[J]. Computers and Applied Chemistry, 2018, 35(12):1012-1025(in Chinese)
[9] 贾慧. 热力学模型参数对部分含低碳醇二元共沸物相行为预测的影响及应用[D]. 山东青岛:青岛科技大学, 2018 Jia Hui. Effects and applications of thermodynamic model parameters for the phase behavior prediction of some binary azeotropes containing lower alcohols[D]. Shandong Qingdao, China:Qingdao University of Science & Technology, 2018(in Chinese)
[10] 李旭. MATLAB在简单化学反应动力学教学中的应用[J]. 广州化工, 2015, 43(10):172-174, 187 Li Xu. Application of MATLAB in the teaching of simple chemical reaction kinetics[J]. Guangzhou Chemical Industry, 2015, 43(10):172-174, 187(in Chinese)
[11] 张兴法. n级不可逆气液反应的宏观动力学方程[J]. 合肥工业大学学报:自然科学版, 1995, 18(2):77-81 Zhang Xingfa. The over-all kinetic equation ofn-order irreversible gas-liquid reaction[J]. Journal of Hefei University of Technology:Natural Science, 1995, 18(2):77-81(in Chinese)
[12] 高铭书. 用分子结构法计算液体活度系数:UNIQUAC、UNIFAC及ASOG法简介[J]. 石油化工, 1981, 10(10):713-715 Gao Mingshu. Calculation of liquid activity coefficient by molecular structure method-Introduction of UNIQUAC, UNIFAC and ASOG methods[J]. Petrochemical Technology, 1981, 10(10):713-715(in Chinese)
[13] William L. Distillation design and control using Aspen simulation.[M]. John Wiley & Sons, 2013
[14] 廖丽华, 程建民, 汪志娟, 等. 碳三馏分选择加氢催化精馏及催化剂的研究[J]. 化学工业与工程, 2003, 20(5):275-278 Liao Lihua, Cheng Jianmin, Wang Zhijuan, et al. Study on C3 streams selective hydrogenation with distillation and catalyst[J]. Chemical Industry and Engineering, 2003, 20(5):275-278(in Chinese)
[15] Taylor R, Krishna R. Modelling reactive distillation[J]. Chemical Engineering Science, 2000, 55(22):5183-5229
[16] Huang C, Yang L, Ng F T T, et al. Application of catalytic distillation for the aldol condensation of acetone:A rate-based model in simulating the catalytic distillation performance under steady-state operations[J]. Chemical Engineering Science, 2000, 55(23):5919-5931
[17] Kim Y K, Hatfield J D. Kinetics and equilibrium data of the dehydration-hydration reaction between diacetone alcohol and mesityl oxide in phosphoric acid[J]. Journal of Chemical & Engineering Data, 1985, 30(2):149-153
[18] 姜斌, 杨静, 孙永利, 等. 连续流化催化精馏与间歇精馏制备乳酸乙酯的对比研究[J]. 化学工业与工程, 2015, 32(4):34-38 Jiang Bin, Yang Jing, Sun Yongli, et al. Comparison of ethyl lactate synthesis by continuous fluidized catalytic distillation and batch distillation[J]. Chemical Industry and Engineering, 2015, 32(4):34-38(in Chinese)
[19] 邵利, 杨彩娟, 许春建, 等. 浆料催化精馏制备甲缩醛[J]. 化学工业与工程, 2006, 23(6):471-474 Shao Li, Yang Caijuan, Xu Chunjian, et al. Preparation of methylal by slurry catalytic distillation process[J]. Chemical Industry and Engineering, 2006, 23(6):471-474(in Chinese)
[20] 王宇. 基于Aspen Plus的动力学子程序开发及固定床反应器模拟[J]. 广东化工, 2018, 45(18):78-79 Wang Yu. Kinetic user subroutine development and fixed bed reactor simulation based on aspen plus[J]. Guangdong Chemical Industry, 2018, 45(18):78-79(in Chinese)
[21] 诸林, 蒋鹏. 基于Aspen Plus用户模型的MTBE反应精馏模拟[J]. 计算机与应用化学, 2015, 32(1):30-34 Zhu Lin, Jiang Peng. Simulation of reactive distillation process for production of MTBE by developing user's module on Aspen Plus platform[J]. Computers and Applied Chemistry, 2015, 32(1):30-34(in Chinese)
[22] 赵月红, 温浩, 许志宏. Aspen Plus用户模型开发方法探讨[J]. 计算机与应用化学, 2003, 20(4):435-438 Zhao Yuehong, Wen Hao, Xu Zhihong. Discussions on development of user models for Aspen Plus[J]. Computers and Applied Chemistry, 2003, 20(4):435-438(in Chinese)
|