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Kinetic Model and Simulation Analysis for Toluene Disproportionation and C9-Aromatics Transalkylation 被引量:4

Kinetic Model and Simulation Analysis for Toluene Disproportionation and C9-Aromatics Transalkylation
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摘要 A new kinetic model for commercial unit of toluene disproportionation and C9-armatiocs transalkylation is developed based on the reported reaction scheme.A time based catalyst deactivation function taking weight hourly space velocity(WHSV)into account is incorporated into the model,which reasonably accounts for the loss in activity because of coke deposition on the surface of catalyst during long-term operation.The kinetic parameters are benchmarked with several sets of balanced plant data and estimated by the differential variable metric optimiza- tion method.Sets of plant data at different operating conditions are applied to make sure validation of the model and the results show a good agreement between the model predictions and plant observations.The simulation analysis of key variables such as temperature and WHSV affecting process performance is discussed in detail,giv- ing the guidance to select suitable operating conditions. A new kinetic model for commercial unit of toluene disproportionation and C9-armatiocs transalkylation is developed based on the reported reaction scheme.A time based catalyst deactivation function taking weight hourly space velocity(WHSV)into account is incorporated into the model,which reasonably accounts for the loss in activity because of coke deposition on the surface of catalyst during long-term operation.The kinetic parameters are benchmarked with several sets of balanced plant data and estimated by the differential variable metric optimiza- tion method.Sets of plant data at different operating conditions are applied to make sure validation of the model and the results show a good agreement between the model predictions and plant observations.The simulation analysis of key variables such as temperature and WHSV affecting process performance is discussed in detail,giving the guidance to select suitable operating conditions.
出处 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2007年第3期326-332,共7页 中国化学工程学报(英文版)
基金 Supported by the National'Creative Research Groups Science Foundation of China (No.60421002) and priority supported financially by "the New Century 151 Talent Project" of Zhejiang Province.
关键词 toluene disproportionation and C9-armatiocs transalkylation kinetic model catalyst deactivation func-tion parameter estimation simulation analysis 甲苯歧化 C9芳烃烷基转移 反应动力学 模型 模拟分析
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  • 1钟思青,陈庆龄,陈智强,童海颖,陈祎华,徐依菡.轴向流固定床内流场的数值模拟与实验验证[J].化工学报,2005,56(4):632-636. 被引量:16
  • 2侯卫锋,苏宏业,胡永有,褚健.催化重整集总动力学模型的建立及其在线应用[J].化工学报,2006,57(7):1605-1611. 被引量:22
  • 3Robschlager K H,Christoffel E G.Reaction mechanism of ethylbenzene isomerization.Ind.Eng.Chem.Prod.Res.Dev.,1979,18(4):347-352
  • 4Jenkins J H,Stephens T W.Kinetics of catalytic reforming.Hydrocarbon Processing,1980(11):163-167
  • 5WuDengxi(伍登熙) LinZhengxian(林正仙).Kinetic modeling of hydroisomerization of C8-aromatics(Ⅰ):Modeling and estimation of relative rate constants by the Wei-Prater method[J].化工学报,1985,3(3):257-267.
  • 6Cui Shichun(崔世纯),Zhu Dongmao(朱冬茂),Li Xiangyong(李向勇).Axial-flow fixed-bed reactor:CN,1351900A.2002
  • 7Huang Huajiang(黄华江).Practical Computer Simulation of Chemical Process-MATLAB's Application in Chemical Engineering(实用化工计算机模拟--MATLAB在化学工程中的应用).Beijing:Chemical Industry Press,2001
  • 8Hu Yongyou(胡永有).A study on simulation and optimization of naphtha catalytic reforming process[D].Hangzhou:Zhejiang University,2004
  • 9Gorra F,Breckenridge L L,Guy W M,Sailor R A.Selective toluene disproportionation process proven at Italian refinery.Oil&Gas Journal,1992,90(41):60-67
  • 10Shashldhar S B,Suresh R P.Toluene disproportionation over nickel-loaded aluminum-deficient mordenite(Ⅱ):Kinetics.Ind.Eng.Chem.Prod.Res.Dev.,1981,20:106-109

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  • 1于静江,周春晖.过程控制中的软测量技术[J].控制理论与应用,1996,13(2):137-144. 被引量:147
  • 2SULIKOWSKI B, RACHWALIK R. Catalytic Properties of Heteropoly Acid/Zeolite Hybrid Materials:Toluene Disproportion- ation and Transalkylation with 1,2,4-Trimethylbezene [ J ]. Applied Catalysis A : General,2003,256 : 173 - 182.
  • 3DAS J, BHAT Y S, BHARDWAJ A I, et al. Zeolite Beta Catalyzed C7 and C9 Aromatics Transformation [ J ]. Applied Catalysis A :General, 1994,116:71 - 79.
  • 4TSAI T C ,CHEN Wen-hua,LAI C S,et al. Kinetics of Toluene Disproportionation over Fresh and Coked H-mordenite [ J ]. Catalysis Today,2004,97:297 - 302.
  • 5EGAN C J. Calculated Equilibria of the Methylbenzenes and Benzene from 298 to 1 000 K[J]. J Chem Eng Data,1960,5 (3) :298 -29.
  • 6THAM M T,MONTAGUE G A,MORRIS A J,et al. Soft-sensors for Process Estimation and Inferential Control [ J ]. Journal of Process Control,1991,1 ( 1 ) :3 - 14.
  • 7MU Sheng-jing, ZENG Ying-zhi, LIU Rui-lan, et al. Online Dual Updating with Recursive PLS Model and Its Application in Predicting Crystal Size of Purified Terephthalic Acid (PTA) Process [ J ]. Journal of Process Control,2006,16 : 557 - 566.
  • 8孙建勋,林润雄,苗丽红,孙建敏,孙立水,张成龙.利用磷肥副产氟硅酸制白炭黑的氨化工艺研究[J].无机盐工业,2009,41(7):48-50. 被引量:10
  • 9秦颖,乐英红,高滋.化学液相沉积与沸石疏水性[J].高等学校化学学报,1998,19(9):1479-1483. 被引量:5
  • 10程文才,孔德金,杨德琴,符盼安,陈凤池,王磊.HAT-095甲苯歧化与烷基转移催化剂的研制与应用[J].石油化工,1999,28(2):107-111. 被引量:23

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