Analysis of the synthesis of 1,1-dibutoxyethane in a simulated moving-bed adsorptive reactor

被引:28
|
作者
Graca, Nuno S. [1 ]
Pais, Luis S. [2 ]
Silva, Viviana M. T. M. [1 ]
Rodrigues, Alirio E. [1 ]
机构
[1] Univ Porto, LSRE, Associate Lab LSRE LCM, Dept Chem Engn,Fac Engn, P-4200465 Oporto, Portugal
[2] Braganca Polytech Inst, Sch Technol & Management, P-5301857 Braganca, Portugal
关键词
Simulated moving-bed reactors; Multifunctional reactors; Adsorption; Catalysis; Amberlyst; 15; ESTERIFICATION; CATALYSTS; BUTANOL;
D O I
10.1016/j.cep.2011.08.004
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The synthesis of 1,1 -dibutoxyethane was carried out in a simulated moving-bed pilot unit LICOSEP 12-26 (Novasep, France) with 12 columns packed with the commercial ion-exchange resin Amberlyst 15 (Rohm & Haas, France). Experimentally the best raffinate purity obtained was 85% with a productivity of 5.04 kg L-1 d(-1) and a desorbent consumption of 13.5 L kg(-1). The TMBR model was used to construct reaction/separation regions and to study the influence of feed composition, switching time, flow rates and mass-transfer resistances on the SMBR performance. The SMBR process shows a potential to be a competitive, efficient and environmentally friendly way to produce 1,1-dibutoxyethane and other acetals. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:1214 / 1225
页数:12
相关论文
共 50 条
  • [21] Simulated moving-bed reactor: Reactive-separation regions
    Minceva, M
    Rodrigues, AE
    AICHE JOURNAL, 2005, 51 (10) : 2737 - 2751
  • [22] ANALYSIS OF THE COUNTERCURRENT MOVING-BED CHROMATOGRAPHIC REACTOR
    PETROULAS, T
    ARIS, R
    CARR, RW
    COMPUTERS & MATHEMATICS WITH APPLICATIONS, 1985, 11 (1-3) : 5 - 34
  • [23] Continuous Synthesis and Purification by Direct Coupling of a Flow Reactor with Simulated Moving-Bed Chromatography
    O'Brien, Alexander G.
    Horvath, Zoltan
    Levesque, Francois
    Lee, Ju Weon
    Seidel-Morgenstern, Andreas
    Seeberger, Peter H.
    ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2012, 51 (28) : 7028 - 7030
  • [24] Synthesis of 1,1-dimethoxyethane in a fixed bed adsorptive reactor
    Gandi, GK
    Silva, VMTM
    Rodrigues, AE
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (06) : 2032 - 2039
  • [25] Coupled PermSMBR - Process design and development for 1,1-dibutoxyethane production
    Pereira, Carla S. M.
    Silva, Viviana M. T. M.
    Rodrigues, Alirio E.
    CHEMICAL ENGINEERING RESEARCH & DESIGN, 2014, 92 (11): : 2017 - 2026
  • [26] NUMERICAL-SIMULATION OF A SIMULATED COUNTERCURRENT MOVING-BED CHROMATOGRAPHIC REACTOR
    AJAY, AK
    CARR, RW
    CHEMICAL ENGINEERING SCIENCE, 1995, 50 (19) : 3033 - 3041
  • [27] Optimization of the Production of 1,1-Diethoxybutane by Simulated Moving Bed Reactor
    Spitters, Jasper
    Goncalves, Jonathan C.
    Faria, Rui P. V.
    Rodrigues, Alirio E.
    PROCESSES, 2021, 9 (02) : 1 - 21
  • [28] ANALYSIS AND PERFORMANCE OF A COUNTERCURRENT MOVING-BED CHROMATOGRAPHIC REACTOR
    PETROULAS, T
    ARIS, R
    CARR, RW
    CHEMICAL ENGINEERING SCIENCE, 1985, 40 (12) : 2233 - 2240
  • [29] COMPLETE DESIGN OF A SIMULATED MOVING-BED
    CHARTON, F
    NICOUD, RM
    JOURNAL OF CHROMATOGRAPHY A, 1995, 702 (1-2) : 97 - 112
  • [30] DESIGN OF OPTIMAL OPERATING-CONDITIONS OF SIMULATED MOVING-BED ADSORPTIVE SEPARATION UNITS
    STORTI, G
    BACIOCCHI, R
    MAZZOTTI, M
    MORBIDELLI, M
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (01) : 288 - 301