Synergizing Process Conditions, Water Sensitivity, and Kinetic Mechanisms to Optimize Sodium Salicylate Yield in Sodium Phenol Carboxylation

被引:0
作者
Zhang, Haodong [1 ]
Zhang, Junmei [2 ]
Ma, Jingjing [1 ]
Wu, Maoqian [1 ]
Hu, Linbo [3 ]
Chen, Hongfu [4 ]
Duan, Zhenya [1 ]
机构
[1] Qingdao Univ Sci & Technol, Coll Electromech Engn, Qingdao 266061, Peoples R China
[2] Qingdao Univ Sci & Technol, Coll Chem Engn, Qingdao 266042, Peoples R China
[3] Shandong Xinhua Pharmaceut Co Ltd, Shouguang 255000, Peoples R China
[4] Zhejiang Kejian Safety & Hlth Consulting Co LTD, Quzhou 324000, Zhejiang, Peoples R China
关键词
conversion rate; carboxylation reaction; kineticmodel; ash layer diffusion; KOLBE-SCHMITT CARBONATION; MASS-TRANSFER MODEL;
D O I
10.1021/acs.oprd.4c00383
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Sodium salicylate can be formed by carboxylation of solid sodium phenol particles with carbon dioxide gas under certain conditions. Single-factor experiments were carried out with self-made dried sodium phenol particles in a batch high-pressure reactor. It was determined that the carboxylation reaction of sodium phenol particles was more suitable under the conditions of a reaction temperature of 160 degrees C, a reaction pressure of 0.55 MPa, a reaction time of about 40 min, and a stirring speed of 50 rpm. Besides that, the water content of the material also had important effects on the yield. Through the establishment of the kinetic model of the carboxylation reaction between solid sodium phenol particles and carbon dioxide gas, the control step of the reaction temperature at 150 and 160 degrees C was determined as ash layer diffusion, and the kinetic equation was further calculated. The research results can provide the basic technological conditions and kinetic data of the carboxylation reaction of sodium phenol particles and provide a reference for the development of a continuous and efficient production process of sodium phenol carboxylation.
引用
收藏
页码:344 / 352
页数:9
相关论文
共 18 条
  • [1] Chongzhen W., 2003, Henan Sci, V21, P418
  • [2] Numerical simulation of a novel fluidized bed for gas-solid non-catalytic reactions (NRFB)
    Duan, Zhenya
    Sun, Shujie
    Lan, Zhujun
    Wang, Yan
    Zhang, Junmei
    Wang, Jingtao
    [J]. POWDER TECHNOLOGY, 2020, 372 : 428 - 437
  • [3] COMPARISON OF KINETIC AND DIFFUSIONAL MODELS FOR SOLID-GAS REACTIONS
    ISHIDA, M
    WEN, CY
    [J]. AICHE JOURNAL, 1968, 14 (02) : 311 - &
  • [4] Carboxylations of alkali metal phenoxides with carbon dioxide
    Kosugi, Y
    Imaoka, Y
    Gotoh, F
    Rahim, MA
    Matsui, Y
    Sakanishi, K
    [J]. ORGANIC & BIOMOLECULAR CHEMISTRY, 2003, 1 (05) : 817 - 821
  • [5] THE KOLBE-SCHMITT REACTION
    LINDSEY, AS
    JESKEY, H
    [J]. CHEMICAL REVIEWS, 1957, 57 (04) : 583 - 620
  • [6] Carboxylation of Phenols with CO2 at Atmospheric Pressure
    Luo, Junfei
    Preciado, Sara
    Xie, Pan
    Larrosa, Igor
    [J]. CHEMISTRY-A EUROPEAN JOURNAL, 2016, 22 (20) : 6798 - 6802
  • [7] Meng M., 2003, Fine Specialty Chem, V15, P17
  • [8] Mingxuan X., 2011, Chem. React. Eng. Technol, V27, P472
  • [9] KOLBE-SCHMITT CARBONATION OF 2-NAPHTHOL - CONFIRMATION OF MASS TRANSFER MODEL AND PROCESS OPTIMIZATION
    PHADTARE, PG
    DORAISWAMY, LK
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1969, 8 (02): : 165 - +
  • [10] MASS TRANSFER MODEL FOR KOLBE-SCHMITT CARBONATION OF 2-NAPHTHOL
    PHADTARE, PG
    DORAISWA.LK
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1965, 4 (03): : 274 - &