High-gravity and high-shear gas-liquid contactors for the chemical process industry

被引:22
作者
van der Schaaf, J. [1 ]
Schouten, J. C. [1 ]
机构
[1] Eindhoven Univ Technol, Dept Chem Engn & Chem, Lab Chem Reactor Engn, NL-5600 MB Eindhoven, Netherlands
关键词
SPINNING DISK REACTOR; PROCESS INTENSIFICATION; MASS-TRANSFER; FILM; STYRENE;
D O I
10.1016/j.coche.2011.08.005
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
Intensification of chemical processes leads to significantly smaller equipment with a considerable reduction in holdup of liquids and gases, thus reducing the impact of chemical hazards. Also, different, more expensive, construction materials and specialty coatings can be used, thereby increasing safety and durability of equipment. Additionally, the waste production can be reduced as a result of the higher mixing efficiency and better control of chemical conversion processes, which reduces environmental impact and increases resource efficiency. The thin-film spinning disc (TFSD), the rotor-stator spinning disc (RSSD), and a combination of these, are highly attractive for highly reactive, exothermic reactions in multiphase systems. A barrier for industrial application is its success: demonstration requires hazardous chemicals in large quantities and flows and is not easily done in university laboratories. A piloting facility with sufficient resources is needed where this and other process intensification equipment can be safely tested.
引用
收藏
页码:84 / 88
页数:5
相关论文
共 21 条
  • [1] Process intensification: heat and mass transfer characteristics of liquid films on rotating discs
    Aoune, A
    Ramshaw, C
    [J]. INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1999, 42 (14) : 2543 - 2556
  • [2] Process intensification: spinning disc reactor for condensation polymerisation
    Boodhoo, KVK
    Jachuck, RJ
    [J]. GREEN CHEMISTRY, 2000, 2 (05) : 235 - 244
  • [3] Classical cationic polymerization of styrene in a spinning disc reactor using silica-supported BF3 catalyst
    Boodhoo, KVK
    Dunk, WAE
    Vicevic, M
    Jachuck, RJ
    Sage, V
    Macquarrie, DJ
    Clark, JH
    [J]. JOURNAL OF APPLIED POLYMER SCIENCE, 2006, 101 (01) : 8 - 19
  • [4] Process intensification: spinning disk reactor for styrene polymerisation
    Boodhoo, KVK
    Jachuck, RJ
    [J]. APPLIED THERMAL ENGINEERING, 2000, 20 (12) : 1127 - 1146
  • [5] FAST REACTIONS IN ROTOR-STATOR MIXERS OF DIFFERENT SIZE
    BOURNE, JR
    STUDER, M
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1992, 31 (05) : 285 - 296
  • [6] Buhtz E, 1925, An improved method of and apparatus for carrying out chemical reactions, Patent No. [GB250722, 250722]
  • [7] Buhtz E, 1925, Method of and apparatus for carrying out chemical reactions or physical processes, Patent No. [US1629200, 1629200]
  • [8] Gas-liquid mass transfer in a rotor-stator spinning disc reactor
    Meeuwse, M.
    van der Schaaf, J.
    Kuster, B. F. M.
    Schouten, J. C.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2010, 65 (01) : 466 - 471
  • [9] Effect of rotor-stator distance and rotor radius on the rate of gas-liquid mass transfer in a rotor-stator spinning disc reactor
    Meeuwse, Marco
    Hamming, Edwin
    van der Schaaf, John
    Schouten, Jaap C.
    [J]. CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2011, 50 (10) : 1095 - 1107
  • [10] Multistage Rotor-Stator Spinning Disc Reactor
    Meeuwse, Marco
    van der Schaaf, John
    Schouten, Jaap C.
    [J]. AICHE JOURNAL, 2012, 58 (01) : 247 - 255