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Spinning discs Reactor

In particular, two main streams of PI applications have been identified (i) PI innovations for reactors (e.g., microreactors, monolith reactors, spinning disc reactors, reactive separations) and (ii) PI technologies for more efficient energy transfer (e.g., ultrasound, pulse, plasma, microwave). Several PI technologies offer important potential, but require important fundamental/strategic research to reach proof-ofconcept on the laboratory scale. These PI technologies are ... [Pg.206]

Ramshaw, C. (2004) The spinning disc reactor, in Re-Engineering the Chemical Processing Plant Process Intensification (eds A. Stankiewicz and J.A. Moulijn), Marcel Dekker Inc., New York, pp. 69-119. [Pg.308]

Boodhoo, K.V.K., Jachuck, R.J., and Ramshaw, C. (1997) Spinning disc reactor for the intensification of styrene polymerization, in Process Intensification in Practice Applications and Opportunities (ed. J. Semel) Mechanical Engineering Publications, Ltd, Bury St. Edmunds, pp. 125-133. [Pg.308]

Spinning disc reactor Supercritical fluids Static mixer reactor Reactor... [Pg.248]

The use of a rotating reactor to provide efficient mixing has been proposed and tested for viscous polymerizations and acid-catalysed rearrangement reactions [6], The principle of these spinning disc reactors is that the centrifugal force... [Pg.222]

Figure 11.5 Schematic diagram of a spinning disc reactor. Products are collected from a cooled trough positioned below the disc... Figure 11.5 Schematic diagram of a spinning disc reactor. Products are collected from a cooled trough positioned below the disc...
Figure 20.19. View of sheared thin films on a spinning disc reactor 28 ... Figure 20.19. View of sheared thin films on a spinning disc reactor 28 ...
More recently spinning disc reactors have been used by Wilson et alP0) to carry out catalytic reactions using supported zinc triflate catalyst for the rearrangement of a-pinene oxide to yield campholenic aldehyde. The results of this study, presented in Table 20.1, suggest that by using a supported catalyst on a spinning disc reactor it is possible to... [Pg.1130]

Figure 20.20. Process time saving for the polymerisation styrene in a spinning disc reactor with a disc of 1.08 m in diameter rotating at 6.7 Hz (400 rpm/28)... Figure 20.20. Process time saving for the polymerisation styrene in a spinning disc reactor with a disc of 1.08 m in diameter rotating at 6.7 Hz (400 rpm/28)...
Table 20.1. Performance of batch, catalysed spinning-disc reactors(3°)... Table 20.1. Performance of batch, catalysed spinning-disc reactors(3°)...
Boodhoo, K. V. K. and JACHUCK, R. J. J. Appl. Therm. Eng. 20 (2000) 1127. Process intensification spinning disc reactor for styrene polymerisation. [Pg.1136]

Polycondensation reactions that are equilibrium controlled, such as polyesters, could benefit from the thin films generated in the RPB or spinning disc. In these reactions, removal of the coproduct of polymerization, e.g., ethylene glycol, is necessary in order to advance the polymerization, a task that becomes increasingly difficult as the reaction proceeds. The thin films and short residence time of high-gravity devices aid the evaporation and may permit operation at higher temperatures than conventional reactors (50). [Pg.70]

The main variables on a specific spinning disc reactor are ... [Pg.127]

These prices are for the spinning disc reactor as just defined in points a to c, including advanced control and data-logging software with computer and flat screen. The following ancillaries are usually necessary for the system, and these may exist, or Triton can recommend units or can supply them integrated into the system. [Pg.128]

Schematic of SDR system Lid with viewing windows Spinning Disc, diameter D Reactor Vessel Injector (with stirrer option)... Schematic of SDR system Lid with viewing windows Spinning Disc, diameter D Reactor Vessel Injector (with stirrer option)...
Boodhoo KVK, Jachuck RJJ, Ramshaw C. Spinning disc reactor for the intensification of styrene polymerisation. In Semel J, ed. 2nd International Conference on Process Intensification in Practice, Antwerp, Oct. 1997. [Pg.131]

Vicevic M, Jachuck RJ, Scott K. Process intensification for green chemistry rearrangement of ci-pinene oxide using a catalyzed spinning disc reactor. 4th International Conference on Process Intensification for the Chemical Industry, Brugge, Belgium, Sept. 10, 2001. [Pg.131]


See other pages where Spinning discs Reactor is mentioned: [Pg.160]    [Pg.160]    [Pg.300]    [Pg.303]    [Pg.13]    [Pg.250]    [Pg.253]    [Pg.1112]    [Pg.1129]    [Pg.1129]    [Pg.1130]    [Pg.70]    [Pg.70]    [Pg.81]    [Pg.84]    [Pg.88]    [Pg.88]    [Pg.125]    [Pg.126]    [Pg.129]    [Pg.131]    [Pg.197]   
See also in sourсe #XX -- [ Pg.303 ]

See also in sourсe #XX -- [ Pg.222 ]

See also in sourсe #XX -- [ Pg.222 ]




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