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Caterpillar mini mixer

Reactor 21 [R 21] Caterpillar Mini Mixer-Tube Reactor... [Pg.401]

Figure 4.22 Second-generation caterpillar mini mixer with splitting plate and improved microstructure geometry [50]. Figure 4.22 Second-generation caterpillar mini mixer with splitting plate and improved microstructure geometry [50].
Figure 4.23 Near-ideal multi-lamination flow patterns in the second-generation caterpillar mini mixer as a result of introducing a splitting plate and improving micro structure geometry [50],... Figure 4.23 Near-ideal multi-lamination flow patterns in the second-generation caterpillar mini mixer as a result of introducing a splitting plate and improving micro structure geometry [50],...
This plate cuts the flow into pieces which are better defined than the poorly defined ones obtained by the first-generation caterpillar mini mixer. In addition, the micro structure geometry was improved by means of simulation. As a result, near-ideal multi-lamination flow patterns were yielded (Figure 4.23), which showed excellent correspondence with simulation [50]. [Pg.402]

Reactor type Caterpillar mini mixer-tube reactor, 1st generation Micro structure in one plate initial depth maximum depth 600 pm 850 pm... [Pg.402]

Mini mixer channel inihal width maximum width 1200 pm 2400 pm Total length of caterpillar mini mixer 19.2 mm... [Pg.402]

P 29] A set-up comprising a steel caterpillar mini mixer and four steel tubes attached was used, being dipped into a cylinder completely filled with a cooling medium (scale-up set-up) [48,108]. By means of a 5/2-way valve, it was possible to switch the reactants to either of the tubes acting as delay loops, differing in inner diameter and hence residence time. [Pg.467]

OS 40] [R 21] [P 29] Using a caterpillar mini mixer inserted in the scale-up setup, a maximum yield of 89% was determined [48]. This is even slightly higher than for the laboratory-scale setup (83%, see above). [Pg.468]

GL 22] [R 3] [R 9] [R 10] [P 23] The mass transfer efficiency of different gas/liquid contactors as a function of residence time was compared qualitatively (Figure 5.29), including an interdigital micro mixer, a caterpillar mini mixer, a mixing tee and three micro bubble columns using micro channels of varying diameter [5]. [Pg.639]

All other devices showed only the increasing part of such a dependence, i.e. the highest performance measured was obtained at the longest residence time [5], The best conversions with the interdigital micro and caterpillar mini mixers (-78 and -70%, respectively) still exceed considerably the performance of a conventional mixing tee (1 mm inner diameter). [Pg.640]

Figure 4.61 Yield of product and side/consecutive products as a function of temperature for the scale-up set-up with a caterpillar steel mini mixer [48],... Figure 4.61 Yield of product and side/consecutive products as a function of temperature for the scale-up set-up with a caterpillar steel mini mixer [48],...
A caterpillar steel mini mixer can be connected to conventional tubing, either stainless steel or polymeric, to prolong the residence time. The caterpillar mixer as all types of split-recombine mixers, profits from high volume flows (e.g. 100 1 h and more at moderate pressure drops) at favorable pressure drop (not exceeding 5 bar) as its internal microstructures can be held large [25-28]. [Pg.591]


See other pages where Caterpillar mini mixer is mentioned: [Pg.468]    [Pg.468]    [Pg.591]    [Pg.468]    [Pg.468]    [Pg.591]    [Pg.401]   
See also in sourсe #XX -- [ Pg.591 ]




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