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Multi mixing time

Micro mixers permit mixing times much below 1 s. Some multi-lamination micro mixers even approach sub-millisecond mixing [40]. Therefore, mixing can performed faster than most knovm reactions, including fast radical polymerizations. [Pg.502]

Considering the width of typical interdigital outlets, which are of the order of several tens of microns, it stands to reason that multi-lamination on its own is a rather slow mixing process, typically needing liquid mixing times of the order of seconds (see Figure 1.76 and, e.g., [34]). [Pg.103]

The simplest technique that enables phosphorus-phosphorus correlations for complex multi-component system and elucidation of structural constraints is the PDSD sequence.48 This experiment is relatively easy to set up however, the distances between spins cannot be established with satisfactory precision. One common way of determining distance type information using spin-7i NMR is based on the acquisition of the DQ filtered spectra as a function of the DQ mixing time.49 The recently introduced DQ homonuclear recoupling sequences based on C and/or R symmetry developed by Levitt and co-workers allows very precise analysis of intemuclear distances.50 The accuracy of distances obtained from these DQ experiments depends on the effective suppression of contributions to the spin Hamiltonian other than the required homonuclear dipolar coupling terms. [Pg.49]

Mixing simulation was carried out by finite volume computations with the multi physics software package CFDRC ACE +, 43 The mixing time was estimated assuming diffusion of water molecules in water (injected at a total flow rate of 2pLmin 1) across the microchannel. [Pg.203]

In order to work safely with multi-injection reactor, an accumulation of the limiting reactant and of heat in the main channel has to be thoroughly prevented. As the considered reactions are mostly Umited by mixing, the time required to mix can be estimated by using the correlation between specific energy dissipation and mixing time. Sufficient residence time should be provided between two injection points to minimize the hot spot. [Pg.226]

Selective intensification of mass transfer with respect to reaction. With a similar scale dependence to heat transfer, one can preferentially improve the selectivity of competing reactions, in either single- or multi-phase systems. For reasons of readability, the mixing times are not discussed in this chapter but would enter this category. [Pg.1035]

Polymer blending is a useful and attractive approach to new polymeric materials with more balanced properties than their components. Most polymers are immiscible so that during the processing these compraient polymers form a multi-phase system in their blends. Several factors such as the composition, viscosity ratio, elasticity ratio, interfacial tension, shear rate and mixing time have their own influences on the final morphology of the phases. [Pg.124]

It is user friendly and possesses a graphical user interface for developing the flow paths, ventilation system, and initial conditions. The FIRIN and CFAST modules can be bypassed and temperature, pressure, gas, release energy, mass functions of time specified. FIRAC i.s applicable to any facility (i.e., buildings, tanks, multiple rooms, etc,) with and without ventilation systems. It is applicable to multi species gas mixing or transport problems, as well as aerosol transport problems, FIRAC includes source term models for fires and limitless flow paths, except the FlRlN fire compartment limit of to no more than three... [Pg.354]

Interdigital micro mixers comprise feed channel arrays which lead to an alternating arrangement of feed streams generating multi-lamellae flows [39 2]. If processes have to be carried out with extended residence times (> 1 s) and/or at a temperature level different from the mixing step, tubes have to be attached to the interdigital micro mixers. Their internals comprise millimeter dimensions or below, if necessary. [Pg.399]

Figure 5.29 Special-type multi-purpose micro devices and mixing tee used for investigation of CO2 absorption. Comparison of their reactor performance as a function of the residence time. Micro bubble columns ( ) 1100 pm x 170 pm, (A) 300 pm x 100 pm and (T) 50 pm x 50 pm Interdigital mixer ( ) (40 pm) caterpillar mixer (A) (850 pm ramp) mixing tee (0) (1 mm) [5],... Figure 5.29 Special-type multi-purpose micro devices and mixing tee used for investigation of CO2 absorption. Comparison of their reactor performance as a function of the residence time. Micro bubble columns ( ) 1100 pm x 170 pm, (A) 300 pm x 100 pm and (T) 50 pm x 50 pm Interdigital mixer ( ) (40 pm) caterpillar mixer (A) (850 pm ramp) mixing tee (0) (1 mm) [5],...

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See also in sourсe #XX -- [ Pg.126 ]




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Mixing time

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