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Transfer matrix global

The decoupling structure is depicted in Figure 11. The global transfer matrix is diagonal. It is clear that the decoupling, as stated, is not always possible, as the transfer function of the different blocks should be stable and physically feasible. If it is possible, the new input variable u will control the concentration and U2 will control the temperature, and both control loops could be tuned independently. Sometimes, a static decoupling is more than enough. [Pg.24]

Now this global transfer matrix can be used to express the boundary conditions at the inlet and outlet of die reactor. We assume that at t=0 at the inlet a sharp pulse of gas is injected into the system. Physically this means that 7iniet(0 = — 0 ). We also assume that the vacuum at the outlet is... [Pg.120]

For a one-zone TAP reactor with diffusion only, the global transfer matrix can be written as (with symbol for complicated irrelevant entries)... [Pg.121]

The zone transfer matrices will include all gases and their fluxes, so will be of dimension 2Ng) X (2Ng), and the global transfer matrix obtained as their product will have the same size, P P... [Pg.131]

This is similar to the outlet condition /outlet = v outiet for prescribed outlet velocity v, except that its role is played by the expression / ebS + ka)Den, which is a function of the Laplace variable s. Proceeding as usual to extract /outlet from the global transfer matrix,... [Pg.142]

If a TAP reactor is run with the injection point not at the left end, but internal to the cylinder, the formulation of the transfer matrix leads to further elegant equations. We write Pij for the global transfer matrix elements of the reactor to the left of the injection point and Qij for the elements to the right of this point (see Fig. 5.9). [Pg.143]

The technique of building the global transfer matrix is the same as for TAP reactors, but the boundary conditions are typically generalized to / = vc, that is, no diffusive flux at the outlet. This is the condition studied before in a generalized outlet condition for TAP reactors and leads to an outlet flux of the form... [Pg.146]

Global transfer matrix for tray column Consolidate equation (4) and equation (7) to attain ... [Pg.104]

Mass transfer limitations can be relevant in heterogeneous biocatalysis. If the enzyme is immobilized in the surface or inside a solid matrix, external (EDR) or internal (IDR) diffusional restrictions may be significant and have to be considered for proper bioreactor design. As shown in Fig. 3.1, this effect can be conveniently incorporated into the model that describes enzyme reactor operation in terms of the effectiveness factor, defined as the ratio between the effective (or observed) and inherent (in the absence of diffusional restrictions) reaction rates. Expressions for the effectiveness factor (rj), in the case of EDR, and the global effectiveness factor (t ) for different particle geometries, in the case of IDR, were developed in sections 4.4.1 and 4.4.2 (see Eqs. 4.39-4.42,4.53,4.54,4.71 and 4.72). Such functions can be generically written as ... [Pg.223]

In fibre composites, the presence of the fibres can change the fatigue strength of the matrix in several ways. On the one hand, global effects due to load transfer and the corresponding change in the stress and strain fields can play a role, on the other hand, local effects can occur, especially at the fibre-matrix interface. [Pg.347]


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See also in sourсe #XX -- [ Pg.120 , Pg.121 , Pg.131 , Pg.145 ]




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