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Three-dimensional flow manifolds

In order to nummize the volume associated with interconnections and to come to a robust setup, a vertical arrangement of elem s is chosen [3] The construction of three-dimensional flow manifolds out of planar structures allows for a maximum flexibihty in the interconnection of the elements Instead of using valves to mtroduce samples mto the system, multiple pumps are used to control the flow in the system Although this mcreases the number of pumps required compared to a normal Flow Injection Analysis (FLA) system, it ehmmates the need for a micromachined sample mjection valve that is more difficult to realize... [Pg.182]

In Fig. 6, the dynamics on can be decomposed into the movement along the normal directions and the flow on the manifold Mg. Note that the time development of b does not affect the movement of the base points. Suppose two points PI and PI on with the same base point yl. Then, the orbit from PI through P2 reaching P3 and the one from PI through P2 reaching P3 are projected to the same movement of the base points on from yl through y2 reaching y3. In other words, the three-dimensional invariant manifold Wl consists of two-dimensional invariant manifolds that correspond to the movements of the base points. Then, in mathematics, we say that the three-dimensional stable manifold is foliated by two-dimensional leaves. This structure is called foliation [28,30]. [Pg.351]

Fig. 2.2. Supercritical (left) and subcriticcJ (right) Hopf bifurcations embedded in a three dimensional center manifold with a curved coordinate system (, i ) The arrows indicate the direction of the flow. Fig. 2.2. Supercritical (left) and subcriticcJ (right) Hopf bifurcations embedded in a three dimensional center manifold with a curved coordinate system (, i ) The arrows indicate the direction of the flow.
From the mathematical point of view the complexity is reduced because the system of equations which has to be solved is a function defined on the two-dimensional manifold of the control volumes boundary and leads to a dimension reduction. Practically the discretisation of the boundary usually is more simple than the meshing of complex three dimensional volumes. Especially this pertains to the transient flow channel geometry in co-rotating twin screw extruders. The surface meshes for the screws can independently be rotated inside the screw and barrel mesh analogous to the batchwise working internal mixer (Banbury Mixer) shown in the bottom part of Fig. 5.26. [Pg.501]

Verpoorte, E., van der School, B. H., Jeanneret, S., Manz, A., Widmer, H. M., and de Rooij, N. F., Three-dimensional micro flow manifolds for miniaturized chemical analysis systems, J. Micromech. Microeng., 4, 246,1994. [Pg.1439]

The PECVD or plasma polymerization represents a new technology that enables the production of thin films with manifold properties. Plasma polymerized layers are insoluble in organic solvents, indicative of the highly three dimensional crosslinked structure. The properties of such films can be influenced by parameters like pressure, flow rate, nature of monomer, carrier or reactive gases, power input, reactor configuration, substrate location, frequency (r.f. or microwave). In a "cold plasma" the particles are not in thermical equilibrium. The temperature of the electrons goes up to 10 °C, that of neutral particles and ions reaches about 300 C. The monomers get fragmented in the plasma and polymerize on the fibre surface. [Pg.288]

The geodesic flow has the function H Xf ) as a first integral. Examine three-dimensional level surfaces Q of the integral fT, that is, = ((x, ) T Mf = h = const). As we already know (see 2.1), these surfaces fibre over the surface Af with a circle as a fibre provided that h is greater than zero. Fix, for simplicity, the value of h to be equal to zero and examine a three-dimensional manifold Q, ... [Pg.273]

Center Manifolds. The Center Manifold Theorem (see Carr (1981)) states that all branches of stationary and periodic states in a neighborhood of a bifurcation point are embedded in a sub-manifold of the extended phase space X M that is invariant with respect to the flow generated by the ODE (2.1). All trajectories starting on this so-called center manifold remain on it for all times. All trajectories starting from outside of it exponentially converge towards the center manifold. Specifically, static bifurcations are embedded in a two dimensional center manifold, whereas center manifolds for Hopf bifurcations are three dimensional. Figures 2.1 and 2.2 summarize the geometric properties of the flows inside a center manifold in the case of saddle-node and Hopf bifurcations, respectively. [Pg.159]

Various calculations of reacting flows, such as perfectly stirred reactors [12], laminar flames [13,14], turbulent flames [15,16], and hypersonic flows [17] have verified the approach presented above. Due to space limitation we shall only present one example, namely a premixed laminar flat flame calculation [13]. It provides a nice, simple test case for the verification of the model. The specific example is a syngas (40 Vol. % CO, 30 Vol. % H2, 30 Vol. % N2)-air system at p = 1 bar, and with a temperature of 290 K in the unburnt gas. The fuel/air ratio is 6/10. The influence of simplified transport models is described elsewhere [13]. Here, for the sake of simplicity, only systems with equal diffusivity shall be considered. In this case a three-dimensional manifold with enthalpy and two reaction progress variables as parameters has been calculated, i.e. the chemistry has been simpli-... [Pg.340]

A three-dimensional modular setup for a miniaturized analysis system for flowing streams is presented The system uses silicon micromachined pumps and flow manifolds in combination with electrochemical sensors or optical detection Applications range from simple ion concentration measurements with ISFETs to a multi-step chemical analysis of phosphate Miniaturization of the flow systems leads to a substantial reduction in reagent consumption... [Pg.181]

An example of a smart tabulation method is the intrinsic, low-dimensional manifold (ILDM) approach (Maas and Pope 1992). This method attempts to reduce the number of dimensions that must be tabulated by projecting the composition vectors onto the nonlinear manifold defined by the slowest chemical time scales.162 In combusting systems far from extinction, the number of slow chemical time scales is typically very small (i.e, one to three). Thus the resulting non-linear slow manifold ILDM will be low-dimensional (see Fig. 6.7), and can be accurately tabulated. However, because the ILDM is non-linear, it is usually difficult to find and to parameterize for a detailed kinetic scheme (especially if the number of slow dimensions is greater than three ). In addition, the shape, location in composition space, and dimension of the ILDM will depend on the inlet flow conditions (i.e., temperature, pressure, species concentrations, etc.). Since the time and computational effort required to construct an ILDM is relatively large, the ILDM approach has yet to find widespread use in transported PDF simulations outside combustion. [Pg.331]

Note that the dimensions of the fast and slow manifolds will depend upon the time step. In the limit where At is much larger than all chemical time scales, the slow manifold will be zero-dimensional. Note also that the fast and slow manifolds are defined locally in composition space. Hence, depending on the location of 0q], the dimensions of the slow manifold can vary greatly. In contrast to the ILDM method, wherein the dimension of the slow manifold must be globally constant (and less than two or three ), ISAT is applicable to slow manifolds of any dimension. Naturally this flexibility comes with a cost ISAT does not reduce the number (Ns) of scalars that are needed to describe a reacting flow.168... [Pg.334]

The renormalization group flows of the variables A and B in this case is shown in Fig. 14. There is the trivial fixed point A = B = 0, which is reached if a < Xc u). If a > Xc u), the fixed point A = B = oo is reached. The two-dimensional space of possible initial conditions (A B >) is divided into the basins of attraction of these two fixed points. The common boundary of these basins is a line. This line is an invariant sub-manifold of the renormalization flows (i.e. points starting on the line remain on the line). On this line we have three fixed points ... [Pg.172]


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See also in sourсe #XX -- [ Pg.182 ]




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