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In hydrodynamic problems it is an advantage to transform all variables into dimensionless parameters by 'scaling' each variable, using constants characterizing the dimensions and other properties of a given system. Thus, in the differential equations describing the systems, these constants are combined into dimensionless numbers or criteria. This formulation of the problem is very convenient because a process may be characterized in a much more general way by using the dimensionless criteria and, furthermore, in more complicated cases it is possible to find the properties of a system using a small model and then to apply the results to a large device keeping the criteria constant. In consideration of the hydrodynamic problem alone, it is usually attempted to characterize the studied system by three quantities, the characteristic length / (e.g. the length of the plate in the direction of the flowing liquid or the radius of a rotating disk), the velocity of the flowing liquid outside the Prandtl layer Vo and the kinematic viscosity v. The Cartesian coordinates of the system, x, y and z, are referred to the characteristic length / and the components of the velocity vx, vy and vz within the Prandtl layer are referred to the characteristic velocity Vo, -t=X, ^=Y, ^=VU y= Z (2.7.19) (2.7.20)

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how to reach the far router s network interface. Confirm what route information is being sent to CE1.

where u = x} y, z. When the first and third terms on the right-hand side of Eq. (2.7.8) are neglected, the Navier-Stokes equation is obtained in Cartesian coordinates as three equations: dX

*B:PE1# show router bgp neighbor 140.10.0.3 advertised-routes =========================================================== BGP Router ID : 140.10.0.1 AS : 65001 Local AS : 65001 =========================================================== Legend Status codes : u - used, s - suppressed, h - history, d - decayed, * - valid Origin codes : i - IGP, e - EGP, - incomplete, > - best =========================================================== BGP IPv4 Routes =========================================================== Flag Network LocalPref MED Nexthop VPN Label As-Path ----------------------------------------------------------[... Additional output omitted ...] 150.10.0.1/32 140.10.0.98 65002 150.10.0.11/32 140.10.0.98 65002 100 None -

The dimensionless number appearing in Eq. (2.7.21), = Re is called the Reynolds number. (2.7.22)

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While I advise you to let go of the urge to always center your subject in the frame and to employ the rule of thirds when possible instead, there are those times when the old center-comp does indeed work best. This occurs when I shoot a business portrait or I want to just capture a person s expression or some other element for the strongest effect. I ll look for balancing colors in the background or some architectural items I can use to frame my subject. Balance is what you re striving for and sometimes putting the subject smack dab in the middle does have the most powerful impact. The rule of odds further suggests that an odd number of subjects in an image is more interesting than an even number. An even number of subjects produces symmetries in the image that can appear unnatural and dif cult to balance visually. When shooting engagement sessions or couples, I often compose the shot in such a way as to create visual diagonals, balancing the shot by having one person slightly higher than the other or farther away.

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142 Its value, among others, characterizes the flow of the liquid in the system. For not very large Reynolds numbers the flow is laminar, which means that the velocity is stationary and its change monotonic in a perpendicular direction to the phase boundary between the phase boundary and the region of maximum relative velocity of the liquid. For very large values of Re the flow becomes turbulent. The value of the Reynolds number characterizing the start of turbulent flow depends strongly on the properties of the system. Thus, for example, in the case of a liquid flowing along a smooth plate the critical value is Re 1.5 x 103. However, this limiting value may be considerably decreased by attaching various obstacles to the surface or by roughening the surface. It holds approximately for the thickness of the Prandtl layer that <50~/VRe (2.7.23)

----------------------------------------------------------Routes : 6 =========================================================== *B:PE1>config>router>bgp# *B:PE1>config>router>bgp#

In order for the flow along the boundary to come to a steady state, it is necessary that R e l . It follows from the form of Eq. (2.7.21) that the solution for the flow rate can be expressed as a function of dimensionless quantities: Vu =fu(X, Y, Z, Re) (2.7.24)

6a. What specific IP address does PE2 specify as the next-hop address to reach its interfaces 6b. Is that address known to CE1 (In Step 1 of the previous exercise, did you remember to remove the toPE2 interface from PE1 s OSPF configuration )

The concentration of the transported substance c is converted to a dimensionless form, C = c/(c c*). Then the equation for convective diffusion at a steady state (2.7.7) can be converted by using Eqs (2.7.19) and (2.7.20) to the form

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