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-- SIMPLE HEAT EXCHANGER (Schiesser and Silebi, 1997) --------------------------------------------------------------------------------------------display N1 | display C8 | display R --------------------------------------------------------------------------------------------- -Schiesser numerical-differentiation operator -ARRAY vx[1], v[1] | -dummy arrays for submodel SUBMODEL DDx(n$, bb$, v, vx) Vector vx = (v{1} - v{-1}) * bb$ vx[1] = (-3 * v[1] + 4 * v[2] - v[3]) * bb$ vx[n$] = (3 * v[n$] 4 * v[n$ - 1] + v[n$ - 2]) * bb$ end --------------------------------------------------------------------------------------------L = 100 | -heat-exchanger tube length V = 10 | -flow velocity rho = 1 | -density of fluid in tube CP = 1 | -specific heat of fluid D=2 | -tube diameter H = 01 | -heat-transfer coefficient a = 4 * H/(rho * CP * D) -Tac = 100 | -constant annulus temperature T0c = 0 | -initial temperature in tube Tec = 50 | -tube-entry temperature -------------------------------------------------------------------------------------------------------------n = 201 | STATE u[n] | ARRAY ux[n] -DX = L/(n-1) | bb = 05/DX DT = 00005 | TMAX = 10 | NN = 20000 | scale = 100 irule 4 | RK4 rule ---------------X = 05 * (n-1) * DX/V | -time delay used in theoretical solution ---------------------------------------------------------------------------------------------program initial conditions u[k] for k = 1 to n | u[k] = T0c | next U = Tac | constant annulus temperature drun | write n = ;n -------------------------------------------------------------------------------------------------------------DYNAMIC -------------------------------------------------------------------------------------------------------------u[1] = Tec | set tube-entry boundary value for u invoke DDx(n, bb, u, ux) | -differentiate u to get ux Vectr d/dt u = - V * ux + a * (U - u) ------------------------------compare u with theoretical solution f f = 2 * (Tac + (T0c Tac * exp(-a * t) * (1 - swtch(t - X)) + swtch(t - X) * ((Tec - Tac) * exp(-a*X))) - scale uu = 2 * u[05*(n-1)] scale | errx5 = 25 * (uu - f) - 05 * scale dispt uu, errx5, f.



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Soft scheduling allows a new way of shortening this admission delay. The principle is to try to admit a new stream into the current round rather than waiting for the next round to begin. If admission to the current round is successful, then we can reduce the admission delay by one service round as shown in Figure 4.2. Let si be the start time for round i. Consider a new stream arriving at time ta when service round i is in progress. At that instant, the disk head is either moving to the next target track (Case 1) or stationed in a track reading data (Case 2). Let n be the track number for the target track (Case 1) or current track (Case 2). Assuming Poisson arrival and randomized placement, the disk head would be equally probable to be located at any one of the N tracks for non-zoned disks when a new request arrives. For zoned disks, the probability for the disk head to be located at track n when a new stream arrives, denoted by pn , would be skewed by the track size: pn = zn N 1 zj





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Not all sites need comment functionality, but chances are that a lot of the sites you ll be building with WordPress will. Most, if not all, blogs allow readers to comment on the posts, and the same goes for the vast majority of editorial sites out there, from newspapers to magazines. It is just a good way to connect with the readership, and while the sites in question may have completely different motives for doing this, and may have different comment policies, the basic functionality remains the same. From a WordPress theme designer s point of view, comments can be a bore, mostly because making them look good can be a problem. The actual code isn t all that hard, though, and if you like the default comment view (as featured in the default WordPress theme) you won t even have to create the comments.php template file. We looked closer at such a file in the A Closer Look at the Notes Blog Core section earlier in this chapter, so we ll gloss over that part for now and look at the comments from a less technical point of view for a little while. These are the most important things to consider when designing the comments section of a site:

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j= 0

n = 201

(4.12)

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FIGURE 7-9b Theoretical and computed time histories of the heat-exchanger tube temperature u(x, t) for x = L/2

where z j is the size of track j. We consider the case where the disk head is scanning in the forward direction with increasing track number. The case for reverse direction scanning is similar and thus is omitted here. To

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