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Hot-Rolled Strip Laminar Cooling Process with Distributed Predictive Control  245


                                             1   2    3     …    n s  Strip thickness
                                         ∆z
                                      …                  …
                                         ∆l
                                       …   l s−1     l s  …  l n−1     l N
                                  l 1
                          l 0
                       z
                                            Subsystem i          Subsystem N
                            l
                                 Figure 11.4 The division of each subsystem


             problem. In each subsystem s, denote the number of volumes in the l-direction by n and the
                                                                                s
             z-direction by m as shown in Figure 11.4. Each volume, denoted by V, equals to ΔlΔz. Δl and
             Δz are the length and thickness of each volume, respectively. Denote the temperature of the
                                                    s
             ith z-direction and the jth l-direction volume by x .Let
                                                    i,j
                                        x 0  = x , i = 1, 2, … , m                (11.7)
                                              FT
                                         i,n s
                                       x N  = x N  , i = 1, 2, … , m              (11.8)
                                        i,n s  i,n s −1
               The energy balance equation (11.1) being applied to the top surface and bottom surface
             volumes leads to
                        s   (     (              s           ))
                          1, j  1               h 1, j  (   )      1
               ̇ x s  =−            x s  − x s  −Δz  x s  − x    −   v(x s  − x s  ) (11.9)
               1, j   s   s      2  2, j  1, j   s   1, j  ∞           1, j  1, j−1
                        cp    Δz                                   Δl
                      1, j  1, j                 1, j
                                 s    (    (                 s            ))
                                   m, j  1                  h m, j  (   )
                       ̇ x s  =−             x s  − x s  −Δz     x s  − x
                        m, j   s   s      2   m−1, j  m, j   s    m, j  ∞
                                  cp    Δz                    
                               m, j  m, j                    m, j
                               1   s     s
                             −   v(x  − x   )                                    (11.10)
                               Δl  m, j  m, j−1
               For the internal volumes, it is
                                      s
                                 1      i, j  s   s    s      1   s    s
                          s
                          ̇ x  =−        (x    − 2x + x   )−    v(x − x   )      (11.11)
                          i, j    2  s  s  i+1, j  i, j  i−1, j   i, j  i, j−1
                                Δz    cp                     Δl
                                    i, j  i, j
                      ̇
             where v = l is the coiling velocity, x s  = x s−1  when j = 1 and x s  = x s+1  when j = n .
                                                                                   s
                                          i, j−1  i,n s−1        i, j+1  i,1
               In industrial application, the measurements are available digitally with a sampling time Δt.
             Thus the discrete-time version of the subsystem is derived by approximating the derivatives
                                                          s
                                               s
                                                  s
             using simple Euler approximation. Since    ,    , and cp are temperature-dependent, define
                                               i, j  i, j  i, j
                                         s
                                                 s
                                                     s
                              2 s
                         s
               s
                                   s
             a(x )=−Δt   ∕(Δz    cp ),   (x )=Δta ∕   and    =Δtv/Δl. Then the nonlinear state
               i, j      i, j   i, j  i, j  i, j  i, j  i, j
             space representation of subsystem s, deduced from the previous Equations (11.7)–(11.11), can
             be expressed as
                {
                                                  s
                                            s
                              s
                                    s
                   s
                  x (k + 1) = f(x (k)) ⋅ x (k)+ g(x (k)) ⋅ u (k)+ D ⋅ x s−1  (k)
                                                           n s−1   s = 1, 2, … , N  (11.12)
                            s
                   s
                  y (k)= C ⋅ x (k)
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