Binary Variable y;
If the number of subcycles of feed i in furnace l is equal to k, the binary variable Y(i,l,k) is one.
decaying performance:
defobj.. Tcycle * obj =e= sum((i,j),
Cc(i,j)*t(i,j) - Cs(i,j)*n(i,j)
+ Cp(i,j)*n(i,j)*(1 - exp(-b(i,j)*t(i,j)/n(i,j)))) ;
$Title Cyclic Scheduling of Continuous Parallel Units (CSCHED,SEQ=222)
$ontext
Cyclic Scheduling of Continuous Parallel Units
Jain, V, and Grossmann, I E, Cyclic Scheduling of Continuous
Parallel Units with Decaying Performance. American Institute
of Chemical Engineers Journal 44, 7 (1998), 1623-1636.
$offtext
Set k subcycles
kzero(k) subcycle 0
i furnaces
j feeds
Parameter tau(i,j) "changeover time [days]"
D(i,j) "processing rate [tons/day]"
a(i,j) "conversion parameters [1/day]"
b(i,j) "conversion parameter [1/day]"
c(i,j) "conversion parameter [1/day]"
p(i,j) "price parameter [$/ton]"
Cs(i,j) "setup/cleaning cost [$]"
Flo(j) lower bnd on flow rate
Fup(j) upper bnd on flow rate
Cc(i,j)
Cp(i,j)
yk(k);
Scalar U upper bound on processing time
epsi "small const to avoid 0/0"
Variables t(i,j) process time of feed in furnace
n(i,j) number of subcycles of feed in furnace
F(j) rate of arrival of feed j
S(j) extra amount of feed processed above min
dt(i,j) time devoted to feed in furnace
Tcycle common cycle time for all furnaces
y(i,j,k) "SOS to model n(i,j)"
obj objective variable;
Positive Variable t, n, S, dt, Tcycle;
Binary Variable y;
Equation defobj "objective is to maximize profit/cycle-time"
massbal_1(j) "mass balance equations (8)"
massbal_2(j) "mass balance equations (9)"
integ_1(i,j) "integrality constraints (10)"
integ_2(i,j) "integrality constraints (11)"
time_1(i,j) "relate total time of feed to processing & clean-up"
time_2(i) "total time less than cycle time"
time_3(i,j) "t(i,j) is zero if number of subcycles is zero"
extra(j) "extra constraints";
defobj.. Tcycle * obj =e= sum((i,j),
Cc(i,j)*t(i,j) - Cs(i,j)*n(i,j)
+ Cp(i,j)*n(i,j)*(1 - exp(-b(i,j)*t(i,j)/n(i,j)))) ;
massbal_1(j).. Flo(j)*Tcycle + S(j) =e= sum(i, D(i,j)*t(i,j));
massbal_2(j).. S(j) =l= (Fup(j) - Flo(j))*Tcycle;
integ_1(i,j).. n(i,j) =e= sum(k, yk(k) * y(i,j,k));
integ_2(i,j).. 1 =e= sum(k, y(i,j,k));
time_1(i,j).. dt(i,j) =e= n(i,j)*tau(i,j) + t(i,j);
time_2(i).. sum(j, dt(i,j)) =l= Tcycle;
time_3(i,j).. t(i,j) =l= sum(kzero,U*(1 - y(i,j,kzero)));
extra(j)$(Flo(j) > 0).. sum(i, n(i,j)) =g= 1;
model csched /all/;
$if not set dataset $set dataset 1
$include csched%dataset%.inc
yk(k) = ord(k)-1; yk(kzero) = epsi;
Cc(i,j) = P(i,j)*D(i,j)*c(i,j);
Cp(i,j) = P(i,j)*D(i,j)*a(i,j)/ b(i,j);
n.up(i,j) = card(k)-1;
n.l(i,j) = 1;
n.lo(i,j) = epsi;
F.lo(j) = Flo(j); F.up(j) = Fup(j);
Tcycle.l = 100;
solve csched maximizing obj using minlp;
$ontext
Cyclic Scheduling of Continuous Parallel Units
Jain, V, and Grossmann, I E, Cyclic Scheduling of Continuous
Parallel Units with Decaying Performance. American Institute
of Chemical Engineers Journal 44, 7 (1998), 1623-1636.
$offtext
Set k subcycles
kzero(k) subcycle 0
i furnaces
j feeds
Parameter tau(i,j) "changeover time [days]"
D(i,j) "processing rate [tons/day]"
a(i,j) "conversion parameters [1/day]"
b(i,j) "conversion parameter [1/day]"
c(i,j) "conversion parameter [1/day]"
p(i,j) "price parameter [$/ton]"
Cs(i,j) "setup/cleaning cost [$]"
Flo(j) lower bnd on flow rate
Fup(j) upper bnd on flow rate
Cc(i,j)
Cp(i,j)
yk(k);
Scalar U upper bound on processing time
epsi "small const to avoid 0/0"
Variables t(i,j) process time of feed in furnace
n(i,j) number of subcycles of feed in furnace
F(j) rate of arrival of feed j
S(j) extra amount of feed processed above min
dt(i,j) time devoted to feed in furnace
Tcycle common cycle time for all furnaces
y(i,j,k) "SOS to model n(i,j)"
obj objective variable;
Positive Variable t, n, S, dt, Tcycle;
Binary Variable y;
Equation defobj "objective is to maximize profit/cycle-time"
massbal_1(j) "mass balance equations (8)"
massbal_2(j) "mass balance equations (9)"
integ_1(i,j) "integrality constraints (10)"
integ_2(i,j) "integrality constraints (11)"
time_1(i,j) "relate total time of feed to processing & clean-up"
time_2(i) "total time less than cycle time"
time_3(i,j) "t(i,j) is zero if number of subcycles is zero"
extra(j) "extra constraints";
defobj.. Tcycle * obj =e= sum((i,j),
Cc(i,j)*t(i,j) - Cs(i,j)*n(i,j)
+ Cp(i,j)*n(i,j)*(1 - exp(-b(i,j)*t(i,j)/n(i,j)))) ;
massbal_1(j).. Flo(j)*Tcycle + S(j) =e= sum(i, D(i,j)*t(i,j));
massbal_2(j).. S(j) =l= (Fup(j) - Flo(j))*Tcycle;
integ_1(i,j).. n(i,j) =e= sum(k, yk(k) * y(i,j,k));
integ_2(i,j).. 1 =e= sum(k, y(i,j,k));
time_1(i,j).. dt(i,j) =e= n(i,j)*tau(i,j) + t(i,j);
time_2(i).. sum(j, dt(i,j)) =l= Tcycle;
time_3(i,j).. t(i,j) =l= sum(kzero,U*(1 - y(i,j,kzero)));
extra(j)$(Flo(j) > 0).. sum(i, n(i,j)) =g= 1;
model csched /all/;
$if not set dataset $set dataset 1
$include csched%dataset%.inc
yk(k) = ord(k)-1; yk(kzero) = epsi;
Cc(i,j) = P(i,j)*D(i,j)*c(i,j);
Cp(i,j) = P(i,j)*D(i,j)*a(i,j)/ b(i,j);
n.up(i,j) = card(k)-1;
n.l(i,j) = 1;
n.lo(i,j) = epsi;
F.lo(j) = Flo(j); F.up(j) = Fup(j);
Tcycle.l = 100;
solve csched maximizing obj using minlp;
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