Consider an oil refinery scenario. A step in refining crude oil into finished oil products involves a distillation process that splits crude into various streams. Suppose there are three types of crude available: Arabian light (a_l), Arabian heavy (a_h), and Brega (br). These crudes are distilled into light naphtha (na_l), intermediate naphtha (na_i), and heating oil (h_o). These in turn are blended into two types of jet fuel. Jet fuel j_1 is made up of 30% intermediate naphtha and 70% heating oil, and jet fuel j_2 is made up of 20% light naphtha and 80% heating oil. What amounts of the three crudes maximize the profit from producing jet fuel (j_1, j_2)? This problem can be formulated as the following linear program:
The constraints "blend1" and "blend2" ensure that j_1 and j_2 are made with the specified amounts of na_i and na_l, respectively. The constraint "blend3" is actually the reduced form of the following constraints:
where h_o1 and h_o2 are dummy variables.
You can use the following SAS code to create the input data set ex1
:
data ex1; input field1 $ field2 $ field3 $ field4 field5 $ field6; datalines; NAME . EX1 . . . ROWS . . . . . N profit . . . . E napha_l . . . . E napha_i . . . . E htg_oil . . . . L blend1 . . . . L blend2 . . . . L blend3 . . . . COLUMNS . . . . . . a_l profit -175 napha_l .035 . a_l napha_i .100 htg_oil .390 . a_h profit -165 napha_l .030 . a_h napha_i .075 htg_oil .300 . br profit -205 napha_l .045 . br napha_i .135 htg_oil .430 . na_l napha_l -1 blend2 -1 . na_i napha_i -1 blend1 -1 . h_o htg_oil -1 blend3 -1 . j_1 profit 350 blend1 .3 . j_1 blend3 .7 . . . j_2 profit 350 blend2 .2 . j_2 blend3 .8 . . BOUNDS . . . . . UP . a_l 110 . . UP . a_h 165 . . UP . br 80 . . ENDATA . . . . . ;
You can use the following call to PROC OPTLP to solve the LP problem:
proc optlp data=ex1 objsense = max algorithm = primal primalout = ex1pout dualout = ex1dout logfreq = 1; run; %put &_OROPTLP_;
Note that the OBJSENSE=MAX option is used to indicate that the objective function is to be maximized.
The primal and dual solutions are displayed in Output 12.1.1.
Output 12.1.1: Example 1: Primal and Dual Solution Output
Primal Solution |
Obs | Objective Function ID | RHS ID | Variable Name |
Variable Type |
Objective Coefficient |
Lower Bound |
Upper Bound | Variable Value | Variable Status |
Reduced Cost |
---|---|---|---|---|---|---|---|---|---|---|
1 | profit | a_l | D | -175 | 0 | 110 | 110.000 | U | 10.2083 | |
2 | profit | a_h | D | -165 | 0 | 165 | 0.000 | L | -22.8125 | |
3 | profit | br | D | -205 | 0 | 80 | 80.000 | U | 2.8125 | |
4 | profit | na_l | N | 0 | 0 | 1.7977E308 | 7.450 | B | 0.0000 | |
5 | profit | na_i | N | 0 | 0 | 1.7977E308 | 21.800 | B | 0.0000 | |
6 | profit | h_o | N | 0 | 0 | 1.7977E308 | 77.300 | B | 0.0000 | |
7 | profit | j_1 | N | 350 | 0 | 1.7977E308 | 72.667 | B | 0.0000 | |
8 | profit | j_2 | N | 350 | 0 | 1.7977E308 | 33.042 | B | 0.0000 |
Dual Solution |
Obs | Objective Function ID | RHS ID | Constraint Name | Constraint Type |
Constraint RHS |
Constraint Lower Bound |
Constraint Upper Bound |
Dual Variable Value |
Constraint Status |
Constraint Activity |
---|---|---|---|---|---|---|---|---|---|---|
1 | profit | napha_l | E | 0 | . | . | 0.000 | L | 0.00000 | |
2 | profit | napha_i | E | 0 | . | . | -145.833 | U | 0.00000 | |
3 | profit | htg_oil | E | 0 | . | . | -437.500 | U | 0.00000 | |
4 | profit | blend1 | L | 0 | . | . | 145.833 | L | -0.00000 | |
5 | profit | blend2 | L | 0 | . | . | 0.000 | B | -0.84167 | |
6 | profit | blend3 | L | 0 | . | . | 437.500 | L | 0.00000 |
The progress of the solution is printed to the log as follows.
Output 12.1.2: Log: Solution Progress
NOTE: The OPTLP procedure is executing in single-machine mode. |
NOTE: The problem EX1 has 8 variables (0 free, 0 fixed). |
NOTE: The problem has 6 constraints (3 LE, 3 EQ, 0 GE, 0 range). |
NOTE: The problem has 19 constraint coefficients. |
WARNING: The objective sense has been changed to maximization. |
NOTE: The LP presolver value AUTOMATIC is applied. |
NOTE: The LP presolver removed 3 variables and 3 constraints. |
NOTE: The LP presolver removed 6 constraint coefficients. |
NOTE: The presolved problem has 5 variables, 3 constraints, and 13 constraint |
coefficients. |
NOTE: The LP solver is called. |
NOTE: The Primal Simplex algorithm is used. |
Objective Entering Leaving |
Phase Iteration Value Time Variable Variable |
P 1 1 0.000000E+00 0 |
P 2 2 0.000000E+00 0 j_1 blend1 (S) |
P 2 3 1.405640E-01 0 j_2 blend3 (S) |
P 2 4 1.454487E-01 0 a_l blend2 (S) |
P 2 5 2.379819E-01 0 br a_l |
P 2 6 1.202394E+03 0 blend2 (S) br |
P 2 7 1.348074E+03 0 |
D 2 8 1.347917E+03 0 |
NOTE: Optimal. |
NOTE: Objective = 1347.9166667. |
NOTE: The Primal Simplex solve time is 0.00 seconds. |
NOTE: The data set WORK.EX1POUT has 8 observations and 10 variables. |
NOTE: The data set WORK.EX1DOUT has 6 observations and 10 variables. |
Note that the %put statement immediately after the OPTLP procedure prints value of the macro variable _OROPTLP_ to the log as follows.
The value briefly summarizes the status of the OPTLP procedure upon termination.