In order to prove the effectiveness of the optimization process and the proposed methodology, a refinery was taken as an example. There were 20 plants in total, e.g., a power station (PS), crude oil fractionation plant (COF), gas separation (GS), hydrogenation union (HU), residual and wax oil hydrodesulfurization (RWH), fluidized catalytic cracking (FCC), light hydrocarbon recovery (LHR), LPG desulfurization and demercaptan (LPGDD), sulfur recovery (SR), aromatics combine plant (AC), hydrogen production (HP), continuous catalytic reforming (CR), naphtha hydrofining (NH), polypropylene and polyester (PP), delayed coking (DC), air separation and compressor (ASC), central control room (CCR), railway transportation department (RTD), tank field (TF), and sewage treatment area (STA). The initial sizes of the plants are shown in Table 1. It should be noted that the lengths and widths include both the original plant sizes and the safety distances.
Table 1. Sizes and area of each plant.
Number |
Name |
Length (m) |
Width (m) |
Area (m2) |
1 |
PS |
205 |
234 |
47,970 |
2 |
COF |
95 |
190 |
18,050 |
3 |
GS |
37 |
59 |
2183 |
4 |
HU |
176 |
190 |
33,440 |
5 |
RWH |
165 |
190 |
31,350 |
6 |
FCC |
74 |
186 |
13,764 |
7 |
LHR |
59 |
44 |
2596 |
8 |
LPGDD |
59 |
146 |
8614 |
9 |
SR |
80 |
190 |
15,200 |
10 |
AC |
196 |
88 |
17,248 |
11 |
HP |
91 |
190 |
17,290 |
12 |
CR |
88 |
146 |
12,848 |
13 |
NH |
88 |
59 |
5192 |
14 |
PP |
73 |
146 |
10,658 |
15 |
DC |
124 |
205 |
25,420 |
16 |
ACS |
99 |
80 |
7920 |
17 |
CCR |
92 |
69 |
6348 |
18 |
RTD |
117 |
439 |
51,363 |
19 |
TF |
731 |
434 |
317,254 |
20 |
STA |
176 |
322 |
56,672 |
Process of Finding the Key Plant
In this section, the key plant with the greatest impact was found based on our methodology. Because the changes of the area and aspect ratio theoretically affect the overall industrial area, the two aspects were both studied. The area and aspect ratio of each plant were adjusted one by one while the sizes of other plants remained unchanged. The aim of this action is to study the influence on the area-wide layout of each plant. Two scenarios were used for the study. One scenario only changed the area of a certain plant, and the other adjusted the area and aspect ratio simultaneously.
When studying the area change of a plant, it was assumed that the area of the modified plant is 20%, 40%, 60% and 80% of the original one. The minimum of the occupied industrial area was set to be the optimization objective, and the e value of each plant was calculated one by one. When the area and aspect ratio were simultaneously changed, the area was still calculated as above, and the aspect ratio was regarded as a random variable with a certain upper and lower bound according to the inner structure of the plant. The aspect ratio was calculated with other variables in GA to obtain the modified plant layout and calculate the e value of the plant. The values of e of each plant with different areas and aspect ratios are listed in Table 2. Since GS and LHR are too small compared with other plants and have little impact on the overall layout, they are excluded from the selection of the key plant. RTD is not eligible to be the key plant because its size is fixed.
Table 2. e value of each plant.
Number |
Name |
Area Changes Aspect Ratio Stays the Same |
Area Changes Aspect Ratio Changes |
20% |
40% |
60% |
80% |
20% |
40% |
60% |
80% |
1 |
PS |
1.10 |
1.46 |
1.76 |
1.89 |
1.20 |
1.18 |
1.76 |
1.71 |
2 |
COF |
2.13 |
1.80 |
2.13 |
1.14 |
1.56 |
1.80 |
2.13 |
1.14 |
3 |
HU |
1.26 |
1.53 |
2.22 |
2.15 |
1.26 |
1.69 |
1.41 |
2.45 |
4 |
RWH |
1.35 |
1.14 |
1.55 |
2.94 |
1.27 |
1.36 |
1.55 |
2.94 |
5 |
FCC |
2.70 |
3.23 |
4.28 |
5.21 |
2.70 |
3.48 |
4.84 |
7.07 |
6 |
LPGDD |
2.68 |
3.17 |
4.16 |
2.38 |
2.08 |
2.38 |
3.57 |
2.38 |
7 |
SR |
2.19 |
1.80 |
2.19 |
2.70 |
1.35 |
1.80 |
2.28 |
3.62 |
8 |
AC |
1.41 |
1.88 |
2.23 |
4.46 |
2.08 |
1.58 |
2.23 |
2.08 |
9 |
HP |
1.93 |
1.38 |
1.63 |
2.98 |
1.41 |
1.78 |
2.22 |
4.15 |
10 |
CR |
2.69 |
3.06 |
2.79 |
3.19 |
2.59 |
3.06 |
3.19 |
3.44 |
11 |
NH |
2.96 |
3.95 |
1.97 |
3.95 |
4.44 |
3.29 |
1.97 |
3.95 |
12 |
PP |
3.25 |
3.05 |
1.90 |
1.92 |
3.13 |
3.05 |
4.33 |
5.29 |
13 |
DC |
1.66 |
1.55 |
1.81 |
2.82 |
1.86 |
1.95 |
2.82 |
3.63 |
14 |
ACS |
3.07 |
2.59 |
2.59 |
2.59 |
3.07 |
4.10 |
4.53 |
4.53 |
15 |
CCR |
4.24 |
3.77 |
2.83 |
3.23 |
3.63 |
3.77 |
3.63 |
3.23 |
16 |
TF |
1.05 |
1.10 |
1.15 |
1.16 |
1.03 |
1.07 |
1.05 |
1.11 |
17 |
STA |
1.06 |
1.24 |
1.49 |
1.72 |
1.29 |
1.18 |
1.49 |
1.27 |
In order to display the results more intuitively, the average value of e under the two different conditions was calculated and is drawn in Figure 2.
Figure 2. Average of e of each plant in two scenarios.
As mentioned above, the larger the value of e, the greater the influence of the plant on the area-wide layout. Combined with Table 2 and Figure 2, it can be seen that when only the area of a plant changes, the average e value of the FCC plant is higher than other plants. When both the aspect ratio and area are changed, the e value of the FCC plant is still larger in each area condition and is the largest in average. In particular, when the area is 80% of the original one, e reaches 7.07. This shows that the FCC plant has a much greater impact on the area-wide layout than other plants. When the area of the FCC plant is modified, the overall area can be significantly reduced. Therefore, the FCC plant was selected as the key plant in this case.
Internal Layout Optimization of the Key Plant
Through the efforts above, FCC was selected to be the key plant with 217 facilities in total, including 48 heat exchangers, 70 vessels, five reactors, six towers and 79 pumps, and 224 material connections. Since it was proved to be an effective way of modifying the key plant, the changes in the area and aspect ratio of the FCC plant were carried out at the same time by building a double-floor structure and modifying the inner layout of each floor.
For the internal layout of the FCC plant, the bottom length of the plant was set as a variable with 20 m lower bound and 60 m upper bound. The floor height was set as 6 m. Pumps were centrally arranged in a pump area with 16 rows and five columns on the first floor. Air coolers were placed on the second floor. Towers and reactors were placed across floors. Their shapes in a two-dimensional plane were circles and were treated as rectangles with sides equal to their diameters for the convenience of arrangement. Parallel heat exchangers were placed as groups with other facilities. The algorithm combining GA and SRFA was applied to solve the mathematical model by using parallel computation on MATLAB with the objective of minimizing the total cost. Figure 3 shows the plant layout plan after the modification, and Table 3 shows the comparison of the sizes and costs of the original and modified plant layout. Figure 4 shows the convergence curve of the hybrid algorithm. Due to the adoption of parallel computing, the calculation speed was greatly increased, and the computing time for the optimization of the layout inside the FCC plant was around 300 s.
Figure 3. Floor layout of modified FCC layout.
Figure 4. Convergence curve of the hybrid algorithm.
Table 3. Results comparison of original and modified FCC layout.
|
Original Layout |
Reconstruction Layout |
Length (m) |
34 |
42 |
Width (m) |
146 |
76 |
LC (104 ¥/a) |
49.57 |
32.15 |
PIC (104 ¥/a) |
30.26 |
34.99 |
POC (104 ¥/a) |
22.28 |
29.82 |
FC (104 ¥/a) |
0 |
19.29 |
TC (104 ¥/a) |
102.11 |
116.25 |
It can be seen from Table 3 that, after the modification, the area of the FCC plant is 64.89% of the original one. However, in terms of costs, the original layout is superior. After the modification, the total cost is higher. In order to facilitate comparative analysis, the comparison of five kinds of cost of the key plant is drawn in Figure 5.
Figure 5. The cost comparison of original and reconstruction layout.
Combined with Figure 3 and Figure 5 and Table 3, it can be seen that the modified layout satisfies the constraints established in the model; however, its total cost is higher than the original layout, which is 1.1625 million yuan per year.
As for LC, the land cost of the double-floor modified layout is lower, which is 64.89% of that of the original single-floor layout. However, in the ideal case where all the facilities can be arranged without constraints, the land cost should be 50% of the original one when an additional floor is added. The reason is that, firstly, the practical constraints must be satisfied. Secondly, towers and reactors occupy the same position on the two floors at the same time. Additionally, pumps must be placed on the first floor as a pump area, which limits the area of the first floor and may lead to the loose layout of other floors. Therefore, the land cost is 64.89% of the original one, instead of 50%. The pipe investment cost PIC and pumping operating cost POC after the modification are both higher. This is because the materials are transformed horizontally in the single-floor layout and only needs to overcome friction resistance. When it becomes a multi-floor structure, cross-floor connections are added, and the more connections in the vertical direction there are, the longer the vertical conveying distance will be. In addition to overcoming the friction resistance, the materials need to overcome gravity, which increases the energy consumption and leads to the increase in the operational cost. After the modification, due to the addition of floors, the floor construction cost FC needs to be taken into account. As for the total cost, after the modification, it is 141,400 CNY/a higher than the original cost.
Coupling of the Key Plant and Industrial Area
In this section, the key plant and other plants are optimized through coupling to figure out the effectiveness of the proposed methodology. With the initial sizes of all the plants and the sizes of the modified FCC plant, the industrial area is optimized with the objective of minimizing the total land cost. The original and modified industrial layout are, respectively, drawn in Figure 6 and Figure 7. The comparison of numerical results is represented in Table 4, which shows the respective and coupling results of the key plant and industrial area.
Figure 6. Layout diagram with original fluidized catalytic cracking (FCC).
Figure 7. Layout diagram with modified FCC.
Table 4. Results comparison of original and reconstruction FCC and industrial layout.
|
Original Layout |
Modified Layout |
Difference between the Modified and Original Layout |
Coupling Result |
FCC plant total annual cost (104 ¥/a) |
102.11 |
116.25 |
14.14 |
−180.61 |
Industrial annual cost (104 ¥/a) |
7492.75 |
7298.00 |
−194.75 |
The modified key FCC plant with a new area and aspect ratio was coupled with the whole industrial layout, and the e of the FCC plant was calculated to be 4.58, indicating that the change in the key plant can effectively reduce the industrial area. Combined with Figure 6 and Figure 7 and Table 4, it can be seen that, for the key plant itself, the total annual cost after the reconstruction is 141,400 CNY/a higher than before. However, when the key plant is coupled with other plants to reach an area-wide layout, there is a significant reduction in the overall total industrial cost. The coupling cost after the modification is 1,947,500 CNY/a less than before, which is around 17 times the increased cost of the key plant itself. Combined with the two costs, the overall total cost of the industrial layout reduces by 1,806,100 CNY/a. Even though the key plant cost is higher after the modification due to the increase in PIC, POC, and FC, the total cost of the industrial area is still much lower. This is because after the modification, the changes of the area and aspect ratio lead to a better coupling of the key plant and other plants. A more compact area-wide layout is acquired and the land is used more efficiently, which greatly reduces the occupied area and saves the land cost. Compared with the increased cost of the key plant itself, the reduced cost of the whole industrial land is far greater and, therefore, the modified layout is obviously better. This indicates that the key plant surely has a significant impact on the area-wide layout. The plant modification and the slight increase in costs in the key plant may lead to a substantial reduction in the total costs of the area-wide layout, which can provide an idea for the design of an industrial park.