Research on Multi-Decision Sinter Composition Optimization Based on OLS Algorithm
Abstract
:1. Introduction
2. Least Square Method (OLS)
2.1. OLS Algorithm
- (1)
- The raw material composition analysis method based on the OLS algorithm can analyze the characteristics and differences of different raw materials. This method takes into account the analysis of raw material composition by traditional ore blending and the dimensionless machine learning algorithm, and can improve the sintering process while complying with the sintering process.
- (2)
- The raw material ratio adjustment method based on multiple decisions can accurately adjust the ratio according to the weight of various constraints and can adapt to a variety of production environments.
- (3)
- The calculation time complexity of the sintering ore blending model is low, and the calculation performance is significantly better than other sintering ore blending algorithms, which can meet the real-time requirements of online material change.
2.2. Fitting to the Analysis
3. Multiple Decision Ore Allocation Algorithm Based on OLS Analysis
3.1. Overall Algorithm Framework
3.2. Multiple-Decision Ore Allocation Algorithm Based on OLS Analysis
- (1)
- We need to use the OLS algorithm to fit the ratio and each component of the sintered ore one by one. Among them, x is the ore powder to be mainly adjusted, and y is the composition of sintered ore.
- (2)
- Import the DataFrame data source in Python, specify x and y for fitting, and establish the mapping relationship between x and y in the program through the fit() method.
- (3)
- Obtain the OLS fitting report through the summary() method, and count the slopes in all OLS reports. Sintering ore blending should not only consider the influence of composition but also factors such as price and equipment operation. In the company’s sintering ore blending process, the items that need to be considered in weight are listed in Table 1 below:
- (1)
- Maintain the raw material warehouse and update information such as available raw materials, storage volume, raw material composition, and price.
- (2)
- Set the ratio of raw materials used in the current production line and the ratio of blast furnace charge as a benchmark for the ore blending plan.
- (3)
- Set the target element target value of the blast furnace charge.
- (4)
- Start by solving the decision and getting the result.
4. Case of Multiple Decision Ore Blending Algorithm Based on OLS Analysis
4.1. Evaluation Criteria for Experimental Data Sets and Protocol Feasibility
4.2. Performance Test
4.3. Model Application
4.4. Accuracy of Decision-Making
- ①
- According to the recent iron powder purchase situation, the ore powder 8 in the warehouse is about to be used up. It is expected that the cost of molten iron will increase after the material change, and the subsequent adjustment of the blast furnace charge structure and the increase in the proportion of pellets will reduce the cost of molten iron;
- ②
- It is estimated that after reducing the proportion of ore powder 8, the alkali load of the sintering blast furnace will decrease;
- ③
- In addition, due to the influence of limestone powder procurement, the lime ratio is increased, the daily consumption of limestone powder is controlled to be about 700 t/day, the daily consumption of limestone is controlled to be 1650 t/t, and the coke powder is calculated based on 55.8 Kg/t of sintered ore;
- ④
- MgO in sinter is controlled according to the 2.6–2.7 midline, and it is estimated that the pre-mixing will start to change at 6 o’clock after 8 days;
4.5. Model Improvement and Practical Application
5. Conclusions
- (1)
- The model realizes the calculation of the composition of sinter and blast furnace charge. On this basis, there are 15 decision-making items to evaluate the sintering scheme to get the optimal scheme.
- (2)
- By simulating the real production situation for ore blending, a solution that meets the requirements can be calculated within 0.9s.
- (3)
- According to the experimental results, 96% of the final schemes are feasible, 4% are not suitable for practical application, and the comprehensive effect is better.
- (4)
- Engineers continuously revise the model according to the production situation, and the model will become more accurate until it can replace the traditional method.
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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First-Level Decision Items | Second-Level Decision-Making |
---|---|
Raw material comprehensive composition and cost | Original main material |
accessory material | |
Fuel and power costs | solid fuel |
Energy media | |
cost of production | Fixed equipment damage and environmental protection costs |
Controlled consumables and maintenance costs | |
Employee compensation affected by production volume | |
Powder rate influence | Price and performance |
The alkali metal, and the negative effects | Price and product performance |
Equipment carrying capacity |
Scheme | Mineral Powder 1 | Mineral Powder 2 | Mineral Powder 3 | Mineral Powder 4 | Mining Powder 5 | Mining Powder 6 | Mineral Powder 7 | Mineral Powder 8 | Mine Powder 9 | Mineral Powder 10 | The Others |
---|---|---|---|---|---|---|---|---|---|---|---|
Before the dressing | 22.48 | 3.88 | 20.15 | 4.65 | 6.98 | 6.98 | 9.30 | 1.80 | 3.20 | 3.10 | 17.50 |
After the dressing | 22.18 | 3.89 | 20.23 | 4.67 | 7.00 | 7.00 | 9.34 | 1.81 | 3.21 | 3.11 | 17.57 |
Scheme | TFe | CaO | MgO | SiO2 | TiO2 | Al2O3 | P | Mn | Na2O | K2O | Zn | S | V2O5 |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Before the dressing | 53.25 | 11.43 | 2.92 | 6.29 | 0.41 | 2.75 | 0.0649 | 0.4879 | 0.0820 | 0.0775 | 0.0092 | 0.060 | 0.090 |
After the dressing | 53.10 | 11.46 | 2.93 | 6.29 | 0.41 | 2.74 | 0.0650 | 0.4852 | 0.0821 | 0.0775 | 0.0092 | 0.060 | 0.101 |
CaO | MgO | SiO2 | TiO2 | Al2O3 | P | Mn | Na2O | K2O | Zn | S | V2O5 | |
---|---|---|---|---|---|---|---|---|---|---|---|---|
Mineral powder 1 | −0.97066 | −0.89448 | −0.95274 | −0.27248 | −0.89135 | 3.61644 | −0.38733 | 2.65449 | 2.86947 | 0.00001 | 0.011 | 0.011 |
Mineral powder 2 | −0.97121 | −0.89494 | −0.95444 | −0.27235 | −0.89041 | 3.62297 | −0.38502 | 2.65344 | 2.86396 | 0.00001 | 0.006 | 0.008 |
Mineral powder 3 | −0.97066 | −0.89444 | −0.95174 | −0.27229 | −0.89173 | 3.63016 | −0.38410 | 2.65397 | 2.86303 | 0.00001 | 0.008 | 0.012 |
Mineral powder 4 | −0.97116 | −0.89493 | −0.95347 | −0.27246 | −0.89074 | 3.61664 | −0.38696 | 2.65616 | 2.86936 | 0.00001 | 0.006 | 0.014 |
Mining powder 5 | −0.97098 | −0.89521 | −0.95142 | −0.27479 | −0.88956 | 3.60947 | −0.38392 | 2.66428 | 2.88015 | 0.00001 | 0.007 | 0.007 |
Mining powder 6 | −0.97466 | −0.89761 | −0.95258 | −0.27330 | −0.89081 | 3.62086 | −0.38469 | 2.66288 | 2.87497 | 0.00001 | 0.004 | 0.010 |
Mineral powder 7 | −0.99654 | −0.89364 | −0.95040 | −0.27203 | −0.88708 | 3.60594 | −0.38412 | 2.64744 | 2.85967 | 0.00001 | 0.006 | 0.012 |
Mineral powder 8 | −0.96999 | −0.94617 | −0.95161 | −0.27280 | −0.88879 | 3.61330 | −0.38440 | 2.65255 | 2.86519 | 0.00001 | 0.009 | 0.008 |
Mine powder 9 | −0.97904 | −0.91616 | −0.95155 | −0.27275 | −0.89069 | 3.61259 | −0.38432 | 2.65205 | 2.86463 | 0.00001 | 0.010 | 0.009 |
Mineral powder 10 | −0.98394 | −0.89454 | −0.95165 | −0.27254 | −0.88873 | 3.61269 | −0.38438 | 2.65233 | 2.86501 | 0.00001 | 0.005 | 0.013 |
Scheme | Mineral Powder 1 | Mineral Powder 2 | Mineral Powder 3 | Mineral Powder 4 | Mining Powder 5 | Mining Powder 6 | Mineral Powder 7 | Mineral Powder 8 | Mine Powder 9 | Mineral Powder 10 | Mineral Powder 11 | Mineral Powder 12 | The Others |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Before the dressing | 3.94 | 11.81 | 14.17 | 22.82 | 0 | 3.94 | 5.51 | 3.94 | 8.66 | 5.00 | 3.70 | 6.80 | 9.71 |
After the dressing | 4.01 | 12.02 | 14.42 | 23.23 | 5.61 | 4.01 | 4.01 | 0 | 8.81 | 7.30 | 3.70 | 3.20 | 9.68 |
Scheme | TFe | CaO | MgO | SiO2 | TiO2 | Al2O3 | P | Mn | Na2O | K2O | Zn | S | V2O5 |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|
Before the dressing | 53.61 | 11.23 | 2.66 | 6.15 | 0.3536 | 2.48 | 0.0625 | 0.4054 | 0.0671 | 0.0931 | 0.0115 | 0.078 | 0.100 |
After the dressing | 53.60 | 11.23 | 2.61 | 6.17 | 0.2948 | 2.50 | 0.0668 | 0.4083 | 0.0592 | 0.0844 | 0.0101 | 0.071 | 0.093 |
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Feng, S.; Wang, B.; Zhou, Z.; Xue, T.; Yang, A.; Li, Y. Research on Multi-Decision Sinter Composition Optimization Based on OLS Algorithm. Metals 2023, 13, 548. https://doi.org/10.3390/met13030548
Feng S, Wang B, Zhou Z, Xue T, Yang A, Li Y. Research on Multi-Decision Sinter Composition Optimization Based on OLS Algorithm. Metals. 2023; 13(3):548. https://doi.org/10.3390/met13030548
Chicago/Turabian StyleFeng, Shilong, Bin Wang, Zixing Zhou, Tao Xue, Aimin Yang, and Yifan Li. 2023. "Research on Multi-Decision Sinter Composition Optimization Based on OLS Algorithm" Metals 13, no. 3: 548. https://doi.org/10.3390/met13030548
APA StyleFeng, S., Wang, B., Zhou, Z., Xue, T., Yang, A., & Li, Y. (2023). Research on Multi-Decision Sinter Composition Optimization Based on OLS Algorithm. Metals, 13(3), 548. https://doi.org/10.3390/met13030548