4.1. Prototype Experiments
To simulate the working conditions of pulverized coal flow, we constructed an air-coal loop setup [
28]. This setup, depicted in
Figure 5, was designed as a prototype system to investigate the interaction between microwave signals and pulverized coal. The setup is supported by an aluminum alloy frame, with the microwave sensor mounted at the center of the left steel pipe via a flange. The air-coal loop setup facilitates the circulation of pulverized coal using an industrial fan. A centrifugal fan with a power rating of 750 W and a nominal flow rate of 1810 m
3/h serves as the power source for air circulation. Under this configuration, the internal flow velocity of the setup can reach up to 28.4 m/s, meeting the actual flow velocity requirements of 20-30 m/s.
The microwave signal was swept from 0.55 to 3 GHz in steps of 0.025 GHz. For the full-path S
21 data with a PCC of 0.8 kg/kg, the L1 distance metric was utilized for calculation, which can be expressed as follows:
where
is the S
21 data under pulverized coal-air mixture conditions,
is the S
21 data under pure air conditions, and
is the signal path index.
The results are presented in
Figure 6(a). It can be concluded that, under this specific condition, the microwave signal at approximately 1.25 GHz exhibits the peak L1 distance metric, indicating that microwave signals near this frequency band experience the strongest attenuation after passing through the pulverized coal flow. Therefore, with consistent hardware and measurement environments, it is evident that selecting the appropriate working frequency is crucial for obtaining accurate measurement results.
After determining the optimal working frequency, we collected full-path S
21 data at PCC of 0.2, 0.5, and 0.8 kg/kg, respectively, and calculated their L1 distances. Using the SVM model, successful classification was achieved. The confusion matrix, presented in
Figure 7, demonstrates that the majority of predicted values were accurately classified, thereby validating the effectiveness of the prototype design and methodology for microwave measurement of PCC.
4.2. Field Experiments
The coal-fired unit typically utilizes a direct-firing pulverizing system. Raw coal is transported from the coal bunker to the coal feeder via a conveyor belt. Subsequently, the raw coal is fed into the coal mill in a controlled, continuous, and adjustable manner for pulverization. The pulverized coal is then conveyed to the boiler through the coal pipeline with the aid of heated primary air for combustion.
After preliminary certification of the prototype experiments, we conducted tests directly in the coal-fired units at the power plant to evaluate the system's performance under field conditions. The multi-frequency microwave sensing system was installed on the coal pipelines of several coal mills. As shown in
Figure 8, the outcomes of the installation are illustrated.
Currently, there is no consensus on methods for measuring the concentration of gas-solid two-phase flows, which complicates the direct determination of absolute concentrations. Consequently, during the experiments, we monitored both the primary air flow rate of the coal mill and the coal quantity from the coal feeder, as recorded by the DCS system. PCC at each moment was calculated using the following formula:
where
is the coal quantity from the coal feeder,
is the primary air flow volume, and
is the primary air flow rate.
After integrating the system into the field environment, adjustments were made to factors such as sensor size and fabrication materials to better suit the conditions, as detailed in Table 3. The ability to identify an appropriate working frequency range for the scenario significantly influences the measurement results.
Table 3.
Sensor specifications for different experimental scenarios.
Table 3.
Sensor specifications for different experimental scenarios.
Experiments Scenario |
Sensor Diameter(mm) |
Outer Wall Material |
Substrate Layer Material |
Prototype Experiments |
150 |
Aluminium |
Epoxy Resin |
Field Experiments |
508 |
Carbon Steel |
PTFE |
A frequency sweep was conducted across the range of 0.55 to 3 GHz. The L1 distance metric was used to assess signal attenuation at each frequency through the pulverized coal flow, with the results presented in
Figure 6(b). The results clearly indicate that microwave signals experience the greatest attenuation within the frequency range of 1.2 to 1.5 GHz. This suggests higher sensitivity to pulverized coal within this range, which provides a basis for subsequent frequency selection.
To address redundant information in excess frequencies and the non-linear relationship between S
21 parameters and solid phase concentration, a frequency selection method based on principal component analysis (PCA) and orthogonal matching pursuit (OMP) [
27] was employed. By varying the voltage from 0 to 10 V in increments of 0.1 V using a VCO during each acquisition, extensive frequency domain information was collected. Additionally, signal path switching is managed by a high-speed microwave signal routing module, resulting in a comprehensive 240-dimensional dataset across 101 frequencies, which forms the raw data matrix. Eigenvalue decomposition is performed for each frequency to derive multiple eigenvectors and their explained variances. We ensure that the eigenvectors for each frequency retain more than 80% of the information content from the raw data matrix, i.e., the cumulative explained variance exceeds 80%. As illustrated in
Figure 9(a), the number of eigenvectors k is generally below 24 for most frequencies, demonstrating that PCA effectively reduces the dimensionality of high-dimensional full-path data. The cumulative explained variance is plotted for frequencies corresponding to eigenvector counts of k = 3 and k = 23, respectively. As shown in
Figure 9(b), when k is smaller, each eigenvector contains more information, allowing for the characterization of the original dataset with less data. This effectively reduces computational requirements.
After applying PCA, 25 frequencies with k≤3 are selected, resulting in a dataset comprising 45 sets of eigenvectors. Subsequently, OMP is used to select the optimal subset of these eigenvectors. The distribution of eigenvectors across various sizes of frequency combinations is illustrated in
Figure 10. It is evident that these eigenvectors exhibit clustering in specific frequency bands, suggesting that measurements in these bands more effectively represent the actual value.
The mean absolute error (MAE) and correlation coefficient between the predicted and the actual values for various sizes of frequency combinations are shown in
Figure 11(a). As the size of the frequency combination increases, the MAE decreases while the correlation coefficient increases. This trend indicates that incorporating more eigenvectors improves the accuracy of the predictions. However, beyond a certain point, both the MAE and correlation coefficient tend to stabilize, suggesting that some eigenvectors become redundant and have minimal impact on the prediction results.
Based on the results of the OMP calculations, we can determine the optimal size N of the frequency combination S by identifying the point at which both the MAE and the correlation coefficient stabilize. Considering both the OMP results and the efficiency of data collection and processing, we concluded that N=16.
Figure 11(b) presents a preliminary comparison of prediction results from two stages of the frequency selection method: using PCA alone versus integrating PCA with OMP. After normalizing these predictions through min-max normalization, we visualized their distances from the actual values. The predictions from PCA combined with OMP are closer to the actual values. Error analysis reveals that the MAE for PCA alone can be as low as 7%, whereas the PCA+OMP method achieves a MAE of 3.8%. This demonstrates that combining PCA with OMP effectively integrates multi-frequency information, thereby improving prediction accuracy.
We conducted on-site monitoring of the C# coal mill, as illustrated in
Figure 12, which displays the predicted results from our frequency selection method alongside the actual PCC data. This comparison indicates that the system effectively captures the trend of PCC variations within the 0 to 0.5 kg/kg range. We have highlighted several notable regions with circles and included an enlarged view of these areas. In these marked regions, the slopes of the predicted values closely align with those of the actual measurements. Even when the conveying of pulverized coal ceases and PCC approaches zero, the multi-frequency microwave sensing system continues to detect changes promptly. Error analysis reveals a MAE of 2.1%, demonstrating the system’s effectiveness and reliability.
Identical tests were conducted on various coal mills within the same unit to evaluate the reproducibility of the proposed method. The results, shown in
Figure 13, indicate that the system effectively estimates PCC within the typical range of 0.3 to 0.5 kg/kg, which is commonly observed in power plants. A comparison of these estimates with the PCC data provided by the DCS system reveals that the predicted results closely align with the actual values in terms of trends. Furthermore, at points with more pronounced slopes, the predicted and actual values exhibit simultaneous peaks and troughs, further confirming the system's accuracy.
A numerical analysis of the experimental results was conducted, focusing on error and correlation. As shown in Table 3, the MAE for nearly all coal mills did not exceed 2.1%, with the best result reaching 1.41%. This indicates a high level of consistency between predicted and actual values, thereby validating the repeatability and effectiveness of the multi-frequency microwave sensing system. Furthermore, it was observed that the amplitude of changes in PCC is positively correlated with the correlation coefficient. This suggests that when amplitude changes are substantial, measurement errors in the system are negligible, resulting in an increased correlation coefficient. Conversely, when amplitude changes are minor, the relative error increases, and the effects of amplitude changes on the results become less pronounced, leading to a decrease in the correlation coefficient. Thus, the system can achieve higher measurement accuracy under conditions of significant PCC variation, thereby maintaining the accuracy and reliability of predictions in dynamic environments.
Table 3.
Numerical analysis of test results on different coal mills.
Table 3.
Numerical analysis of test results on different coal mills.
|
A# |
B# |
C# |
D# |
E# |
Mean Absolute Error(%) |
1.46 |
1.58 |
2.07 |
1.41 |
1.55 |
Correlation coefficient |
0.57 |
0.31 |
0.98 |
0.85 |
0.66 |