Virtual Sensing of Key Variables in the Hydrogen Production Process: A Comparative Study of Data-Driven Models
Abstract
:1. Introduction
- (1)
- The developed DVBPCA considers both process dynamics and transportation delays of energies and materials. Concretely, the finite impulse response (FIR) method is employed to model the dynamics of the hydrogen production process. And the transportation delays related to the EVs are automatically determined by differential evolution (DE). Moreover, the DVBPCA is able to make full use of the correlations between KVs for performance enhancement.
- (2)
- The moving window (MW) approach is employed for updating the DVBPCA with the latest online process information, which effectively captures the time-varying characteristics of the hydrogen production process in real-time.
- (3)
- A comparative study of data-driven virtual sensors is implemented for the hydrogen production process, which is sparsely mentioned in the predecessors’ research. Furthermore, the performance of the developed MW-DVBPCA is verified by the real-life natural gas steam reforming hydrogen production process.
2. Variational Inference
3. Dynamic Variational Bayesian Principal Component Analysis Based on Moving Window
3.1. Time-Delayed Moving Average Model
3.2. Dynamic Variational Bayesian Principal Component Analysis
Algorithm 1 Pseudocode for the DVBPCA. |
|
3.3. Moving Window-Based Dynamic Variational Bayesian Principal Component Analysis
3.4. Differential Evolutionary-Based Model Selection
4. Case Studies and Comparisons
4.1. Natural Gas Steam Reforming Hydrogen Production Process
4.2. Explanatory Variable Selection and Data Collection
4.3. Evaluation Metrics
4.4. Parameter Selection
4.5. Results and Analysis
4.6. Computational Efficiency Analysis
5. Conclusions and Outlook
- Robust methods. The probabilistic model in this article is based on the traditional Gaussian distribution assumption, which is susceptible to outliers. Therefore, the training set must be cleaned to remove outliers. However, some outliers are indistinctive and challenging to detect and remove. To this end, finding a probability distribution insensitive to the noise and outliers can help improve the generalization performance of predictive models. Typically, Student’s t distribution with heavier tails is a candidate choice. As a result, designing a robust virtual sensor based on Student’s t distribution is worth investigating.
- Data-driven approaches fused with process knowledge. In fact, the states (or the hidden variables) of the system are influenced by variables characterizing materials and energies fed into the process. Conventional virtual sensors take all observed variables as inputs and the KVs as outputs, which makes it difficult to describe the true causality between variables of the hydrogen production process, weakening the interpretability and generalization abilities. A causal virtual sensor can better reflect the process mechanism and thus estimate the KVs more accurately. Therefore, equipping the MW-DVBPCA model with the causality of process variables of the hydrogen production process is desirable.
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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EV | Description |
---|---|
U1 | Flow of fuel natural gas into primary reformer |
U2 | Flow of fuel off gas into primary reformer |
U3 | Pressure of fuel off gas at the exit of heat exchanger 3 |
U4 | Pressure of furnace flue gas at primary reformer’s exit |
U5 | Temperature of fuel off gas at the exit of heat exchanger 3 |
U6 | Temperature of fuel natural gas at pre-heater’s exit |
U7 | Temperature of process gas at primary reformer’s entrance |
U8 | Temperature of furnace flue gas at primary reformer’s top left |
U9 | Temperature of furnace flue gas at primary reformer’s top right |
U10 | Temperature of mixed furnace flue gas at primary reformer’s top |
U11 | Temperature of transformed gas at primary reformer’s left exit |
U12 | Temperature of transformed gas at primary reformer’s right exit |
U13 | Temperature of transformed gas at primary reformer’s exit |
RMSE | MAE | RMSE | MAE | ||||
---|---|---|---|---|---|---|---|
➀ | PLS | 0.1915 | −0.1329 | 0.1643 | 0.1944 | −0.0975 | 0.1483 |
VBPCA | 0.2061 | −0.2566 | 0.1703 | 0.2054 | −0.2259 | 0.1592 | |
LSTM | 0.1567 | 0.2733 | 0.1373 | 0.1351 | 0.5370 | 0.1080 | |
ESN | 0.1150 | 0.6088 | 0.0965 | 0.1148 | 0.6173 | 0.0968 | |
DPLS | 0.0942 | 0.7373 | 0.0770 | 0.0956 | 0.7348 | 0.0764 | |
DVBPCA | 0.0827 | 0.7975 | 0.0704 | 0.0826 | 0.8018 | 0.0662 | |
MW-DVBPCA | 0.0525 | 0.9186 | 0.0388 | 0.0709 | 0.8538 | 0.0533 | |
➁ | PLS | 0.1348 | 0.4623 | 0.1077 | 0.1352 | 0.4687 | 0.1067 |
VBPCA | 0.1339 | 0.4694 | 0.1092 | 0.1315 | 0.4976 | 0.1052 | |
LSTM | 0.1227 | 0.5543 | 0.1051 | 0.0829 | 0.8128 | 0.0606 | |
ESN | 0.0955 | 0.7301 | 0.0759 | 0.0912 | 0.7582 | 0.0730 | |
DPLS | 0.0777 | 0.8215 | 0.0647 | 0.0732 | 0.8444 | 0.0587 | |
DVBPCA | 0.0673 | 0.8659 | 0.0536 | 0.0719 | 0.8497 | 0.0574 | |
MW-DVBPCA | 0.0511 | 0.9228 | 0.0368 | 0.0665 | 0.8717 | 0.0515 |
RMSE | MAE | RMSE | MAE | ||||
---|---|---|---|---|---|---|---|
➀ | PLS | 0.1930 | 0.0095 | 0.1536 | 0.1882 | −0.0729 | 0.1612 |
VBPCA | 0.1913 | 0.0264 | 0.1521 | 0.1973 | −0.1792 | 0.1660 | |
LSTM | 0.1562 | 0.3949 | 0.1293 | 0.1302 | 0.4863 | 0.1118 | |
ESN | 0.1152 | 0.6471 | 0.0946 | 0.1057 | 0.6616 | 0.0895 | |
DPLS | 0.1346 | 0.5185 | 0.1099 | 0.0955 | 0.7237 | 0.0779 | |
DVBPCA | 0.1145 | 0.6514 | 0.0906 | 0.0796 | 0.8080 | 0.0676 | |
MW-DVBPCA | 0.1103 | 0.6765 | 0.0858 | 0.0548 | 0.9090 | 0.0425 | |
➁ | PLS | 0.1724 | 0.2094 | 0.1400 | 0.1320 | 0.4722 | 0.1090 |
VBPCA | 0.1648 | 0.2777 | 0.1361 | 0.1289 | 0.4964 | 0.1065 | |
LSTM | 0.1352 | 0.5137 | 0.1094 | 0.1292 | 0.4943 | 0.1015 | |
ESN | 0.1230 | 0.5978 | 0.1007 | 0.0823 | 0.7948 | 0.0678 | |
DPLS | 0.1156 | 0.6448 | 0.0934 | 0.0790 | 0.8107 | 0.0669 | |
DVBPCA | 0.1119 | 0.6670 | 0.0859 | 0.0752 | 0.8285 | 0.0605 | |
MW-DVBPCA | 0.1056 | 0.7036 | 0.0835 | 0.0531 | 0.9146 | 0.0403 |
KV | Hypothesis | Decision | |
---|---|---|---|
concentration | |||
concentration | |||
concentration | |||
concentration | |||
PLS | 3.44 | <0.01 |
VBPCA | 11.49 | <0.01 |
LSTM | 3893.01 | 0.04 |
ESN | 264.38 | <0.01 |
DPLS | 255.83 | <0.01 |
DVBPCA | 210.16 | <0.01 |
MW-DVBPCA | 1877.91 | 0.06 |
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Yao, Y.; Xing, Y.; Zuo, Z.; Wei, C.; Shao, W. Virtual Sensing of Key Variables in the Hydrogen Production Process: A Comparative Study of Data-Driven Models. Sensors 2024, 24, 3143. https://doi.org/10.3390/s24103143
Yao Y, Xing Y, Zuo Z, Wei C, Shao W. Virtual Sensing of Key Variables in the Hydrogen Production Process: A Comparative Study of Data-Driven Models. Sensors. 2024; 24(10):3143. https://doi.org/10.3390/s24103143
Chicago/Turabian StyleYao, Yating, Yupeng Xing, Ziteng Zuo, Chihang Wei, and Weiming Shao. 2024. "Virtual Sensing of Key Variables in the Hydrogen Production Process: A Comparative Study of Data-Driven Models" Sensors 24, no. 10: 3143. https://doi.org/10.3390/s24103143
APA StyleYao, Y., Xing, Y., Zuo, Z., Wei, C., & Shao, W. (2024). Virtual Sensing of Key Variables in the Hydrogen Production Process: A Comparative Study of Data-Driven Models. Sensors, 24(10), 3143. https://doi.org/10.3390/s24103143