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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2024, Vol. 18 Issue (4): 42   https://doi.org/10.1007/s11705-024-2403-7
  本期目录
A hybrid spatial-temporal deep learning prediction model of industrial methanol-to-olefins process
Jibin Zhou1, Xue Li1, Duiping Liu2, Feng Wang3, Tao Zhang1(), Mao Ye1(), Zhongmin Liu1
1. National Engineering Research Center of Lower-Carbon Catalysis Technology, Dalian Institute of Chemical Physics, Chinese Academy of Sciences, Dalian 116023, China
2. Yulin Innovation Institute for Clean Energy, Clean Energy Innovation Institute of Chinese Academy of Sciences, Yulin 719053, China
3. Xuelang Industrial Intelligence Technology Co., Ltd., Wuxi 214000, China
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Abstract

Methanol-to-olefins, as a promising non-oil pathway for the synthesis of light olefins, has been successfully industrialized. The accurate prediction of process variables can yield significant benefits for advanced process control and optimization. The challenge of this task is underscored by the failure of traditional methods in capturing the complex characteristics of industrial processes, such as high nonlinearities, dynamics, and data distribution shift caused by diverse operating conditions. In this paper, we propose a novel hybrid spatial-temporal deep learning prediction model to address these issues. Firstly, a unique data normalization technique called reversible instance normalization is employed to solve the problem of different data distributions. Subsequently, convolutional neural network integrated with the self-attention mechanism are utilized to extract the temporal patterns. Meanwhile, a multi-graph convolutional network is leveraged to model the spatial interactions. Afterward, the extracted temporal and spatial features are fused as input into a fully connected neural network to complete the prediction. Finally, the outputs are denormalized to obtain the ultimate results. The monitoring results of the dynamic trends of process variables in an actual industrial methanol-to-olefins process demonstrate that our model not only achieves superior prediction performance but also can reveal complex spatial-temporal relationships using the learned attention matrices and adjacency matrices, making the model more interpretable. Lastly, this model is deployed onto an end-to-end Industrial Internet Platform, which achieves effective practical results.

Key wordsmethanol-to-olefins    process variables prediction    spatial-temporal    self-attention mechanism    graph convolutional network
收稿日期: 2023-11-01      出版日期: 2024-03-15
Corresponding Author(s): Tao Zhang,Mao Ye   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2024, 18(4): 42.
Jibin Zhou, Xue Li, Duiping Liu, Feng Wang, Tao Zhang, Mao Ye, Zhongmin Liu. A hybrid spatial-temporal deep learning prediction model of industrial methanol-to-olefins process. Front. Chem. Sci. Eng., 2024, 18(4): 42.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-024-2403-7
https://academic.hep.com.cn/fcse/CN/Y2024/V18/I4/42
Fig.1  
Fig.2  
Variables Description Unit Variables Description Unit
FI1401B Methanol feed t·h−1 TIC1101 Reactor temperature °C
TI1111 Dilute phase temperature of the reactor °C PI1101D Reactor pressure MPa
WI1102 Catalyst inventory in the reactor t WIC1101 Catalyst density in the reactor t
DI1105A Catalyst density of the dense phase in the reactor kg·m−3 TI1134A Regenerator temperature °C
PIC1110 Regenerator pressure MPa WI1105 Catalyst inventory in the regenerator t
WZ1101 Catalyst inventory in the reactor and regenerator t FIC1104B Upper stripping steam feed Nm3·h−1
FIC1105B Lower stripping steam feed Nm3·h−1 FIC1113B Steam delivery feed Nm3·h−1
ZI1102 Value of slide valve of regenerated catalysts % DI1106 Regenerated catalyst density kg·m−3
TI1119 Regenerated catalyst temperature °C TI1135B Lower stripping temperature °C
FIC1121A Air feed Nm3·h−1 FIC1001 C4 feed kg·h−1
FIC1103 Nitrogen feed Nm3·h−1 Q_PDI1113 Catalyst circulation rate t·h
PDI1113 Pressure drop of the slide valve of regenerated catalysts kPa PDI1106 Pressure drop of the standby valve of coked catalysts kPa
AI1603G Ethylene yield % AI1603I Propylene yield %
Tab.1  
Fig.3  
Models Horizon = 1 (2 h) Horizon = 3 (6 h) Horizon = 5 (10 h)
MAE MAPE MAE MAPE MAE MAPE
Classical VAR 15.25 1.21% 88.37 0.29% 96.63 4.09%
LSTM 24.39 1.40% 27.57 0.23% 37.70 2.98%
GRU 12.94 0.94% 23.35 0.15% 22.96 2.08%
Attention DSANet 6.65 0.54% 9.32 0.62% 10.73 0.75%
LSTNet 7.67 0.62% 10.08 0.70% 11.85 0.85%
Graph Graph WaveNet 8.31 0.70% 13.36 0.85% 16.53 1.19%
STGCN 7.91 0.81% 11.27 0.86% 12.97 1.10%
MTGNN 7.25 0.71% 10.93 0.79% 11.85 0.87%
This work CSA-MGCN 6.33 0.49% 9.10 0.58% 10.28 0.66%
Improvements +4.83% +8.13% +2.41% +7.05% +4.20% +11.23%
Tab.2  
Fig.4  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
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