CIESC Journal ›› 2023, Vol. 74 ›› Issue (10): 4218-4228.DOI: 10.11949/0438-1157.20230707
• Process system engineering • Previous Articles Next Articles
Shuaihang JI1,3(), Jinjiang WANG1,2,3(), Rui CAI1,3, Xuehao SUN2,3, Weifeng GE4
Received:
2023-07-07
Revised:
2023-09-10
Online:
2023-12-22
Published:
2023-10-25
Contact:
Jinjiang WANG
籍帅航1,3(), 王金江1,2,3(), 蔡睿1,3, 孙雪皓2,3, 葛伟凤4
通讯作者:
王金江
作者简介:
籍帅航(1999—),男,博士研究生,jishh@student.cup.edu.cn
基金资助:
CLC Number:
Shuaihang JI, Jinjiang WANG, Rui CAI, Xuehao SUN, Weifeng GE. Research on reduced order modeling and intelligent sensing method for heat exchangers driven by digital twin[J]. CIESC Journal, 2023, 74(10): 4218-4228.
籍帅航, 王金江, 蔡睿, 孙雪皓, 葛伟凤. 数字孪生驱动的热交换器降阶建模及智能感知方法研究[J]. 化工学报, 2023, 74(10): 4218-4228.
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参数 | 数值 | 参数 | 数值 |
---|---|---|---|
壳体内径/m | 0.160 | 铝密度/(kg/m3) | 2719 |
壳体厚度/m | 0.01 | 铝比热容/(J/(kg·℃)) | 871 |
换热面积/m2 | 0.78 | 铝热导率/(W/(m·℃)) | 202.4 |
换热管长/m | 1 | 液态水密度/(kg/m3) | 998.2 |
换热管外径/m | 0.012 | 液态水比热容/(J/(kg·℃)) | 4182 |
换热管壁厚/m | 0.0016 | 液态水热导率/(W/(m·℃)) | 0.6 |
换热管排列方式 | 正三角形 | 液态水动力黏度/(Pa·s) | 0.001003 |
换热管数量 | 26 | 碳酸钙密度/(kg/m3) | 2800 |
折流板数量 | 3 | 碳酸钙比热容/(J/(kg·℃)) | 856 |
碳酸钙热导率/(W/(m·℃)) | 2.25 |
Table 1 Structural parameter and physical property parameters
参数 | 数值 | 参数 | 数值 |
---|---|---|---|
壳体内径/m | 0.160 | 铝密度/(kg/m3) | 2719 |
壳体厚度/m | 0.01 | 铝比热容/(J/(kg·℃)) | 871 |
换热面积/m2 | 0.78 | 铝热导率/(W/(m·℃)) | 202.4 |
换热管长/m | 1 | 液态水密度/(kg/m3) | 998.2 |
换热管外径/m | 0.012 | 液态水比热容/(J/(kg·℃)) | 4182 |
换热管壁厚/m | 0.0016 | 液态水热导率/(W/(m·℃)) | 0.6 |
换热管排列方式 | 正三角形 | 液态水动力黏度/(Pa·s) | 0.001003 |
换热管数量 | 26 | 碳酸钙密度/(kg/m3) | 2800 |
折流板数量 | 3 | 碳酸钙比热容/(J/(kg·℃)) | 856 |
碳酸钙热导率/(W/(m·℃)) | 2.25 |
项目 | 入口温度/℃ | 入口压力/MPa | 流量/(m3/h) | 介质 |
---|---|---|---|---|
管程 | 60 | 0.1 | 0.8 | 水 |
壳程 | 25 | 0.1 | 0.5 | 水 |
Table 2 Heat exchanger simulation conditions settings
项目 | 入口温度/℃ | 入口压力/MPa | 流量/(m3/h) | 介质 |
---|---|---|---|---|
管程 | 60 | 0.1 | 0.8 | 水 |
壳程 | 25 | 0.1 | 0.5 | 水 |
采样方法 | 构建快照 时间/s | 模型训练 时间/s | 模型推理 时间/s | MAPE |
---|---|---|---|---|
不使用采样 | 4.2087 | 0.0656 | 0.0010 | 0.0425 |
LHS | 136.6628 | 0.0330 | 0.0010 | 0.0430 |
RS | 3.8994 | 0.0337 | 0.0010 | 0.2585 |
PAS | 3.9554 | 0.0331 | 0.0010 | 0.0408 |
Table 3 Model performance comparison of reduced order models
采样方法 | 构建快照 时间/s | 模型训练 时间/s | 模型推理 时间/s | MAPE |
---|---|---|---|---|
不使用采样 | 4.2087 | 0.0656 | 0.0010 | 0.0425 |
LHS | 136.6628 | 0.0330 | 0.0010 | 0.0430 |
RS | 3.8994 | 0.0337 | 0.0010 | 0.2585 |
PAS | 3.9554 | 0.0331 | 0.0010 | 0.0408 |
序号 | 奇异值 | 奇异值累计值占比/% |
---|---|---|
1 | 3.4356×10-3 | 99.25 |
2 | 2.3597×10-5 | 99.94 |
3 | 1.9781×10-6 | 99.99 |
4 | 1.2714×10-7 | 99.99 |
Table 4 Percentage of cumulative values of singular values
序号 | 奇异值 | 奇异值累计值占比/% |
---|---|---|
1 | 3.4356×10-3 | 99.25 |
2 | 2.3597×10-5 | 99.94 |
3 | 1.9781×10-6 | 99.99 |
4 | 1.2714×10-7 | 99.99 |
工况 | 实际厚度/mm | 预测厚度/mm | 相对误差/% |
---|---|---|---|
1 | 1.794 | 1.736 | 3.23 |
2 | 1.347 | 1.394 | 3.48 |
3 | 0.824 | 0.867 | 5.21 |
4 | 0.198 | 0.185 | 6.57 |
Table 5 Prediction results of fouling thickness in heat exchangers based on BP model
工况 | 实际厚度/mm | 预测厚度/mm | 相对误差/% |
---|---|---|---|
1 | 1.794 | 1.736 | 3.23 |
2 | 1.347 | 1.394 | 3.48 |
3 | 0.824 | 0.867 | 5.21 |
4 | 0.198 | 0.185 | 6.57 |
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