CIESC Journal ›› 2019, Vol. 70 ›› Issue (2): 607-616.DOI: 10.11949/j.issn.0438-1157.20181343
• Process system engineering • Previous Articles Next Articles
Yongfei XUE1(
),Yalin WANG1(
),Bei SUN1,Qianzhong LI2,Jiazhou SUN1
Received:2018-11-15
Revised:2018-11-21
Online:2019-02-05
Published:2019-02-05
Contact:
Yalin WANG
通讯作者:
王雅琳
作者简介:<named-content content-type="corresp-name">薛永飞</named-content>(1988—),男,博士研究生,<email>xueyongfei@csu.edu.cn</email>|王雅琳(1973—),女,博士,教授,<email>ylwang@csu.edu.cn</email>
基金资助:CLC Number:
Yongfei XUE, Yalin WANG, Bei SUN, Qianzhong LI, Jiazhou SUN. Improved state transfer algorithm-based kinetics parameter estimation for cascaded plug flow reactors[J]. CIESC Journal, 2019, 70(2): 607-616.
薛永飞, 王雅琳, 孙备, 李钱钟, 孙家舟. 基于改进状态转移算法的串级平推流反应器动力学参数估计[J]. 化工学报, 2019, 70(2): 607-616.
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URL: https://hgxb.cip.com.cn/EN/10.11949/j.issn.0438-1157.20181343
| 物性名称 | 本文取值 |
|---|---|
| 第1反应器中混合物的比定压热容 | 3.14 kJ?kg-1?K-1 |
| 第2反应器中混合物的比定压热容 | 2.48 kJ?kg-1?K-1 |
| 第3反应器中混合物的比定压热容 | 2.47 kJ?kg-1?K-1 |
| 第4反应器中混合物的比定压热容 | 2.26 kJ?kg-1?K-1 |
| 反应器级间冷氢的比定压热容 | 14.32 kJ?kg-1?K-1 |
| 加氢裂化反应平均放热系数Hr | 418.4 kJ?kg-1 |
| 第1反应器中混合物的密度ρ1 | 905 kg·m-3 |
| 第2反应器中混合物的密度ρ2 | 833 kg·m-3 |
| 第3反应器中混合物的密度ρ3 | 809.8 kg·m-3 |
| 第4反应器中混合物的密度ρ4 | 737.1 kg·m-3 |
Table 1 Physical property data used for estimating kinetics parameters of hydrocracking
| 物性名称 | 本文取值 |
|---|---|
| 第1反应器中混合物的比定压热容 | 3.14 kJ?kg-1?K-1 |
| 第2反应器中混合物的比定压热容 | 2.48 kJ?kg-1?K-1 |
| 第3反应器中混合物的比定压热容 | 2.47 kJ?kg-1?K-1 |
| 第4反应器中混合物的比定压热容 | 2.26 kJ?kg-1?K-1 |
| 反应器级间冷氢的比定压热容 | 14.32 kJ?kg-1?K-1 |
| 加氢裂化反应平均放热系数Hr | 418.4 kJ?kg-1 |
| 第1反应器中混合物的密度ρ1 | 905 kg·m-3 |
| 第2反应器中混合物的密度ρ2 | 833 kg·m-3 |
| 第3反应器中混合物的密度ρ3 | 809.8 kg·m-3 |
| 第4反应器中混合物的密度ρ4 | 737.1 kg·m-3 |
| 反应速率常数 | 活化能Ei/(J·mol-1) | 指前因子ki0/s-1 |
|---|---|---|
| k1 | 95700.39 95700.39 95700.39 95700.39 95700.39 95700.39 | 4585.95 |
| k2 | 2383.74 | |
| k3 | 2373.56 | |
| k4 | 417.33 | |
| k5 | 39.32 | |
| k6 | 97199.38 97199.38 97199.38 97199.38 | 473.33 |
| k7 | 96.48 | |
| k8 | 2.65×10-5 | |
| k9 | 0 | |
| k10 | 63753.57 63753.57 63753.57 | 0.20 |
| k11 | 0 | |
| k12 | 9.92×10-3 | |
| k13 | 97292.32 97292.32 | 44.70 |
| k14 | 0 | |
| k15 | 8018.36 | 11.70×10-3 |
Table 2 Estimation results of kinetics parameters for hydrocracking reaction
| 反应速率常数 | 活化能Ei/(J·mol-1) | 指前因子ki0/s-1 |
|---|---|---|
| k1 | 95700.39 95700.39 95700.39 95700.39 95700.39 95700.39 | 4585.95 |
| k2 | 2383.74 | |
| k3 | 2373.56 | |
| k4 | 417.33 | |
| k5 | 39.32 | |
| k6 | 97199.38 97199.38 97199.38 97199.38 | 473.33 |
| k7 | 96.48 | |
| k8 | 2.65×10-5 | |
| k9 | 0 | |
| k10 | 63753.57 63753.57 63753.57 | 0.20 |
| k11 | 0 | |
| k12 | 9.92×10-3 | |
| k13 | 97292.32 97292.32 | 44.70 |
| k14 | 0 | |
| k15 | 8018.36 | 11.70×10-3 |
| 项目 | 标准STA | 改进STA (平均值) | 性能提升 (平均值)/% |
|---|---|---|---|
| 寻优迭代次数 | 200 | 41.7 | 79.15 |
| 计算总耗时/s | 30477.12 | 6215.60 | 79.61 |
| fitness调用耗时/s | 30378.39 | 6108.06 | 79.89 |
| ode15 s调用耗时/s | 30416.73 | 6199.97 | 79.62 |
| 项目 | 标准STA | 改进STA (平均值) | 性能提升 (平均值)/% |
|---|---|---|---|
| 寻优迭代次数 | 200 | 41.7 | 79.15 |
| 计算总耗时/s | 30477.12 | 6215.60 | 79.61 |
| fitness调用耗时/s | 30378.39 | 6108.06 | 79.89 |
| ode15 s调用耗时/s | 30416.73 | 6199.97 | 79.62 |
| 参数名称 | 取值 | 参数名称 | 取值 |
|---|---|---|---|
| 伸缩算子γ | 1 | 迭代次数iter | 2.0×102 |
| 旋转算子α | (1/2)iterαmax | 误差满意阈值ξ | 3.0×10-2 |
| 旋转算子初值αmax | 1 | 活化能Ei上限 | 1.3×105 |
| 旋转算子终值αmin | 1.0×10-3 | 活化能Ei下限 | 6.0×103 |
| 轴向算子δ | 1 | 指前因子ki0上限 | 7.0×103 |
| 平移算子β | 1 | 指前因子ki0下限 | 0 |
| 状态个数SE | 30 | 所求问题状态维数 | 20 |
Table 4 Parameters setting of improved STA
| 参数名称 | 取值 | 参数名称 | 取值 |
|---|---|---|---|
| 伸缩算子γ | 1 | 迭代次数iter | 2.0×102 |
| 旋转算子α | (1/2)iterαmax | 误差满意阈值ξ | 3.0×10-2 |
| 旋转算子初值αmax | 1 | 活化能Ei上限 | 1.3×105 |
| 旋转算子终值αmin | 1.0×10-3 | 活化能Ei下限 | 6.0×103 |
| 轴向算子δ | 1 | 指前因子ki0上限 | 7.0×103 |
| 平移算子β | 1 | 指前因子ki0下限 | 0 |
| 状态个数SE | 30 | 所求问题状态维数 | 20 |
| 预测项目 | 标准STA | 改进STA | ||
|---|---|---|---|---|
| MAE | MRE | MAE | MRE | |
| 尾油质量分数 | 0.001948 | 1.0627% | 0.002412 | 1.3155% |
| 柴油质量分数 | 0.001188 | 0.3069% | 0.001510 | 0.3899% |
| 航煤质量分数 | 0.000220 | 0.1089% | 0.000306 | 0.1513% |
| 重石质量分数 | 0.000455 | 0.2386% | 0.000629 | 0.3302% |
| 轻石质量分数 | 0.000260 | 1.6356% | 0.000339 | 2.1251% |
| 轻端质量分数 | 0.000280 | 1.3670% | 0.000378 | 1.8609% |
| 1反出口温度 | 0.076543 | 0.0113% | 0.111887 | 0.0166% |
| 2反出口温度 | 0.106760 | 0.0158% | 0.139421 | 0.0207% |
| 3反出口温度 | 0.109646 | 0.0162% | 0.143436 | 0.0212% |
| 4反出口温度 | 0.098496 | 0.0146% | 0.122468 | 0.0182% |
Table 5 Statistical error of 16 hydrocracking testing samples which are adjacent
| 预测项目 | 标准STA | 改进STA | ||
|---|---|---|---|---|
| MAE | MRE | MAE | MRE | |
| 尾油质量分数 | 0.001948 | 1.0627% | 0.002412 | 1.3155% |
| 柴油质量分数 | 0.001188 | 0.3069% | 0.001510 | 0.3899% |
| 航煤质量分数 | 0.000220 | 0.1089% | 0.000306 | 0.1513% |
| 重石质量分数 | 0.000455 | 0.2386% | 0.000629 | 0.3302% |
| 轻石质量分数 | 0.000260 | 1.6356% | 0.000339 | 2.1251% |
| 轻端质量分数 | 0.000280 | 1.3670% | 0.000378 | 1.8609% |
| 1反出口温度 | 0.076543 | 0.0113% | 0.111887 | 0.0166% |
| 2反出口温度 | 0.106760 | 0.0158% | 0.139421 | 0.0207% |
| 3反出口温度 | 0.109646 | 0.0162% | 0.143436 | 0.0212% |
| 4反出口温度 | 0.098496 | 0.0146% | 0.122468 | 0.0182% |
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