Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (4): 1742-1753.DOI: 10.16085/j.issn.1000-6613.2023-0706
• Energy processes and technology • Previous Articles
JIANG Chenguang(), ZHANG Shengzhen(), ZHANG Cuiqing, GUO Yi, SUN Yongwei
Received:
2023-04-28
Revised:
2023-07-10
Online:
2024-05-13
Published:
2024-04-15
Contact:
ZHANG Shengzhen
通讯作者:
张胜振
作者简介:
蒋晨光(1991—),女,博士,从事煤炭综合利用技术研究。E-mail: 20046490@ceic.com。
基金资助:
CLC Number:
JIANG Chenguang, ZHANG Shengzhen, ZHANG Cuiqing, GUO Yi, SUN Yongwei. Optimization of the preparation process of 52# Fischer-Tropsch wax based on DFSS method[J]. Chemical Industry and Engineering Progress, 2024, 43(4): 1742-1753.
蒋晨光, 张胜振, 张翠清, 郭屹, 孙永伟. 基于DFSS方法优化52#费托蜡的制备工艺[J]. 化工进展, 2024, 43(4): 1742-1753.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2023-0706
因子 | 代号 | 编码和水平 | ||||
---|---|---|---|---|---|---|
-1 | - | 0 | + | +1 | ||
剂油比 | X1 | 4.45 | 3.5 | 6.75 | 10 | 9.04 |
溶剂比 | X2 | 2.88 | 2 | 5 | 8 | 7.12 |
结晶时间/min | X3 | 2.19 | 0 | 7.5 | 15 | 12.80 |
降温速率/℃·min-1 | X4 | 5.48 | 5.3 | 5.9 | 6.5 | 6.32 |
结晶温度/℃ | X5 | 1.47 | 0 | 5 | 10 | 8.53 |
因子 | 代号 | 编码和水平 | ||||
---|---|---|---|---|---|---|
-1 | - | 0 | + | +1 | ||
剂油比 | X1 | 4.45 | 3.5 | 6.75 | 10 | 9.04 |
溶剂比 | X2 | 2.88 | 2 | 5 | 8 | 7.12 |
结晶时间/min | X3 | 2.19 | 0 | 7.5 | 15 | 12.80 |
降温速率/℃·min-1 | X4 | 5.48 | 5.3 | 5.9 | 6.5 | 6.32 |
结晶温度/℃ | X5 | 1.47 | 0 | 5 | 10 | 8.53 |
序号 | X1 | X2 | X3/min | X4/℃·min-1 | X5/℃ | 熔点/℃ | 含油量(质量分数)/% | 收率(质量分数)/% |
---|---|---|---|---|---|---|---|---|
1 | 6.75 | 5 | 12.80 | 5.9 | 5 | 51.75 | 0.606 | 18.48 |
2 | 9.04 | 5 | 7.5 | 5.9 | 5 | 53.08 | 0.6 | 18.12 |
3 | 10 | 8 | 15 | 5.3 | 10 | 52.47 | 2.2 | 21.04 |
4 | 3.5 | 2 | 0 | 6.5 | 10 | 58.85 | 0 | 2.24 |
5 | 10 | 8 | 0 | 5.3 | 0 | 49.14 | 1.388 | 38.96 |
6 | 3.5 | 8 | 15 | 6.5 | 10 | 50.92 | 3.565 | 23.66 |
7 | 3.5 | 8 | 0 | 6.5 | 0 | 50.51 | 1.912 | 27.28 |
8 | 3.5 | 8 | 0 | 5.3 | 10 | 50.56 | 2.165 | 28 |
9 | 6.75 | 7.12 | 7.5 | 5.9 | 5 | 50.49 | 1.123 | 26.06 |
10 | 6.75 | 5 | 7.5 | 5.48 | 5 | 51.39 | 0.993 | 26.4 |
11 | 3.5 | 2 | 15 | 5.3 | 10 | 54.82 | 0.847 | 11.5 |
12 | 3.5 | 2 | 15 | 6.5 | 0 | 52.11 | 0.898 | 22.94 |
13 | 6.75 | 5 | 7.5 | 5.9 | 5 | 52.03 | 0.548 | 24.86 |
14 | 4.45 | 5 | 7.5 | 5.9 | 5 | 51.29 | 0.77 | 27.82 |
15 | 6.75 | 5 | 7.5 | 5.9 | 1.47 | 50.65 | 0.615 | 30.64 |
16 | 6.75 | 5 | 7.5 | 6.32 | 5 | 52.63 | 0.877 | 25.56 |
17 | 10 | 2 | 0 | 5.3 | 10 | 60.01 | 0.678 | 3.6 |
18 | 6.75 | 5 | 2.19 | 5.9 | 5 | 53.35 | 0.545 | 19.56 |
19 | 6.75 | 5 | 7.5 | 5.9 | 5 | 51.71 | 0.546 | 22.78 |
20 | 10 | 2 | 15 | 5.3 | 0 | 52.87 | 0.384 | 19.68 |
21 | 6.75 | 5 | 7.5 | 5.9 | 5 | 52.17 | 0.656 | 24.22 |
22 | 10 | 8 | 15 | 6.5 | 0 | 50.21 | 0.1 | 33.74 |
23 | 10 | 8 | 0 | 6.5 | 10 | 57.04 | 1.558 | 7.18 |
24 | 6.75 | 5 | 7.5 | 5.9 | 8.53 | 53.53 | 0.89 | 20.76 |
25 | 10 | 2 | 0 | 6.5 | 0 | 57.27 | 0.91 | 6.06 |
26 | 3.5 | 2 | 0 | 5.3 | 0 | 51.85 | 0.576 | 24.6 |
27 | 10 | 2 | 15 | 6.5 | 10 | 60.94 | 0.067 | 2.5 |
28 | 6.75 | 2.88 | 7.5 | 5.9 | 5 | 53.46 | 0.255 | 15.1 |
29 | 3.5 | 8 | 15 | 5.3 | 0 | 46.83 | 1.424 | 46.44 |
序号 | X1 | X2 | X3/min | X4/℃·min-1 | X5/℃ | 熔点/℃ | 含油量(质量分数)/% | 收率(质量分数)/% |
---|---|---|---|---|---|---|---|---|
1 | 6.75 | 5 | 12.80 | 5.9 | 5 | 51.75 | 0.606 | 18.48 |
2 | 9.04 | 5 | 7.5 | 5.9 | 5 | 53.08 | 0.6 | 18.12 |
3 | 10 | 8 | 15 | 5.3 | 10 | 52.47 | 2.2 | 21.04 |
4 | 3.5 | 2 | 0 | 6.5 | 10 | 58.85 | 0 | 2.24 |
5 | 10 | 8 | 0 | 5.3 | 0 | 49.14 | 1.388 | 38.96 |
6 | 3.5 | 8 | 15 | 6.5 | 10 | 50.92 | 3.565 | 23.66 |
7 | 3.5 | 8 | 0 | 6.5 | 0 | 50.51 | 1.912 | 27.28 |
8 | 3.5 | 8 | 0 | 5.3 | 10 | 50.56 | 2.165 | 28 |
9 | 6.75 | 7.12 | 7.5 | 5.9 | 5 | 50.49 | 1.123 | 26.06 |
10 | 6.75 | 5 | 7.5 | 5.48 | 5 | 51.39 | 0.993 | 26.4 |
11 | 3.5 | 2 | 15 | 5.3 | 10 | 54.82 | 0.847 | 11.5 |
12 | 3.5 | 2 | 15 | 6.5 | 0 | 52.11 | 0.898 | 22.94 |
13 | 6.75 | 5 | 7.5 | 5.9 | 5 | 52.03 | 0.548 | 24.86 |
14 | 4.45 | 5 | 7.5 | 5.9 | 5 | 51.29 | 0.77 | 27.82 |
15 | 6.75 | 5 | 7.5 | 5.9 | 1.47 | 50.65 | 0.615 | 30.64 |
16 | 6.75 | 5 | 7.5 | 6.32 | 5 | 52.63 | 0.877 | 25.56 |
17 | 10 | 2 | 0 | 5.3 | 10 | 60.01 | 0.678 | 3.6 |
18 | 6.75 | 5 | 2.19 | 5.9 | 5 | 53.35 | 0.545 | 19.56 |
19 | 6.75 | 5 | 7.5 | 5.9 | 5 | 51.71 | 0.546 | 22.78 |
20 | 10 | 2 | 15 | 5.3 | 0 | 52.87 | 0.384 | 19.68 |
21 | 6.75 | 5 | 7.5 | 5.9 | 5 | 52.17 | 0.656 | 24.22 |
22 | 10 | 8 | 15 | 6.5 | 0 | 50.21 | 0.1 | 33.74 |
23 | 10 | 8 | 0 | 6.5 | 10 | 57.04 | 1.558 | 7.18 |
24 | 6.75 | 5 | 7.5 | 5.9 | 8.53 | 53.53 | 0.89 | 20.76 |
25 | 10 | 2 | 0 | 6.5 | 0 | 57.27 | 0.91 | 6.06 |
26 | 3.5 | 2 | 0 | 5.3 | 0 | 51.85 | 0.576 | 24.6 |
27 | 10 | 2 | 15 | 6.5 | 10 | 60.94 | 0.067 | 2.5 |
28 | 6.75 | 2.88 | 7.5 | 5.9 | 5 | 53.46 | 0.255 | 15.1 |
29 | 3.5 | 8 | 15 | 5.3 | 0 | 46.83 | 1.424 | 46.44 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 285.795 | 11 | 25.981 | 587.799 | <0.0001 |
X1 | 36.079 | 1 | 36.079 | 816.245 | 0.00000 |
X2 | 109.475 | 1 | 109.475 | 2476.746 | 0.00000 |
X3 | 13.575 | 1 | 13.575 | 307.121 | 0.00000 |
X4 | 23.947 | 1 | 23.947 | 541.782 | 0.00000 |
X5 | 79.906 | 1 | 79.906 | 1807.780 | 0.00000 |
X1X2 | 0.731 | 1 | 0.731 | 16.539 | 0.00080 |
14.547 | 1 | 14.547 | 329.109 | 0.00000 | |
X1X4 | 0.436 | 1 | 0.436 | 9.855 | 0.00598 |
X3X4 | 1.513 | 1 | 1.513 | 34.227 | 0.00002 |
X1X5 | 3.168 | 1 | 3.168 | 71.681 | 0.00000 |
X2X5 | 2.418 | 1 | 2.418 | 54.705 | 0.00000 |
残差 | 0.751 | 17 | 0.044 | — | — |
失拟项 | 0.640 | 15 | 0.043 | 0.767 | 0.6992 |
纯误差 | 0.111 | 2 | 0.055 | — | — |
R2=0.997378 | |||||
W=0.1803>0.05 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 285.795 | 11 | 25.981 | 587.799 | <0.0001 |
X1 | 36.079 | 1 | 36.079 | 816.245 | 0.00000 |
X2 | 109.475 | 1 | 109.475 | 2476.746 | 0.00000 |
X3 | 13.575 | 1 | 13.575 | 307.121 | 0.00000 |
X4 | 23.947 | 1 | 23.947 | 541.782 | 0.00000 |
X5 | 79.906 | 1 | 79.906 | 1807.780 | 0.00000 |
X1X2 | 0.731 | 1 | 0.731 | 16.539 | 0.00080 |
14.547 | 1 | 14.547 | 329.109 | 0.00000 | |
X1X4 | 0.436 | 1 | 0.436 | 9.855 | 0.00598 |
X3X4 | 1.513 | 1 | 1.513 | 34.227 | 0.00002 |
X1X5 | 3.168 | 1 | 3.168 | 71.681 | 0.00000 |
X2X5 | 2.418 | 1 | 2.418 | 54.705 | 0.00000 |
残差 | 0.751 | 17 | 0.044 | — | — |
失拟项 | 0.640 | 15 | 0.043 | 0.767 | 0.6992 |
纯误差 | 0.111 | 2 | 0.055 | — | — |
R2=0.997378 | |||||
W=0.1803>0.05 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 15.971 | 15 | 1.065 | 252.213 | <0.0001 |
X1 | 1.049 | 1 | 1.049 | 248.401 | 0.00000 |
X2 | 6.567 | 1 | 6.567 | 1555.510 | 0.00000 |
X3 | 0.007 | 1 | 0.007 | 1.622 | 0.22518 |
X4 | 0.032 | 1 | 0.032 | 7.507 | 0.01689 |
X5 | 0.798 | 1 | 0.798 | 188.949 | 0.00000 |
X1X2 | 0.782 | 1 | 0.782 | 185.317 | 0.00000 |
X1X3 | 0.933 | 1 | 0.933 | 221.041 | 0.00000 |
0.026 | 1 | 0.026 | 6.078 | 0.02838 | |
X1X4 | 0.713 | 1 | 0.713 | 168.934 | 0.00000 |
X2X4 | 0.020 | 1 | 0.020 | 4.776 | 0.04775 |
0.210 | 1 | 0.210 | 49.762 | 0.00001 | |
X2X5 | 2.132 | 1 | 2.132 | 504.923 | 0.00000 |
X3X5 | 1.133 | 1 | 1.133 | 268.417 | 0.00000 |
X4X5 | 0.035 | 1 | 0.035 | 8.283 | 0.01294 |
0.021 | 1 | 0.021 | 4.935 | 0.04469 | |
残差 | 0.055 | 13 | 0.004 | — | — |
失拟项 | 0.047 | 11 | 0.004 | 1.078 | 0.5758 |
纯误差 | 0.008 | 2 | 0.004 | — | — |
R2=0.996 | |||||
R2Adj=0.992 | |||||
W=0.4765>0.05 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 15.971 | 15 | 1.065 | 252.213 | <0.0001 |
X1 | 1.049 | 1 | 1.049 | 248.401 | 0.00000 |
X2 | 6.567 | 1 | 6.567 | 1555.510 | 0.00000 |
X3 | 0.007 | 1 | 0.007 | 1.622 | 0.22518 |
X4 | 0.032 | 1 | 0.032 | 7.507 | 0.01689 |
X5 | 0.798 | 1 | 0.798 | 188.949 | 0.00000 |
X1X2 | 0.782 | 1 | 0.782 | 185.317 | 0.00000 |
X1X3 | 0.933 | 1 | 0.933 | 221.041 | 0.00000 |
0.026 | 1 | 0.026 | 6.078 | 0.02838 | |
X1X4 | 0.713 | 1 | 0.713 | 168.934 | 0.00000 |
X2X4 | 0.020 | 1 | 0.020 | 4.776 | 0.04775 |
0.210 | 1 | 0.210 | 49.762 | 0.00001 | |
X2X5 | 2.132 | 1 | 2.132 | 504.923 | 0.00000 |
X3X5 | 1.133 | 1 | 1.133 | 268.417 | 0.00000 |
X4X5 | 0.035 | 1 | 0.035 | 8.283 | 0.01294 |
0.021 | 1 | 0.021 | 4.935 | 0.04469 | |
残差 | 0.055 | 13 | 0.004 | — | — |
失拟项 | 0.047 | 11 | 0.004 | 1.078 | 0.5758 |
纯误差 | 0.008 | 2 | 0.004 | — | — |
R2=0.996 | |||||
R2Adj=0.992 | |||||
W=0.4765>0.05 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 2925.057 | 8 | 365.632 | 64.488 | <0.0001 |
X1 | 217.152 | 1 | 217.152 | 38.300 | 0.0000 |
X2 | 1168.309 | 1 | 1168.309 | 206.059 | 0.0000 |
X3 | 107.840 | 1 | 107.840 | 19.020 | 0.0000 |
X4 | 278.555 | 1 | 278.555 | 49.129 | 0.0000 |
X5 | 948.261 | 1 | 948.261 | 167.248 | 0.0003 |
72.162 | 1 | 72.162 | 12.727 | 0.00102 | |
X3X4 | 83.631 | 1 | 83.631 | 14.750 | 0.00193 |
26.589 | 1 | 26.589 | 4.689 | 0.04261 | |
残差 | 113.395 | 20 | 5.669 | — | — |
失拟项 | 111.126 | 18 | 6.174 | 5.439 | 0.1664 |
纯误差 | 2.270 | 2 | 1.135 | — | — |
R2=0.962 | |||||
R2Adj=0.947 | |||||
W=0.1532>0.05 |
方差来源 | 平方和 | 自由度 | 均方 | F值 | P值 |
---|---|---|---|---|---|
模型 | 2925.057 | 8 | 365.632 | 64.488 | <0.0001 |
X1 | 217.152 | 1 | 217.152 | 38.300 | 0.0000 |
X2 | 1168.309 | 1 | 1168.309 | 206.059 | 0.0000 |
X3 | 107.840 | 1 | 107.840 | 19.020 | 0.0000 |
X4 | 278.555 | 1 | 278.555 | 49.129 | 0.0000 |
X5 | 948.261 | 1 | 948.261 | 167.248 | 0.0003 |
72.162 | 1 | 72.162 | 12.727 | 0.00102 | |
X3X4 | 83.631 | 1 | 83.631 | 14.750 | 0.00193 |
26.589 | 1 | 26.589 | 4.689 | 0.04261 | |
残差 | 113.395 | 20 | 5.669 | — | — |
失拟项 | 111.126 | 18 | 6.174 | 5.439 | 0.1664 |
纯误差 | 2.270 | 2 | 1.135 | — | — |
R2=0.962 | |||||
R2Adj=0.947 | |||||
W=0.1532>0.05 |
1 | 相宏伟, 杨勇, 李永旺. 煤炭间接液化: 从基础到工业化[J]. 中国科学:化学, 2014, 44(12): 1876-1892. |
XIANG Hongwei, YANG Yong, LI Yongwang. Indirect coal-to-liquids technology from fundamental research to commercialization[J]. Scientia Sinica Chimica, 2014, 44(12): 1876-1892. | |
2 | ZHAI Peng, LI Yinwen, WANG Meng, et al. Development of direct conversion of syngas to unsaturated hydrocarbons based on Fischer-Tropsch route[J]. Chem, 2021, 7(11): 3027-3051. |
3 | A Yu KRYLOVA. Products of the Fischer-Tropsch synthesis (a review)[J]. Solid Fuel Chemistry, 2014, 48(1): 22-35. |
4 | GRUBER Hannes, LINDNER Lukas, ARLT Stefan, et al. A novel production route and process optimization of biomass-derived paraffin wax for pharmaceutical application[J]. Journal of Cleaner Production, 2020, 275: 124135. |
5 | IVANOVA I K, KASHIRTSEV V A, SEMENOV M E, et al. Effect of the solvent composition on the content of the crystalline phase and melting temperature of paraffin waxes[J]. Russian Journal of Applied Chemistry, 2020, 93(4): 603-610. |
6 | MOHAMED N H, ZAKY M T, FARAG A S, et al. Separation of paraffin wax using solvent fractionation[J]. Petroleum Science and Technology, 2008, 26(5): 562-574. |
7 | 郑立辉. 尿素包合法制取低熔点石蜡的研究[J]. 精细石油化工, 2002, 19(6): 11-13. |
ZHENG Lihui. Preparation of low melting point paraffin by urea-adduct method[J]. Speciality Petrochemicals, 2002, 19(6): 11-13. | |
8 | ZAKY Magdy T, MOHAMED Nermen H, FARAG Amal S. Separation of some paraffin wax grades using solvent extraction technique[J]. Fuel Processing Technology, 2011, 92(10): 2024-2029. |
9 | ZAKY Magdy T, MOHAMED Nermen H, FARAG Amal S. Separation of different paraffin wax grades using two comparative deoiling techniques[J]. Fuel Processing Technology, 2007, 88(9): 913-920. |
10 | 孙东旭, 戴咏川, 齐程远, 等. 费-托合成蜡溶剂精制及其结构与性质的研究[J]. 石油炼制与化工, 2016, 47(11): 78-81. |
SUN Dongxu, DAI Yongchuan, QI Chengyuan, et al. Research on F-T wax solvent deoiling and wax structure and properties[J]. Petroleum Processing and Petrochemicals, 2016, 47(11): 78-81. | |
22 | XU Chunming, YANG Chaohe. Petroleum refining engineering[M]. 4th ed. Beijing: Petroleum Industry Press, 2009: 554-556. |
23 | MOKHLIF Nassir D, AL-KAYIEM Hussain H, BAHAROM M B. Estimation model for the wax crystal size distribution in solvent dewaxing process[J]. Journal of Applied Sciences, 2012, 12(24): 2548-2554. |
24 | MOHAMED Nermen H. Competitive study on separation and characterization of microcrystalline waxes using two deoiling techniques[J]. Fuel Processing Technology, 2012, 96: 116-122. |
25 | 陈洁, 陈侠. 制备碳酸锂结晶的工艺优化[J]. 无机盐工业, 2019, 51(8): 29-32. |
CHEN Jie, CHEN Xia. Crystallization process optimization for preparation of lithium carbonate[J]. Inorganic Chemicals Industry, 2019, 51(8): 29-32. | |
26 | 水天德. 现代润滑油生产工艺[M]. 北京: 中国石化出版社, 1997: 233-240. |
SHUI Tiande. Modern lubricating oil production technology[M]. Beijing: China Petrochemical Press, 1997: 233-240. | |
27 | NIKITIN K V, D’YACHKOV V N, NIKITIN V I, et al. Influence of temperature conditions on the shrinkage of wax patterns for investment casting[J]. IOP Conference Series: Materials Science and Engineering, 2020, 919(2): 022041. |
28 | 张有云. 图像数据过程能力分析系统研究[D]. 昆明: 昆明理工大学, 2021. |
ZHANG Youyun. Research on image data process capability analysis system[D]. Kunming: Kunming University of Science and Technology, 2021. | |
11 | 吴文广. 酮苯二段低温脱蜡-二段脱油工艺研究[D]. 上海: 华东理工大学, 2019. |
WU Wenguang. Study on two-stage low temperature dewaxing-two-stage deoiling process of ketone-benzene[D]. Shanghai: East China University of Science and Technology, 2019. | |
12 | 南远方. 酮苯装置脱蜡结晶工艺因素研究[D]. 北京: 北京化工大学, 2015. |
Yuanfang NAN. Study on technological factors of dewaxing and crystallization in ketone-benzene plant[D]. Beijing: Beijing University of Chemical Technology, 2015. | |
13 | ESLAMI Akbar, ASADI Anvar, MESERGHANI Maryam, et al. Optimization of sonochemical degradation of amoxicillin by sulfate radicals in aqueous solution using response surface methodology (RSM)[J]. Journal of Molecular Liquids, 2016, 222: 739-744. |
14 | 程永春, 徐志枢, 马桂荣, 等. 基于响应曲面法的SMA沥青混合料试验研究[J]. 应用基础与工程科学学报, 2021, 29(2): 493-502. |
CHENG Yongchun, XU Zhishu, MA Guirong, et al. Response surface method for asphalt mixture design[J]. Journal of Basic Science and Engineering, 2021, 29(2): 493-502. | |
15 | 胡菊华. 基于残差分析的线性回归模型的诊断与修正[J]. 统计与决策, 2019, 35(24): 5-8. |
HU Juhua. Diagnosis and correction of linear regression model based on residual analysis[J]. Statistics & Decision, 2019, 35(24): 5-8. | |
16 | 李锐, 姜永华, 张燕玲, 等. 基于响应曲面法优化硫酸铵结晶[J]. 硅酸盐学报, 2022, 50(3): 782-790. |
LI Rui, JIANG Yonghua, ZHANG Yanling, et al. Optimisation of ammonium sulphate crystallization based on response surface methodology[J]. Journal of the Chinese Ceramic Society, 2022, 50(3): 782-790. | |
17 | NOORDIN M Y, VENKATESH V C, SHARIF S, et al. Application of response surface methodology in describing the performance of coated carbide tools when turning AISI 1045 steel[J]. Journal of Materials Processing Technology, 2004, 145(1): 46-58. |
18 | 李恒, 来倩, 何沛, 等. 高介孔率烟梗基活性炭的优化制备[J]. 化学研究, 2021, 32(5): 438-444. |
LI Heng, LAI Qian, HE Pei, et al. Preparation of tobacco stem-based activated carbon with high mesoporosity[J]. Chemical Research, 2021, 32(5): 438-444. | |
19 | 洪东峰. 基于响应面方法的聚丙烯流程模拟与优化[D]. 北京: 北京理工大学, 2013. |
HONG Dongfeng. Simulation and optimization of polypropylene process based on pesponse sruface method[D]. Beijing: Beijing Institute of Technololy, 2013. | |
20 | YETILMEZSOY Kaan, SARAL Arslan. Stochastic modeling approaches based on neural network and linear-nonlinear regression techniques for the determination of single droplet collection efficiency of countercurrent spray towers[J]. Environmental Modeling & Assessment, 2007, 12(1): 13-26. |
21 | 苗恒, 李俊诚, 钱震, 等. 费托合成蜡脱油技术及其研究进展[J]. 当代化工研究, 2020(14): 138-139. |
MIAO Heng, LI Juncheng, QIAN Zhen, et al. Research progress of deoiling technology of Fischer Tropsch synthetic wax[J]. Modern Chemical Research, 2020(14): 138-139. | |
22 | 徐春明, 杨朝合. 石油炼制工程[M]. 4版. 北京: 石油工业出版社, 2009: 554-556. |
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