Chemistry and Industry of Forest Products ›› 2024, Vol. 44 ›› Issue (2): 55-63.doi: 10.3969/j.issn.0253-2417.2024.02.008
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Yan LU1(), Xueqin LI1,2, Yanling LI1, Tanglei SUN1, Peng LIU1,*(), Tingzhou LEI1
Received:
2023-07-18
Online:
2024-04-28
Published:
2024-04-23
Contact:
Peng LIU
E-mail:893667124@qq.com;liupeng@cczu.edu.cn
CLC Number:
Yan LU, Xueqin LI, Yanling LI, Tanglei SUN, Peng LIU, Tingzhou LEI. Preparation of Iron Based Carbon Aluminum Catalyst and Its Catalytic for Hydrogen Production from Corn Straw Pyrolysis[J]. Chemistry and Industry of Forest Products, 2024, 44(2): 55-63.
Table 1
Gas yield of catalytic CS under different conditions"
编号No. | 条件condition | H2/(mL·g-1) | CO/(mL·g-1) | CH4/(mL·g-1) | CO2/(mL·g-1) | 总产率/(mL·g-1)total gas yield | 气体转化率/% gas conversion(yg) |
1 | CS | 43.65 | 25.75 | 14.55 | 48.77 | 132.73 | 39.41 |
2 | CS(HTC) | 58.52 | 15.11 | 10.61 | 23.67 | 107.91 | 40.33 |
3 | CS+WA(HTC) | 49.98 | 23.14 | 15.16 | 49.39 | 137.68 | 36.67 |
4 | CS+AWA(HTC) | 62.76 | 28.82 | 18.25 | 50.73 | 160.56 | 41.54 |
5 | Fe/CS-AWA(HTC) | 64.36 | 30.02 | 16.89 | 49.78 | 161.06 | 43.77 |
Table 2
Experimental design scheme and results"
编号No. | A mAWA∶mCS | B 停留时间(250 ℃)/minresidence time | C 炭化温度/℃carbonization temp. | R1 H2产率/%H2 yield |
1 | 2∶1 | 40 | 500 | 61.48 |
2 | 4∶1 | 40 | 500 | 60.06 |
3 | 2∶1 | 60 | 500 | 98.16 |
4 | 4∶1 | 60 | 500 | 69.06 |
5 | 2∶1 | 40 | 700 | 54.28 |
6 | 4∶1 | 40 | 700 | 76.57 |
7 | 2∶1 | 60 | 700 | 70.72 |
8 | 4∶1 | 60 | 700 | 63.44 |
9 | 1∶1 | 50 | 600 | 78.51 |
10 | 5∶1 | 50 | 600 | 63.49 |
11 | 3∶1 | 30 | 600 | 56.10 |
12 | 3∶1 | 70 | 600 | 69.64 |
13 | 3∶1 | 50 | 400 | 82.57 |
14 | 3∶1 | 50 | 800 | 74.27 |
15 | 3∶1 | 50 | 600 | 59.80 |
16 | 3∶1 | 50 | 600 | 64.03 |
17 | 3∶1 | 50 | 600 | 64.47 |
18 | 3∶1 | 50 | 600 | 56.83 |
19 | 3∶1 | 50 | 600 | 66.49 |
20 | 3∶1 | 50 | 600 | 56.51 |
Table 3
Regression equation analysis of variance"
来源sources | 平方和sum of squares | 自由度df | 均方mean square | F值F value | P值P value | 显著性significant |
模型model | 2 038.89 | 9 | 226.54 | 16.27 | < 0.001 | ** |
A | 129.83 | 1 | 129.83 | 9.33 | 0.012 2 | * |
B | 361.73 | 1 | 361.73 | 25.98 | 0.000 5 | ** |
C | 101.81 | 1 | 101.81 | 7.31 | 0.022 1 | * |
AB | 409.55 | 1 | 409.55 | 29.42 | 0.000 3 | ** |
AC | 259.14 | 1 | 259.14 | 18.62 | 0.001 5 | ** |
BC | 224.26 | 1 | 224.26 | 16.11 | 0.002 5 | ** |
A2 | 155.20 | 1 | 155.20 | 11.15 | 0.007 5 | ** |
B2 | 5.15 | 1 | 5.15 | 0.37 | 0.556 8 | |
C2 | 473.52 | 1 | 473.52 | 34.02 | 0.000 2 | ** |
残差residual | 139.21 | 0 | 13.92 | 0.55 | 0.733 6 | |
失拟项lack of fit | 49.64 | 5 | 9.93 | |||
纯误差pure error | 89.57 | 5 | 17.91 | |||
总和sum | 2 178.10 | 9 |
Table 5
Specific surface area and pore structure analysis of catalyst"
催化剂catalyst | SBET/(m2·g-1) | SMic/(m2·g-1) | SExt/(m2·g-1) | 孔容/(cm3·g-1)pore volume | 孔径/nmpore size | 平均粒径/nmaverage particle size |
AWA | 77.09 | 28.10 | 48.99 | 0.015 0 | 4.38 | 77.83 |
CS-AWA | 30.19 | 13.56 | 16.63 | 0.007 3 | 6.81 | 198.73 |
Fe/CS-AWA | 40.72 | 15.78 | 24.94 | 0.008 1 | 4.84 | 147.34 |
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