Biomass Chemical Engineering ›› 2024, Vol. 58 ›› Issue (2): 22-30.doi: 10.3969/j.issn.1673-5854.2024.02.003
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Huanhuan ZHANG1, Ruinan YANG1, Zhenli YAN2,3, Zigao ZHAO2,3, Chun CHANG1,3,*()
Received:
2023-06-19
Online:
2024-03-30
Published:
2024-03-22
Contact:
Chun CHANG
E-mail:chunchang@zzu.edu.cn
CLC Number:
Huanhuan ZHANG, Ruinan YANG, Zhenli YAN, Zigao ZHAO, Chun CHANG. Hydrolysis and Kinetics of Wheat B Starch Slurry with Extremely Low Acid[J]. Biomass Chemical Engineering, 2024, 58(2): 22-30.
Table 1
Response surface design and results of B starch hydrolysis"
序号 No. | X1 水解温度/℃ temperature | X2 硫酸质量分数/% H2SO4 mass fraction | X3 水解时间/min time | Y DE值/% DE value |
1 | 150 | 0.05 | 60 | 61.38 |
2 | 190 | 0.05 | 60 | 38.78 |
3 | 150 | 0.09 | 60 | 63.05 |
4 | 190 | 0.09 | 60 | 42.26 |
5 | 150 | 0.07 | 30 | 42.27 |
6 | 190 | 0.07 | 30 | 35.47 |
7 | 150 | 0.07 | 90 | 62.49 |
8 | 190 | 0.07 | 90 | 28.72 |
9 | 170 | 0.05 | 30 | 68.26 |
10 | 170 | 0.09 | 30 | 70.78 |
11 | 170 | 0.05 | 90 | 76.34 |
12 | 170 | 0.09 | 90 | 78.96 |
13 | 170 | 0.07 | 60 | 90.36 |
14 | 170 | 0.07 | 60 | 88.88 |
15 | 170 | 0.07 | 60 | 89.41 |
16 | 170 | 0.07 | 60 | 87.25 |
17 | 170 | 0.07 | 60 | 86.98 |
Table 2
Variance analysis of DE value of glucose in B starch hydrolysate"
来源source | 平方和sum of squares | 自由度degree of freedom | 均方mean square | F值F value | P值P value |
模型model | 7 074.81 | 9 | 786.09 | 537.2 | < 0.000 1 |
X1 | 881.16 | 1 | 881.16 | 602.17 | < 0.000 1 |
X2 | 13.24 | 1 | 13.24 | 9.04 | 0.019 7 |
X3 | 110.48 | 1 | 110.48 | 75.5 | < 0.000 1 |
X1X2 | 0.82 | 1 | 0.82 | 0.56 | 0.478 8 |
X1X3 | 181.85 | 1 | 181.85 | 124.27 | 0.001 1 |
X2X3 | 2 500 | 1 | 2 500 | 1 710 | 0.468 2 |
X12 | 4 947.29 | 1 | 4 947.29 | 3 380.88 | < 0.000 1 |
X22 | 36.16 | 1 | 36.16 | 24.71 | 0.001 6 |
X32 | 612.44 | 1 | 612.44 | 418.53 | < 0.000 1 |
残差residual | 10.24 | 7 | 1.46 | 0.32 | 0.813 9 |
失拟项lack of fit | 1.97 | 3 | 0.66 | ||
净误差pure error | 8.28 | 4 | 2.07 | ||
总残差total | 7 085.05 | 16 |
Table 3
Kinetic parameters of ultra-low acid hydrolysis of B starch at different temperatures"
温度/℃ temp. | β=0 | β=1 | β=2 | |||||
R2 | k/(g·L-1·min-1) | R2 | k/min-1 | R2 | k/(g·L-1·min)-1 | |||
150 | 0.967 6 | 0.005 1±0.000 29 | 0.996 5 | 0.007 6±0.000 15 | 0.915 2 | 0.017 2±0.001 65 | ||
160 | 0.936 9 | 0.006 8±0.000 56 | 0.998 6 | 0.013 9±0.000 16 | 0.966 7 | 0.033 8±0.001 98 | ||
170 | 0.871 9 | 0.007 2±0.000 87 | 0.994 2 | 0.018 7±0.000 45 | 0.957 9 | 0.066 1±0.004 62 |
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