Acta Agriculturae Zhejiangensis ›› 2026, Vol. 38 ›› Issue (5): 944-954.DOI: 10.3969/j.issn.1004-1524.20250062
• Environmental Science • Previous Articles Next Articles
CHENG Kai1,2(
), LI Feiyue1, HE Lili2,3, YANG Chenghu2, WANG Yuying2,3, LYU Haohao2,3, YANG Shengmao2,3, LIU Yuxue1,2,3,*(
)
Received:2025-01-18
Online:2026-05-25
Published:2026-06-02
CLC Number:
CHENG Kai, LI Feiyue, HE Lili, YANG Chenghu, WANG Yuying, LYU Haohao, YANG Shengmao, LIU Yuxue. Preparation of nitrogen-doped rice straw biochar activated by sodium bicarbonate and its adsorption of cadmium[J]. Acta Agriculturae Zhejiangensis, 2026, 38(5): 944-954.
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URL: http://www.zjnyxb.cn/EN/10.3969/j.issn.1004-1524.20250062
| 样品 Sample | pH值 pH value | EC/ (μS·cm-1) | wC/% | wN/% | wH/% | wO/% | H/C | O/C | SSA/ (m2·g-1) | PV/ (cm3·g-1) | APS/nm |
|---|---|---|---|---|---|---|---|---|---|---|---|
| BC | 7.93±0.03 | 75.10±1.08 | 48.06 | 0.93 | 2.52 | 48.49 | 0.63 | 0.76 | 181.92 | 0.12 | 2.69 |
| BC2-1-1 | 9.90±0.01 | 115.23±2.20 | 30.00 | 2.03 | 1.86 | 66.11 | 0.74 | 1.65 | 288.79 | 0.24 | 3.28 |
| BC1-1-1 | 9.54±0.01 | 148.70±1.31 | 23.46 | 2.39 | 1.81 | 72.34 | 0.93 | 2.31 | 384.19 | 0.32 | 3.38 |
Table 1 Physicochemical properties of the prepared biochar
| 样品 Sample | pH值 pH value | EC/ (μS·cm-1) | wC/% | wN/% | wH/% | wO/% | H/C | O/C | SSA/ (m2·g-1) | PV/ (cm3·g-1) | APS/nm |
|---|---|---|---|---|---|---|---|---|---|---|---|
| BC | 7.93±0.03 | 75.10±1.08 | 48.06 | 0.93 | 2.52 | 48.49 | 0.63 | 0.76 | 181.92 | 0.12 | 2.69 |
| BC2-1-1 | 9.90±0.01 | 115.23±2.20 | 30.00 | 2.03 | 1.86 | 66.11 | 0.74 | 1.65 | 288.79 | 0.24 | 3.28 |
| BC1-1-1 | 9.54±0.01 | 148.70±1.31 | 23.46 | 2.39 | 1.81 | 72.34 | 0.93 | 2.31 | 384.19 | 0.32 | 3.38 |
Fig.1 Infrared spectrum of prepared biochar BC, Prepared rice straw biochar. BC2-1-1 and BC1-1-1 represent the biochar made from rice straw, sodium and urea at the ratio of 2∶1∶1 and 1∶1∶1, respectively. The same as below.
Fig.3 Effects of pH value (a), initial mass concentration (b), biochar addition amount (c), and temperature (d) on the Cd2+ removal rate of biochar Bars marked without the same letters indicate significant (p<0.05) difference within varying temperature for the same biochar.
Fig.4 Adsorption kinetics models of Cd2+in solution by BC(a), BC2-1-1 (b), and BC1-1-1 (c) qe is the adsorption capacity at equilibrium; qt is the adsorption capacity at time t. The same as below.
| 样品 Sample | 准一级动力学模型Pseudo-first-order model | 准二级动力学模型Pseudo-second-order model | ||||
|---|---|---|---|---|---|---|
| qe/(mg·g-1) | R2 | k1/min-1 | qe/(mg·g-1) | R2 | k2/(g·mg-1·min-1) | |
| BC | 0.496 3 | 0.861 8 | 0.996 0 | 0.702 9 | 0.995 0 | 0.301 8 |
| BC2-1-1 | 7.155 6 | 0.882 9 | 0.157 6 | 7.369 2 | 0.997 1 | 0.023 1 |
| BC1-1-1 | 8.463 8 | 0.817 8 | 0.180 8 | 8.410 4 | 0.997 1 | 0.014 7 |
Table 2 Parameters of pseudo-first-order and pseudo-second-order dynamics equations
| 样品 Sample | 准一级动力学模型Pseudo-first-order model | 准二级动力学模型Pseudo-second-order model | ||||
|---|---|---|---|---|---|---|
| qe/(mg·g-1) | R2 | k1/min-1 | qe/(mg·g-1) | R2 | k2/(g·mg-1·min-1) | |
| BC | 0.496 3 | 0.861 8 | 0.996 0 | 0.702 9 | 0.995 0 | 0.301 8 |
| BC2-1-1 | 7.155 6 | 0.882 9 | 0.157 6 | 7.369 2 | 0.997 1 | 0.023 1 |
| BC1-1-1 | 8.463 8 | 0.817 8 | 0.180 8 | 8.410 4 | 0.997 1 | 0.014 7 |
Fig.5 Isothermal adsorption models of Cd2+ in solution by BC (a), BC2-1-1 (b), and BC1-1-1 (c) Ce is the Cd2+ concentration in the solution at equilibrium, mg·L-1.
| 样品 Sample | 朗缪尔等温吸附模型 Langmuir isothermal adsorption model | 弗罗因德利希等温吸附模型 Freundlich isothermal adsorption model | ||||
|---|---|---|---|---|---|---|
| qm/(mg·g-1) | kL/(L·mg-1) | R2 | kF/[mg·g-1·(mg·L-1)-1/n) | 1/n | R2 | |
| BC | 8.605 8 | 0.996 6 | 0.997 2 | 4.771 7 | 0.173 4 | 0.856 4 |
| BC2-1-1 | 45.322 6 | 0.222 3 | 0.990 9 | 9.068 4 | 0.850 1 | 0.932 1 |
| BC1-1-1 | 40.322 6 | 0.307 7 | 0.991 5 | 9.583 1 | 1.096 9 | 0.878 9 |
Table 3 Fitting parameters of isothermal adsorption models
| 样品 Sample | 朗缪尔等温吸附模型 Langmuir isothermal adsorption model | 弗罗因德利希等温吸附模型 Freundlich isothermal adsorption model | ||||
|---|---|---|---|---|---|---|
| qm/(mg·g-1) | kL/(L·mg-1) | R2 | kF/[mg·g-1·(mg·L-1)-1/n) | 1/n | R2 | |
| BC | 8.605 8 | 0.996 6 | 0.997 2 | 4.771 7 | 0.173 4 | 0.856 4 |
| BC2-1-1 | 45.322 6 | 0.222 3 | 0.990 9 | 9.068 4 | 0.850 1 | 0.932 1 |
| BC1-1-1 | 40.322 6 | 0.307 7 | 0.991 5 | 9.583 1 | 1.096 9 | 0.878 9 |
Fig.6 Effects of solution ion strength (a),coexisting ions (b), and cycle times (c) on Cd2+ adsorption by BC2-1-1 Bars marked without the same letters indicate significant difference at p<0.05. None indicates control without coexisting ions introduced in the solution.
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