浙江农业学报 ›› 2026, Vol. 38 ›› Issue (5): 944-954.DOI: 10.3969/j.issn.1004-1524.20250062
程凯1,2(
), 李飞跃1, 何莉莉2,3, 杨承虎2, 汪玉瑛2,3, 吕豪豪2,3, 杨生茂2,3, 刘玉学1,2,3,*(
)
收稿日期:2025-01-18
出版日期:2026-05-25
发布日期:2026-06-02
作者简介:程凯,研究方向为生物炭与重金属污染修复。E-mail:18155089603@163.com
通讯作者:
*刘玉学,E-mail:liuyuxue505@163.com
基金资助:
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
Published:2026-05-25
Online:2026-06-02
摘要:
以水稻秸秆为原料,分别以尿素和碳酸氢钠为氮源和化学活化剂,制备基于碳酸氢钠活化的氮掺杂水稻秸秆生物炭,开展生物炭吸附溶液中镉离子(Cd2+)的系列实验,研究溶液pH值、生物炭添加量、溶液中Cd2+初始质量浓度、温度、离子强度、共存离子等对生物炭吸附溶液中Cd2+的影响,并从动力学角度探究生物炭吸附Cd2+的机制。结果表明,尿素掺杂和碳酸氢钠活化的共同作用,提高了生物炭对Cd2+的吸附性能。相较于未改性的水稻秸秆生物炭(BC),将水稻秸秆粉、碳酸氢钠、尿素以2∶1∶1的比例改性制备的生物炭BC2-1-1对Cd2+的饱和吸附量为45.322 6 mg·g-1,是BC的5.27倍。生物炭对Cd2+的等温吸附行为符合朗缪尔(Langmuir)等温吸附模型,动力学行为符合准二级动力学方程,说明是以化学吸附为主导的单分子层吸附机制。研究结果可为水稻秸秆的高值化利用和镉污染水体的修复提供理论依据和技术支撑。
中图分类号:
程凯, 李飞跃, 何莉莉, 杨承虎, 汪玉瑛, 吕豪豪, 杨生茂, 刘玉学. 基于碳酸氢钠活化的氮掺杂水稻秸秆生物炭的制备及其对镉的吸附[J]. 浙江农业学报, 2026, 38(5): 944-954.
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.
| 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 |
表1 制备的生物炭的理化性质
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 |
图1 生物炭的红外光谱 BC,本研究制备的水稻秸秆生物炭;BC2-1-1和BC1-1-1分别为由水稻秸秆粉、碳酸氢钠、尿素按2∶1∶1和1∶1∶1的比例混合制作的生物炭。下同。
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.
图3 生物炭Cd2+去除率受pH值(a)、初始质量浓度(b)、生物炭添加量(c)和温度(d)的影响 同一材料柱上无相同字母的表示不同温度下差异显著(p<0.05)。
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.
图4 BC(a)、BC2-1-1(b)和BC1-1-1(c)对溶液中Cd2+的吸附动力学模型 qe为平衡时的吸附量;qt为t时刻的吸附量。下同。
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 |
表2 准一级和准二级动力学方程参数
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 |
图5 BC(a)、BC2-1-1(b)和BC1-1-1(c)对溶液中Cd2+的等温吸附模型 Ce为平衡时溶液中的Cd2+含量,mg·L-1。
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 |
表3 拟合的等温吸附模型参数
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 |
图6 溶液离子强度(a) 、共存离子(b) 和循环次数(c)对BC2-1-1吸附Cd2+的影响 柱上无相同字母的表示差异显著(p<0.05)。None表示溶液中不含有共存离子。
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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