Chemical Industry and Engineering Progress ›› 2019, Vol. 38 ›› Issue (01): 692-706.DOI: 10.16085/j.issn.1000-6613.2018-0993
• Resources and environmental engineering • Previous Articles Next Articles
Chongqing WANG1(),Hui WANG2,Xiaoyan JIANG1,Rong HUANG1,Yijun CAO1()
Received:
2018-05-14
Revised:
2018-07-05
Online:
2019-01-05
Published:
2019-01-05
Contact:
Yijun CAO
通讯作者:
曹亦俊
作者简介:
王重庆(1990—),男,博士,讲师,研究方向为固体废弃物资源化和废水处理。E-mail:<email>zilangwang@126.com</email>。|曹亦俊,博士,教授,博士生导师,研究方向为微细粒浮选理论及工艺。E-mail:<email>yijuncao@126.com</email>。
基金资助:
CLC Number:
Chongqing WANG, Hui WANG, Xiaoyan JIANG, Rong HUANG, Yijun CAO. Research advances on adsorption of heavy metals by biochar[J]. Chemical Industry and Engineering Progress, 2019, 38(01): 692-706.
王重庆, 王晖, 江小燕, 黄荣, 曹亦俊. 生物炭吸附重金属离子的研究进展[J]. 化工进展, 2019, 38(01): 692-706.
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URL: https://hgjz.cip.com.cn/EN/10.16085/j.issn.1000-6613.2018-0993
用途 | 作用 | 优点 | 缺点 |
---|---|---|---|
土壤修复 | 碳封存、土壤改良 | 廉价、可持续性资源、保留水分和养分、降低肥料消费、减少温室气体释放 | 重金属和多环芳烃污染风险 |
吸附剂 | 吸附土壤和水体中的重金属和有机污染物 | 廉价、丰富的可持续资源、表面基团有利于 吸附 | 吸附性能随前体的不同变化较大、对有机/无机污染物修复效率不稳定 |
生物质废弃物管理 | 碳封存、减少废弃物排放 | 实现废弃生物质资源化、减少温室气体释放 | 存在污染的潜在风险 |
燃料电池 | 燃料电池燃料 | 可再生能源 | 高灰分、电压和能量输出较低 |
储存材料 | 二氧化碳封存、氢气储存 | 廉价、丰富的可持续资源 | 需要表面处理 |
催化剂 | 负载活性组分、催化作用 | 共催化、廉价、易于回收负载的金属 | 效率低、耐磨性差 |
用途 | 作用 | 优点 | 缺点 |
---|---|---|---|
土壤修复 | 碳封存、土壤改良 | 廉价、可持续性资源、保留水分和养分、降低肥料消费、减少温室气体释放 | 重金属和多环芳烃污染风险 |
吸附剂 | 吸附土壤和水体中的重金属和有机污染物 | 廉价、丰富的可持续资源、表面基团有利于 吸附 | 吸附性能随前体的不同变化较大、对有机/无机污染物修复效率不稳定 |
生物质废弃物管理 | 碳封存、减少废弃物排放 | 实现废弃生物质资源化、减少温室气体释放 | 存在污染的潜在风险 |
燃料电池 | 燃料电池燃料 | 可再生能源 | 高灰分、电压和能量输出较低 |
储存材料 | 二氧化碳封存、氢气储存 | 廉价、丰富的可持续资源 | 需要表面处理 |
催化剂 | 负载活性组分、催化作用 | 共催化、廉价、易于回收负载的金属 | 效率低、耐磨性差 |
工艺 | 温度 /℃ | 加热速率 /℃·min-1 | 停留时间 | 目标产物 | 生物炭产率/% |
---|---|---|---|---|---|
快速热解 | 400~600 | 约60000 | 数秒 | 生物油 | 10~20 |
慢速热解 | 350~800 | <10 | 数分到数小时 | 生物炭 | 20~40 |
气化 | 700~1500 | >100 | 数秒到数分 | 合成气 | 约10 |
水热炭化 | 175~250 | <10 | 数小时 | 水热炭 | 30~60 |
烘焙 | 200~300 | <10 | 数分到数小时 | 坚硬生物炭 | 67~84 |
工艺 | 温度 /℃ | 加热速率 /℃·min-1 | 停留时间 | 目标产物 | 生物炭产率/% |
---|---|---|---|---|---|
快速热解 | 400~600 | 约60000 | 数秒 | 生物油 | 10~20 |
慢速热解 | 350~800 | <10 | 数分到数小时 | 生物炭 | 20~40 |
气化 | 700~1500 | >100 | 数秒到数分 | 合成气 | 约10 |
水热炭化 | 175~250 | <10 | 数小时 | 水热炭 | 30~60 |
烘焙 | 200~300 | <10 | 数分到数小时 | 坚硬生物炭 | 67~84 |
动力学模型 | 线性方程 | 线性拟合 | 特征 参数 |
---|---|---|---|
准一级动力学 | | ln(Q e-Qt )对t | Q e,k 1 |
准二级动力学 | | t/Qt 对t | Q e,k 2 |
内扩散动力学 | | Qt 对t 0.5 | k |
液膜扩散动力学 | | ln(1-Qt /Q e)对t | k |
Elovich动力学 | | Qt 对lnt | α,β |
动力学模型 | 线性方程 | 线性拟合 | 特征 参数 |
---|---|---|---|
准一级动力学 | | ln(Q e-Qt )对t | Q e,k 1 |
准二级动力学 | | t/Qt 对t | Q e,k 2 |
内扩散动力学 | | Qt 对t 0.5 | k |
液膜扩散动力学 | | ln(1-Qt /Q e)对t | k |
Elovich动力学 | | Qt 对lnt | α,β |
模型 | 非线性方程 | 线性方程 | 线性拟合 | 特征参数 |
---|---|---|---|---|
Langmuir | | | C e/Q e对C e | Q m,b,R L |
Freundlich | | | lgQ e对lgC e | n,K F |
Dubinin-Radushkevich | | | lnQ e对ε2 | Β,ε,E |
Temkin | | | Q e对lnC e | b,A |
Flory–Huggins | | | lg | θ,K |
Hill | | | lg | K , n |
Sips | | | ln | K,a,β |
Toth | | | ln | K,a. ,n |
模型 | 非线性方程 | 线性方程 | 线性拟合 | 特征参数 |
---|---|---|---|---|
Langmuir | | | C e/Q e对C e | Q m,b,R L |
Freundlich | | | lgQ e对lgC e | n,K F |
Dubinin-Radushkevich | | | lnQ e对ε2 | Β,ε,E |
Temkin | | | Q e对lnC e | b,A |
Flory–Huggins | | | lg | θ,K |
Hill | | | lg | K , n |
Sips | | | ln | K,a,β |
Toth | | | ln | K,a. ,n |
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