化工进展 ›› 2019, Vol. 38 ›› Issue (08): 3852-3865.DOI: 10.16085/j.issn.1000-6613.2018-2097
程运1(),王昕晔1(),吕文婷1,黄亚继2,谢浩1,3,郭若军4,朴桂林1
收稿日期:
2018-10-24
出版日期:
2019-08-05
发布日期:
2019-08-05
通讯作者:
王昕晔
作者简介:
程运(1995—),男,硕士研究生,研究方向为重金属高温吸附技术。E-mail:基金资助:
Yun CHENG1(),Xinye WANG1(),Wenting LÜ1,Yaji HUANG2,Hao XIE1,3,Ruojun GUO4,Guilin PIAO1
Received:
2018-10-24
Online:
2019-08-05
Published:
2019-08-05
Contact:
Xinye WANG
摘要:
高岭土在高温下对碱金属和重金属具有吸附能力,可以解决煤、生物质和垃圾等在燃烧、气化等过程中产生的结渣、积灰、腐蚀以及重金属和超细颗粒物排放等问题。国内外学者已对此进行了长期研究,但仍存在相关的难度和问题,因此本文从高岭土高温结构特征、研究方法、高温吸附机理、高温吸附技术应用效果以及高岭土改性等5个方面介绍了相关重要成果,并结合前人研究成果和作者自身的研究经验,提出了本领域研究的展望。指出缺乏简便而准确的金属蒸气定量发生装置和在线检测装置严重阻碍了高岭土高温吸附的试验研究,亟待开发出对应的新方法或新设备;高岭土高温吸附的同时其结构因为高温也在发生畸变,掌握其中的关联是理解高温吸附行为的关键之一;烟气组分对吸附的影响研究仍不充分,因此目前无法形成复杂烟气组分下的高岭土高温吸附行为规律和数学描述;技术应用过程中,高岭土添加量较大(通常大于3%),可能对燃烧或气化工艺产生不良影响,抑制了其工业应用;高岭土改性是提升吸附效率、降低高岭土用量的有效方法,改性工艺仍有待深入研究,但因为吸附后高岭土难以分离回收和循环再生,改性成本必须低。
中图分类号:
程运,王昕晔,吕文婷,黄亚继,谢浩,郭若军,朴桂林. 高岭土高温吸附重金属和碱金属的研究进展[J]. 化工进展, 2019, 38(08): 3852-3865.
Yun CHENG,Xinye WANG,Wenting LÜ,Yaji HUANG,Hao XIE,Ruojun GUO,Guilin PIAO. A review on heavy and alkali metals adsorption by kaolin athigh temperature[J]. Chemical Industry and Engineering Progress, 2019, 38(08): 3852-3865.
温度/℃ | 加热速率/℃·s-1 | 停留时间 | 脱羟基率/% | 气氛 | 参考文献 |
---|---|---|---|---|---|
450 500 550 550 700 1000 1200 1000 900 1050 1200 | 缓慢煅烧 缓慢煅烧 缓慢煅烧 闪煅 4700 4700 4700 4700 15000 15000 15000 | 2 h 2 h 2 h 0.54 s 0.5 s 0.5 s 0.5 s 1.5 s 0.5 s 0.5 s 0.5 s | 16 63 71 15 16 41 30 81 59 80 87 | 空气 空气 空气 空气 氦气 氮气 氦气 氮气 氦气 氮气 氦气 | [ [ [ [ [ [ [ [ [ [ [ |
表1 高岭土脱羟基的动力学数据
温度/℃ | 加热速率/℃·s-1 | 停留时间 | 脱羟基率/% | 气氛 | 参考文献 |
---|---|---|---|---|---|
450 500 550 550 700 1000 1200 1000 900 1050 1200 | 缓慢煅烧 缓慢煅烧 缓慢煅烧 闪煅 4700 4700 4700 4700 15000 15000 15000 | 2 h 2 h 2 h 0.54 s 0.5 s 0.5 s 0.5 s 1.5 s 0.5 s 0.5 s 0.5 s | 16 63 71 15 16 41 30 81 59 80 87 | 空气 空气 空气 空气 氦气 氮气 氦气 氮气 氦气 氮气 氦气 | [ [ [ [ [ [ [ [ [ [ [ |
固体燃料 | 炉型 | 燃烧温度/℃ | 减排对象 | 高岭土添加量占固体燃料的质量分数/% | 排放控制效率/% | 参考文献 |
---|---|---|---|---|---|---|
干污泥颗粒 | 沉降炉 | 800 | 亚微米Pb/亚微米Cd | 5 | 约10/约10 | [ |
875 | 约22/约17 | |||||
950 | 51/40 | |||||
煤粉 | 沉降炉 | 1500 | PM0.2 | 3 | 17 | [ |
1000MW | — | PM0.3 | 2.5 | 56 | [ | |
PM2.5 | 6 | |||||
富钾煤 | 沉降炉 | 900 | PM1 | 11 | 23 | [ |
1100 | 38 | |||||
1300 | 5 | |||||
添加重金属的木屑 | 流化床 | 850 | 亚微米Pb/亚微米Cd | 1 | 25/1 | [ |
3 | 42/4 | |||||
5 | 43/8 | |||||
950 | 1 | 50/11 | [ | |||
3 | 60/12 | |||||
5 | 61/10 |
表2 燃烧条件下高岭土高温控制排放的效果
固体燃料 | 炉型 | 燃烧温度/℃ | 减排对象 | 高岭土添加量占固体燃料的质量分数/% | 排放控制效率/% | 参考文献 |
---|---|---|---|---|---|---|
干污泥颗粒 | 沉降炉 | 800 | 亚微米Pb/亚微米Cd | 5 | 约10/约10 | [ |
875 | 约22/约17 | |||||
950 | 51/40 | |||||
煤粉 | 沉降炉 | 1500 | PM0.2 | 3 | 17 | [ |
1000MW | — | PM0.3 | 2.5 | 56 | [ | |
PM2.5 | 6 | |||||
富钾煤 | 沉降炉 | 900 | PM1 | 11 | 23 | [ |
1100 | 38 | |||||
1300 | 5 | |||||
添加重金属的木屑 | 流化床 | 850 | 亚微米Pb/亚微米Cd | 1 | 25/1 | [ |
3 | 42/4 | |||||
5 | 43/8 | |||||
950 | 1 | 50/11 | [ | |||
3 | 60/12 | |||||
5 | 61/10 |
用途 | 煅烧温度 | 原理 |
---|---|---|
合成分子筛和铝盐化工 | 700℃左右 | 低温煅烧生成的偏高岭土活性高,有利于硅铝酸盐合成分子筛 |
PVC电缆料配料 | <850℃ | 增加高岭土孔隙,增强复合材料电绝缘性能 |
造纸填料和涂料添加成分 | 1000℃左右 | 去除高岭土中杂质碳增加白度,增加孔隙率增强其吸油性能 |
耐火材料填料、玻璃钢增强填料、陶瓷窑具和高级陶瓷胚料的配料以及精密铸件模型 | 1300~1525℃ | 高温后向稳定的莫来石转变 |
表3 不同用途下的高岭土煅烧温度及其原理[87,88]
用途 | 煅烧温度 | 原理 |
---|---|---|
合成分子筛和铝盐化工 | 700℃左右 | 低温煅烧生成的偏高岭土活性高,有利于硅铝酸盐合成分子筛 |
PVC电缆料配料 | <850℃ | 增加高岭土孔隙,增强复合材料电绝缘性能 |
造纸填料和涂料添加成分 | 1000℃左右 | 去除高岭土中杂质碳增加白度,增加孔隙率增强其吸油性能 |
耐火材料填料、玻璃钢增强填料、陶瓷窑具和高级陶瓷胚料的配料以及精密铸件模型 | 1300~1525℃ | 高温后向稳定的莫来石转变 |
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