化工进展 ›› 2021, Vol. 40 ›› Issue (10): 5293-5301.DOI: 10.16085/j.issn.1000-6613.2021-0800
收稿日期:
2021-04-15
修回日期:
2021-05-27
出版日期:
2021-10-10
发布日期:
2021-10-25
通讯作者:
杨骥
作者简介:
曹礼梅(1982—),女,副教授,研究方向为工业废气污染控制、固体废弃物处置。E-mail:基金资助:
CAO Limei(), QIU Zhaofu, ZHANG Wei, YANG Ji()
Received:
2021-04-15
Revised:
2021-05-27
Online:
2021-10-10
Published:
2021-10-25
Contact:
YANG Ji
摘要:
全世界化工行业每年会置换出大量的废催化剂,如处置不当,不仅污染环境,而且浪费了资源。本文对化工行业废催化剂的现状进行了初步调查分析,综述了其来源、类别及特点。基于废催化剂中有价金属的含量远远高于矿藏中所含有的相应组分的特点,建议将其作为二次资源进行利用;分析了化工废催化剂潜在的环境风险并提出了开展环境风险评价的流程,建议建立废催化剂环境风险信息数据库;概括论述了废催化剂减量化、资源化、无害化等的控制手段及存在的问题。文中提出:对于化工废催化剂的处理处置应从清洁生产的角度考虑,不局限于单纯的末端污染控制;建议开展废催化剂减量化、资源化及无害化处理的绿色新技术,达到减少污染、资源综合回收利用的目的。
中图分类号:
曹礼梅, 邱兆富, 张巍, 杨骥. 化工废催化剂污染特征及资源化途径[J]. 化工进展, 2021, 40(10): 5293-5301.
CAO Limei, QIU Zhaofu, ZHANG Wei, YANG Ji. Pollution and utilization of chemical industry spent catalysts[J]. Chemical Industry and Engineering Progress, 2021, 40(10): 5293-5301.
名称 | 生产工艺 | 所用催化剂 | 废催化剂成分 | 废催化剂处置 | 废催化剂产量 | 参考 文献 |
---|---|---|---|---|---|---|
甲醇 | 低压工艺 | 铜锌系催化剂 | ZnO 39.29%, CuO 39.04% | 湿法回收铜锌 | 3000t | [ |
甲基叔丁基醚(MTB) | 异丁烯、甲醇催化 | 苯乙烯-二乙烯苯共聚物 | Na+ 64%,Fe2+ 32%,Ca2+和Mg2+ 3% | 填埋 | 350t | [ |
硫酸 | 催化吸收制备硫酸 | V2O5等钒类催化剂 | V 7.5%,K 9.1%,S 10.2%,Si 23.2% | 回收V2O5 | 4500t | [ |
丙烯腈 | 丙烯氨氧化 | 磷钼铋系或锑铁系催化剂 | Bi 1%~5%,Ni 1%~10%,Mo 5%~21% | 湿法回收 | 115t | [ |
苯胺 | 硝基苯催化加氢法 | 铜/硅、镍或铂/钯为催化剂 | Cu 15%~25% | 湿法回收 | 150t | [ |
邻甲酚 | 甲苯氯化水解法 | 钒系催化剂 | V2O5 | 湿法回收 | 100t | [ |
表1 典型化工废催化剂组成与数量
名称 | 生产工艺 | 所用催化剂 | 废催化剂成分 | 废催化剂处置 | 废催化剂产量 | 参考 文献 |
---|---|---|---|---|---|---|
甲醇 | 低压工艺 | 铜锌系催化剂 | ZnO 39.29%, CuO 39.04% | 湿法回收铜锌 | 3000t | [ |
甲基叔丁基醚(MTB) | 异丁烯、甲醇催化 | 苯乙烯-二乙烯苯共聚物 | Na+ 64%,Fe2+ 32%,Ca2+和Mg2+ 3% | 填埋 | 350t | [ |
硫酸 | 催化吸收制备硫酸 | V2O5等钒类催化剂 | V 7.5%,K 9.1%,S 10.2%,Si 23.2% | 回收V2O5 | 4500t | [ |
丙烯腈 | 丙烯氨氧化 | 磷钼铋系或锑铁系催化剂 | Bi 1%~5%,Ni 1%~10%,Mo 5%~21% | 湿法回收 | 115t | [ |
苯胺 | 硝基苯催化加氢法 | 铜/硅、镍或铂/钯为催化剂 | Cu 15%~25% | 湿法回收 | 150t | [ |
邻甲酚 | 甲苯氯化水解法 | 钒系催化剂 | V2O5 | 湿法回收 | 100t | [ |
方法类别 | 优点 | 缺点 |
---|---|---|
火法 | 工艺简单、回收率高 | (1)焚烧过程会产生大量有害气体形成二次污染; (2)排放大量浮渣,增加了二次固废的产生,部分金属被废弃; (3)其他有色金属回收率较低; (4)能耗大,处理设备昂贵,经济效益低 |
湿法 | 能耗低、工艺过程易监控、贵金属沉淀易进行 | (1)产生的废水和残渣数量过大; (2)面临浸出过的载体处置问题; (3)贵金属富集浓度较低 |
表3 废催化剂中贵金属回收方法的优缺点
方法类别 | 优点 | 缺点 |
---|---|---|
火法 | 工艺简单、回收率高 | (1)焚烧过程会产生大量有害气体形成二次污染; (2)排放大量浮渣,增加了二次固废的产生,部分金属被废弃; (3)其他有色金属回收率较低; (4)能耗大,处理设备昂贵,经济效益低 |
湿法 | 能耗低、工艺过程易监控、贵金属沉淀易进行 | (1)产生的废水和残渣数量过大; (2)面临浸出过的载体处置问题; (3)贵金属富集浓度较低 |
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