Chemical Industry and Engineering Progress ›› 2024, Vol. 43 ›› Issue (7): 4102-4117.DOI: 10.16085/j.issn.1000-6613.2024-0075
• Resources and environmental engineering • Previous Articles
KONG Xiangrui1,2(), DONG Yuecen2, ZHANG Mengyu3, WANG Biao4, YIN Shui′e3, CHEN Bing3, LU Jiawei3, ZHANG Yuan3, FENG Lele4(), WANG Hongtao2, XU Haiyun3()
Received:
2024-01-11
Revised:
2024-03-01
Online:
2024-08-14
Published:
2024-07-10
Contact:
FENG Lele, XU Haiyun
孔祥蕊1,2(), 董玥岑2, 张蒙雨3, 王彪4, 尹水娥3, 陈冰3, 陆家纬3, 张媛3, 冯乐乐4(), 王洪涛2, 徐海云3()
通讯作者:
冯乐乐,徐海云
作者简介:
孔祥蕊(1996—),女,博士,研究方向为固体废物处置。E-mail:kongxiangrui121@mail.tsinghua.edu.cn。
基金资助:
CLC Number:
KONG Xiangrui, DONG Yuecen, ZHANG Mengyu, WANG Biao, YIN Shui′e, CHEN Bing, LU Jiawei, ZHANG Yuan, FENG Lele, WANG Hongtao, XU Haiyun. Treatment technologies of fly ash from municipal solid waste incineration[J]. Chemical Industry and Engineering Progress, 2024, 43(7): 4102-4117.
孔祥蕊, 董玥岑, 张蒙雨, 王彪, 尹水娥, 陈冰, 陆家纬, 张媛, 冯乐乐, 王洪涛, 徐海云. 生活垃圾焚烧飞灰处理技术研究进展[J]. 化工进展, 2024, 43(7): 4102-4117.
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地点 | 炉型 | 集中粒径/μm | CaO/% | SiO2/% | K2O/% | Al2O3/% | Fe2O3/% | Na2O/% | Cl/% | SO3/% | 参考文献 |
---|---|---|---|---|---|---|---|---|---|---|---|
国内 | |||||||||||
浙江 | 流化床 | — | 29.38 | 32.79 | — | 10.97 | 10.88 | — | 17.44 | — | [ |
山东 | 炉排炉 | — | 45.52 | 1.28 | 10.85 | 0.56 | 1.05 | 13.73 | 16.17 | 5 | [ |
山东 | 炉排炉 | — | 52.67 | 1.14 | 7.93 | 0.69 | 0.63 | 13.62 | 11.09 | 5.58 | |
山东 | 炉排炉 | — | 61.49 | 2.67 | 5.07 | 0.56 | 1.92 | 1.18 | 17.7 | 5.97 | |
浙江 | 炉排炉 | — | 74.11 | 2.91 | 1.74 | 0.68 | 1.13 | 0.34 | 11.56 | 4.66 | |
浙江 | 炉排炉 | — | 45.11 | 1.53 | 1.81 | 0.26 | 28.2 | — | 2.82 | 3.31 | |
上海 | 炉排炉 | — | 57.88 | 1.76 | 4.61 | 0.26 | 0.88 | 1.37 | 25.01 | 4.62 | |
四川 | 炉排炉 | — | 61.86 | 2.07 | 4.98 | 0.48 | 0.9 | 0.81 | 15.93 | 10 | |
江苏 | 炉排炉 | — | 56 | 3.71 | 5.12 | 1.19 | 2.75 | 1.6 | 19.92 | 5.27 | |
浙江 | 炉排炉 | 75~2000 | 34.39 | 3.42 | 7.71 | 2.58 | 1.85 | 11.38 | 24.31 | 5.33 | [ |
浙江 | 流化床 | 5~75 | 44.07 | 9.82 | 3.19 | 9.85 | 5.47 | 3.99 | 10.32 | 2.89 | |
上海 | 炉排炉 | 38~75 | 41.38 | 3.44 | 6.15 | 0.66 | 0.52 | 13.4 | 26.07 | 5.31 | [ |
山东 | 炉排炉 | — | 52.42 | 2.84 | 5.3 | 0.88 | 0.92 | 5.09 | 22.26 | 6.3 | [ |
北京 | 炉排炉 | — | 42.81 | 6.78 | 6.41 | 2.96 | 0.96 | 6.19 | 14.83 | 5.01 | [ |
北京 | 炉排炉 | 56.38 | 32.46 | 3.27 | 8.46 | 0.802 | 0.649 | 11.34 | 35.21 | 4.38 | [ |
河南 | 炉排炉 | 108.8 | 38.4 | 6.6 | 6.09 | 2.25 | 1.75 | 9.44 | 26.62 | 4.74 | |
贵州 | 炉排炉 | 64.84 | 52.13 | 2.52 | 5.17 | 1.06 | 1.14 | 10.06 | 21.78 | 3.22 | |
辽宁 | 炉排炉 | 55.16 | 36.72 | 3.17 | 7.01 | 0.727 | 0.65 | 16.47 | 27.23 | 4.59 | |
天津 | 流化床 | 70.95 | 38.16 | 8.59 | 3.88 | 7.61 | 1.68 | 12.27 | 16.37 | 2.99 | |
重庆 | 炉排炉 | 2~100 | 55.08 | 3.97 | 4.23 | 1.2 | 2.28 | 2.74 | 16.95 | 6.92 | [ |
天津 | 炉排炉 | 2~100 | 52.7 | 6.34 | 3.42 | 2.7 | 2.77 | 2.52 | 10.51 | 7.06 | |
天津 | 炉排炉 | — | 41.7 | 2.27 | 7.69 | 0.72 | 0.49 | 12.9 | 24.2 | 7.54 | [ |
山西 | 流化床 | — | 30.09 | 17.91 | 2.35 | 11.9 | 4.4 | 1.26 | 5.23 | 5.45 | [ |
云南 | 炉排炉 | 10~176 | 36.727 | 21.926 | 1.383 | 8.525 | 9.349 | 1.969 | 2.658 | 3.779 | [ |
江苏 | 炉排炉 | — | 42.71 | 5.63 | 6.16 | 2.47 | — | — | 23.41 | 10.6 | [ |
辽宁 | 炉排炉 | — | 45.25 | 2.12 | 8.15 | 2.36 | 0.75 | 9.94 | 21.48 | 8.55 | [ |
广东 | 炉排炉 | 50~280 | 30.57 | 15.92 | 4.18 | 5.74 | 2.26 | 4.49 | 14.1 | 6.91 | [ |
广东 | 炉排炉 | 2~100 | 26.87 | 5.22 | 10.04 | — | — | 9.84 | 20.96 | 11 | [ |
国外 | |||||||||||
瑞典 | 流化床 | — | 40.6 | 6 | 2.4 | 4.5 | 1.7 | 6.2 | 12 | 8.7 | [ |
新加坡 | 炉排炉 | — | 58.79 | 4.71 | 4.66 | — | 2.63 | — | 20.94 | 3.96 | [ |
丹麦 | 炉排炉 | — | 21 | 4.9 | 13.3 | 2.3 | 1.1 | 17.5 | 8.9 | 22.5 | [ |
韩国 | 炉排炉 | — | 41.64 | 3.22 | 6.65 | 1.38 | 0.57 | 9.41 | — | — | [ |
地点 | 炉型 | 集中粒径/μm | CaO/% | SiO2/% | K2O/% | Al2O3/% | Fe2O3/% | Na2O/% | Cl/% | SO3/% | 参考文献 |
---|---|---|---|---|---|---|---|---|---|---|---|
国内 | |||||||||||
浙江 | 流化床 | — | 29.38 | 32.79 | — | 10.97 | 10.88 | — | 17.44 | — | [ |
山东 | 炉排炉 | — | 45.52 | 1.28 | 10.85 | 0.56 | 1.05 | 13.73 | 16.17 | 5 | [ |
山东 | 炉排炉 | — | 52.67 | 1.14 | 7.93 | 0.69 | 0.63 | 13.62 | 11.09 | 5.58 | |
山东 | 炉排炉 | — | 61.49 | 2.67 | 5.07 | 0.56 | 1.92 | 1.18 | 17.7 | 5.97 | |
浙江 | 炉排炉 | — | 74.11 | 2.91 | 1.74 | 0.68 | 1.13 | 0.34 | 11.56 | 4.66 | |
浙江 | 炉排炉 | — | 45.11 | 1.53 | 1.81 | 0.26 | 28.2 | — | 2.82 | 3.31 | |
上海 | 炉排炉 | — | 57.88 | 1.76 | 4.61 | 0.26 | 0.88 | 1.37 | 25.01 | 4.62 | |
四川 | 炉排炉 | — | 61.86 | 2.07 | 4.98 | 0.48 | 0.9 | 0.81 | 15.93 | 10 | |
江苏 | 炉排炉 | — | 56 | 3.71 | 5.12 | 1.19 | 2.75 | 1.6 | 19.92 | 5.27 | |
浙江 | 炉排炉 | 75~2000 | 34.39 | 3.42 | 7.71 | 2.58 | 1.85 | 11.38 | 24.31 | 5.33 | [ |
浙江 | 流化床 | 5~75 | 44.07 | 9.82 | 3.19 | 9.85 | 5.47 | 3.99 | 10.32 | 2.89 | |
上海 | 炉排炉 | 38~75 | 41.38 | 3.44 | 6.15 | 0.66 | 0.52 | 13.4 | 26.07 | 5.31 | [ |
山东 | 炉排炉 | — | 52.42 | 2.84 | 5.3 | 0.88 | 0.92 | 5.09 | 22.26 | 6.3 | [ |
北京 | 炉排炉 | — | 42.81 | 6.78 | 6.41 | 2.96 | 0.96 | 6.19 | 14.83 | 5.01 | [ |
北京 | 炉排炉 | 56.38 | 32.46 | 3.27 | 8.46 | 0.802 | 0.649 | 11.34 | 35.21 | 4.38 | [ |
河南 | 炉排炉 | 108.8 | 38.4 | 6.6 | 6.09 | 2.25 | 1.75 | 9.44 | 26.62 | 4.74 | |
贵州 | 炉排炉 | 64.84 | 52.13 | 2.52 | 5.17 | 1.06 | 1.14 | 10.06 | 21.78 | 3.22 | |
辽宁 | 炉排炉 | 55.16 | 36.72 | 3.17 | 7.01 | 0.727 | 0.65 | 16.47 | 27.23 | 4.59 | |
天津 | 流化床 | 70.95 | 38.16 | 8.59 | 3.88 | 7.61 | 1.68 | 12.27 | 16.37 | 2.99 | |
重庆 | 炉排炉 | 2~100 | 55.08 | 3.97 | 4.23 | 1.2 | 2.28 | 2.74 | 16.95 | 6.92 | [ |
天津 | 炉排炉 | 2~100 | 52.7 | 6.34 | 3.42 | 2.7 | 2.77 | 2.52 | 10.51 | 7.06 | |
天津 | 炉排炉 | — | 41.7 | 2.27 | 7.69 | 0.72 | 0.49 | 12.9 | 24.2 | 7.54 | [ |
山西 | 流化床 | — | 30.09 | 17.91 | 2.35 | 11.9 | 4.4 | 1.26 | 5.23 | 5.45 | [ |
云南 | 炉排炉 | 10~176 | 36.727 | 21.926 | 1.383 | 8.525 | 9.349 | 1.969 | 2.658 | 3.779 | [ |
江苏 | 炉排炉 | — | 42.71 | 5.63 | 6.16 | 2.47 | — | — | 23.41 | 10.6 | [ |
辽宁 | 炉排炉 | — | 45.25 | 2.12 | 8.15 | 2.36 | 0.75 | 9.94 | 21.48 | 8.55 | [ |
广东 | 炉排炉 | 50~280 | 30.57 | 15.92 | 4.18 | 5.74 | 2.26 | 4.49 | 14.1 | 6.91 | [ |
广东 | 炉排炉 | 2~100 | 26.87 | 5.22 | 10.04 | — | — | 9.84 | 20.96 | 11 | [ |
国外 | |||||||||||
瑞典 | 流化床 | — | 40.6 | 6 | 2.4 | 4.5 | 1.7 | 6.2 | 12 | 8.7 | [ |
新加坡 | 炉排炉 | — | 58.79 | 4.71 | 4.66 | — | 2.63 | — | 20.94 | 3.96 | [ |
丹麦 | 炉排炉 | — | 21 | 4.9 | 13.3 | 2.3 | 1.1 | 17.5 | 8.9 | 22.5 | [ |
韩国 | 炉排炉 | — | 41.64 | 3.22 | 6.65 | 1.38 | 0.57 | 9.41 | — | — | [ |
地点 | 炉型 | PCDDs/ng·g-1 | PCDFs/ng·g-1 | PCDDs/PCDFs比值 | dl-PCBs/ng·g-1 | TEQ毒性当量/ng·g-1 | 参考文献 |
---|---|---|---|---|---|---|---|
国内 | |||||||
吉林 | 流化床 | 1.1 | 1.6 | 0.69 | 0.095 | 0.034 | [ |
北京 | 炉排炉 | 10 | 31 | 0.32 | 0.5 | 0.55 | |
山东 | 流化床 | 51 | 79 | 0.65 | 2.3 | 1.8 | |
江苏 | 炉排炉 | 38 | 24 | 1.58 | 1.4 | 0.71 | |
江苏 | 炉排炉 | 7.3 | 17 | 0.43 | 0.55 | 0.44 | |
上海 | 炉排炉 | 39 | 16 | 2.44 | 0.37 | 0.56 | |
上海 | 炉排炉 | 26 | 24 | 1.08 | 1.5 | 0.64 | |
浙江 | 流化床 | 27 | 52 | 0.52 | 2.1 | 1.3 | |
重庆 | 炉排炉 | 28 | 35 | 0.80 | 1.7 | 1 | |
四川 | 炉排炉 | 3.3 | 8.1 | 0.41 | 0.18 | 0.21 | |
福建 | 炉排炉 | 5.6 | 4.2 | 1.33 | 0.21 | 0.11 | |
广东 | 流化床 | 100 | 73 | 1.37 | 9.3 | 2.5 | |
广东 | 炉排炉 | 10 | 17 | 0.59 | 0.36 | 0.44 | |
福建 | 炉排炉 | 59 | 34 | 1.74 | 2.9 | 1 | |
浙江 | 流化床 | 2.384 | 9.21 4 | 0.26 | — | 0.234 | [ |
浙江 | 流化床 | 0.717 | 0.951 | 0.75 | — | 0.058 | [ |
浙江 | 炉排炉 | 0.32 | 1.118 | 0.29 | — | 0.048 | |
国外 | |||||||
法国 | 炉排炉 | 99.48 | 92.55 | 1.07 | — | 6.83 | [ |
日本 | 炉排炉 | 54 | 86 | 0.63 | — | 3.3 | [ |
韩国 | 炉排炉 | 80 | 30 | 2.67 | — | 3.35 | [ |
地点 | 炉型 | PCDDs/ng·g-1 | PCDFs/ng·g-1 | PCDDs/PCDFs比值 | dl-PCBs/ng·g-1 | TEQ毒性当量/ng·g-1 | 参考文献 |
---|---|---|---|---|---|---|---|
国内 | |||||||
吉林 | 流化床 | 1.1 | 1.6 | 0.69 | 0.095 | 0.034 | [ |
北京 | 炉排炉 | 10 | 31 | 0.32 | 0.5 | 0.55 | |
山东 | 流化床 | 51 | 79 | 0.65 | 2.3 | 1.8 | |
江苏 | 炉排炉 | 38 | 24 | 1.58 | 1.4 | 0.71 | |
江苏 | 炉排炉 | 7.3 | 17 | 0.43 | 0.55 | 0.44 | |
上海 | 炉排炉 | 39 | 16 | 2.44 | 0.37 | 0.56 | |
上海 | 炉排炉 | 26 | 24 | 1.08 | 1.5 | 0.64 | |
浙江 | 流化床 | 27 | 52 | 0.52 | 2.1 | 1.3 | |
重庆 | 炉排炉 | 28 | 35 | 0.80 | 1.7 | 1 | |
四川 | 炉排炉 | 3.3 | 8.1 | 0.41 | 0.18 | 0.21 | |
福建 | 炉排炉 | 5.6 | 4.2 | 1.33 | 0.21 | 0.11 | |
广东 | 流化床 | 100 | 73 | 1.37 | 9.3 | 2.5 | |
广东 | 炉排炉 | 10 | 17 | 0.59 | 0.36 | 0.44 | |
福建 | 炉排炉 | 59 | 34 | 1.74 | 2.9 | 1 | |
浙江 | 流化床 | 2.384 | 9.21 4 | 0.26 | — | 0.234 | [ |
浙江 | 流化床 | 0.717 | 0.951 | 0.75 | — | 0.058 | [ |
浙江 | 炉排炉 | 0.32 | 1.118 | 0.29 | — | 0.048 | |
国外 | |||||||
法国 | 炉排炉 | 99.48 | 92.55 | 1.07 | — | 6.83 | [ |
日本 | 炉排炉 | 54 | 86 | 0.63 | — | 3.3 | [ |
韩国 | 炉排炉 | 80 | 30 | 2.67 | — | 3.35 | [ |
地点 | 炉型 | Pb/mg·kg-1 | Cr/mg·kg-1 | Cd/mg·kg-1 | Ni/mg·kg-1 | Cu/mg·kg-1 | Zn/mg·kg-1 | 参考文献 |
---|---|---|---|---|---|---|---|---|
国内 | ||||||||
浙江 | 流化床 | 493.75 | 311.09 | 11.36 | 78.38 | 588.16 | 2265.04 | [ |
山东 | 炉排炉 | 1239 | 89 | 184 | 22 | 563 | 4716 | [ |
山东 | 炉排炉 | 922 | 42 | 152 | 11 | 376 | 4325 | |
山东 | 炉排炉 | 720 | 85 | 65 | 25 | 400 | 2420 | |
浙江 | 炉排炉 | 635 | 50 | 65 | 10 | 350 | 2985 | |
浙江 | 炉排炉 | 710 | 480 | 25 | 125 | 750 | 4715 | |
上海 | 炉排炉 | 1115 | 35 | 75 | 15 | 435 | 4650 | |
四川 | 炉排炉 | 980 | 70 | 140 | 15 | 280 | 4490 | |
江苏 | 炉排炉 | 720 | 140 | 75 | 55 | 575 | 2595 | |
浙江 | 炉排炉 | 1310.8 | 147.7 | 127.8 | 46 | 901.2 | 4582 | [ |
浙江 | 流化床 | 1343.5 | 296.5 | 60 | 53.6 | 1438.9 | 9411.2 | |
上海 | 炉排炉 | 4039 | 140.4 | 267.1 | — | 694.4 | 7714.8 | [ |
山东 | 炉排炉 | 2120 | — | 220 | — | — | — | [ |
浙江 | 炉排炉 | 1830 | 229 | 191 | 44.1 | 757 | 7640 | [ |
浙江 | 流化床 | 1604 | 767.8 | 71.75 | 299.7 | 4084 | 9782 | |
山西 | 流化床 | 677.4 | — | 60.9 | — | 1070.2 | 1166.3 | [ |
安徽 | 流化床 | 1063.35 | 468.04 | 77.38 | 145.61 | 2237.22 | 6305.25 | [ |
江苏 | 炉排炉 | 1647.26 | 40.7 | 280.3 | 24.23 | 626.8 | 6803.43 | |
西藏 | 炉排炉 | 1578 | 57.4 | 107.4 | 25.4 | 561 | 3842 | [ |
黑龙江 | 流化床 | 715 | 307 | 107 | 114 | 1122 | 5664 | [ |
黑龙江 | 炉排炉 | 1653 | 221 | 424 | 62 | 872 | 6532 | |
江苏 | 炉排炉 | 2622 | 787 | 111 | — | 950 | 4803 | [ |
辽宁 | 炉排炉 | 924 | 50 | 172 | 36 | 506 | 4516 | [ |
广东 | 炉排炉 | 1700 | — | — | 40 | 860 | 4900 | [ |
国外 | ||||||||
瑞典 | 流化床 | 5730 | 190 | 90 | 30 | 5400 | 5780 | [ |
瑞典 | 流化床 | 3630 | 23.1 | 62.7 | — | 6940 | 6860 | [ |
挪威 | 炉排炉 | 2900 | 500 | 200 | — | 1200 | 15900 | [ |
日本 | 流化床 | 1274 | 192 | 17 | — | 3517 | 5029 | [ |
奥地利 | 炉排炉 | 2300 | 190 | 180 | — | 780 | 13000 | [ |
瑞士 | 炉排炉 | 9540 | 650 | 227 | — | 3901 | 26770 | [ |
丹麦 | 炉排炉 | 6250 | 126 | 280 | — | 1070 | 34690 | [ |
地点 | 炉型 | Pb/mg·kg-1 | Cr/mg·kg-1 | Cd/mg·kg-1 | Ni/mg·kg-1 | Cu/mg·kg-1 | Zn/mg·kg-1 | 参考文献 |
---|---|---|---|---|---|---|---|---|
国内 | ||||||||
浙江 | 流化床 | 493.75 | 311.09 | 11.36 | 78.38 | 588.16 | 2265.04 | [ |
山东 | 炉排炉 | 1239 | 89 | 184 | 22 | 563 | 4716 | [ |
山东 | 炉排炉 | 922 | 42 | 152 | 11 | 376 | 4325 | |
山东 | 炉排炉 | 720 | 85 | 65 | 25 | 400 | 2420 | |
浙江 | 炉排炉 | 635 | 50 | 65 | 10 | 350 | 2985 | |
浙江 | 炉排炉 | 710 | 480 | 25 | 125 | 750 | 4715 | |
上海 | 炉排炉 | 1115 | 35 | 75 | 15 | 435 | 4650 | |
四川 | 炉排炉 | 980 | 70 | 140 | 15 | 280 | 4490 | |
江苏 | 炉排炉 | 720 | 140 | 75 | 55 | 575 | 2595 | |
浙江 | 炉排炉 | 1310.8 | 147.7 | 127.8 | 46 | 901.2 | 4582 | [ |
浙江 | 流化床 | 1343.5 | 296.5 | 60 | 53.6 | 1438.9 | 9411.2 | |
上海 | 炉排炉 | 4039 | 140.4 | 267.1 | — | 694.4 | 7714.8 | [ |
山东 | 炉排炉 | 2120 | — | 220 | — | — | — | [ |
浙江 | 炉排炉 | 1830 | 229 | 191 | 44.1 | 757 | 7640 | [ |
浙江 | 流化床 | 1604 | 767.8 | 71.75 | 299.7 | 4084 | 9782 | |
山西 | 流化床 | 677.4 | — | 60.9 | — | 1070.2 | 1166.3 | [ |
安徽 | 流化床 | 1063.35 | 468.04 | 77.38 | 145.61 | 2237.22 | 6305.25 | [ |
江苏 | 炉排炉 | 1647.26 | 40.7 | 280.3 | 24.23 | 626.8 | 6803.43 | |
西藏 | 炉排炉 | 1578 | 57.4 | 107.4 | 25.4 | 561 | 3842 | [ |
黑龙江 | 流化床 | 715 | 307 | 107 | 114 | 1122 | 5664 | [ |
黑龙江 | 炉排炉 | 1653 | 221 | 424 | 62 | 872 | 6532 | |
江苏 | 炉排炉 | 2622 | 787 | 111 | — | 950 | 4803 | [ |
辽宁 | 炉排炉 | 924 | 50 | 172 | 36 | 506 | 4516 | [ |
广东 | 炉排炉 | 1700 | — | — | 40 | 860 | 4900 | [ |
国外 | ||||||||
瑞典 | 流化床 | 5730 | 190 | 90 | 30 | 5400 | 5780 | [ |
瑞典 | 流化床 | 3630 | 23.1 | 62.7 | — | 6940 | 6860 | [ |
挪威 | 炉排炉 | 2900 | 500 | 200 | — | 1200 | 15900 | [ |
日本 | 流化床 | 1274 | 192 | 17 | — | 3517 | 5029 | [ |
奥地利 | 炉排炉 | 2300 | 190 | 180 | — | 780 | 13000 | [ |
瑞士 | 炉排炉 | 9540 | 650 | 227 | — | 3901 | 26770 | [ |
丹麦 | 炉排炉 | 6250 | 126 | 280 | — | 1070 | 34690 | [ |
处理技术 | 优点 | 缺点 |
---|---|---|
高温烧结 | 减容效果好,运行条件与高温熔融相比简单 | 烧结过程会产生重金属烟气,产生二次飞灰,成本较高,能耗较高 |
高温熔融/玻璃化 | 减容效果好,降低重金属浸出 | 能耗高,工艺流程复杂,熔融过程会产生烟气 |
水泥回转窑热处理 | 技术较成熟,标准体系较完善 | 需要与水泥窑协同处置,前端水洗工艺增加成本,水泥产品出路 |
低温催化热解 | 能耗较低 | 技术不够成熟,流程比较复杂 |
水热处理 | 操作简单,工艺流程简单 | 能耗高,废液再处理,规模化比较困难 |
机械化学 | 反应条件温和,工艺流程简单 | 能耗高,规模化比较困难 |
处理技术 | 优点 | 缺点 |
---|---|---|
高温烧结 | 减容效果好,运行条件与高温熔融相比简单 | 烧结过程会产生重金属烟气,产生二次飞灰,成本较高,能耗较高 |
高温熔融/玻璃化 | 减容效果好,降低重金属浸出 | 能耗高,工艺流程复杂,熔融过程会产生烟气 |
水泥回转窑热处理 | 技术较成熟,标准体系较完善 | 需要与水泥窑协同处置,前端水洗工艺增加成本,水泥产品出路 |
低温催化热解 | 能耗较低 | 技术不够成熟,流程比较复杂 |
水热处理 | 操作简单,工艺流程简单 | 能耗高,废液再处理,规模化比较困难 |
机械化学 | 反应条件温和,工艺流程简单 | 能耗高,规模化比较困难 |
处理技术 | 优点 | 缺点 |
---|---|---|
固化稳定化 | 成本低,流程简单 | 对多种重金属的固化效果普适性较差,长期容易浸出,对二𫫇英没有去除效果,增大体积 |
固热处理 | 减容效果好,对多种重金属的适用性强 | 能耗高,成本高,工艺流程复杂,产生烟气和二次飞灰 |
金属热分离 | 对多种金属的分离效率均较高 | 能耗高,处理后飞灰与添加剂分离问题,产生烟气处理 |
金属化学浸出与电化学分离 | 国外技术较成熟,分离回收效率高 | 工艺流程复杂,增加废水处理 工艺流程复杂,国内技术不成熟,缺乏政策支持 |
处理技术 | 优点 | 缺点 |
---|---|---|
固化稳定化 | 成本低,流程简单 | 对多种重金属的固化效果普适性较差,长期容易浸出,对二𫫇英没有去除效果,增大体积 |
固热处理 | 减容效果好,对多种重金属的适用性强 | 能耗高,成本高,工艺流程复杂,产生烟气和二次飞灰 |
金属热分离 | 对多种金属的分离效率均较高 | 能耗高,处理后飞灰与添加剂分离问题,产生烟气处理 |
金属化学浸出与电化学分离 | 国外技术较成熟,分离回收效率高 | 工艺流程复杂,增加废水处理 工艺流程复杂,国内技术不成熟,缺乏政策支持 |
处理技术 | 工程实验条件 | 工程实验效果 | 参考文献 |
---|---|---|---|
高温烧结 | 处理量为100t/d的回转窑,将飞灰与烧结剂按照2∶1质量比混合,窑内温度1200℃,回转窑长度为45m,混合物在45min内缓慢迁移通过回转窑,配备脱酸塔、活性炭、袋式除尘器 | 烟气中PCDD/Fs 0.019~0.025ng I-TEQ/m3,低于国际标准,烧结产物中PCDD/Fs从原始飞灰的2.593~2.704μg I-TEQ/kg,降至0.002~0.008μg I-TEQ/kg,在二次飞灰中发现14.3μg I-TEQ/kg高浓度,PCDD/Fs的破坏率较低(8.9%),烧结产物的重金属浸出浓度远低于标准限值 | [ |
高温熔融/玻璃化 | 使用柴油炉,柴油消耗量为5L/h,熔化温度为1230~1350℃、飞灰进料速率为20~25kg/h,反应时间为15~20 min,研究温度为1260℃、1320℃和1350℃ | 在1260~1350℃高温下原始飞灰与水洗飞灰的体积减量率为75%~80%,烟气中PCDD/Fs浓度约为0.053ng TEQ/m3,远低于国家标准限值,二次飞灰中的主要组分是NaCl和KCl,熔渣中重金属浸出浓度低于标准 | [ |
水泥回转窑热处理 | 飞灰经过水洗、脱氯预处理、干燥,使用气动输送机将飞灰送入窑入口的烟道气室,最大输送能力为8t/h,水泥窑为干法回转窑,配有五级旋风预热器和预分解器,熟料生产能力为2500t/d | 水泥窑热处理能够保证飞灰中二𫫇英含量显著降低,并通过指纹图谱技术揭示了水泥窑生产并未受到影响,熟料中二𫫇英含量远低于国家标准,且来源于窑内其他杂质而非飞灰二𫫇英的转移 | [ |
低温催化热解 | 低温热分解+水洗处理+蒸发结晶分盐工艺技术,每年处理飞灰量5万吨,在350~400℃绝氧的环境下进行二𫫇英解毒处理,解毒后的飞灰进行多级逆流漂洗,在MVR蒸发结晶单元将废水中的钠盐、钾盐分离 | 最高可将二𫫇英降从2500ng/kg降低至50ng/kg以下,二𫫇英降解效率大于99%,分离的钠盐、钾盐满足工业钠盐、钾盐产品标准 | [ |
固化稳定化 | 200t/d生活垃圾焚烧飞灰模袋填埋示范工程,添加螯合剂实现飞灰中重金属固化稳定,对于充灌进模袋内的飞灰增加二次螯合工艺,采用飞灰膏体制备-管道泵送-模袋充灌工艺一体化技术 | 固结后模袋体内的飞灰含水率、重金属浸出指标均满足标准要求,与常规吨袋填埋相比,飞灰模袋填埋库容率增加25%左右 | [ |
金属化学浸出与电化学分离 | 瑞士的FLUWA和FLUREC工艺,飞灰通过多级淋洗,使用酸性和中性的洗涤水进行浸出,结合电沉积回收金属 | FLUWA工艺可以提取约60%~80%的Zn、80%~95%的Cd、50%~85%的Pb和Cu,FLUREC工艺从富含重金属的滤液中回收高纯度Zn(回收率>99.995%) | [ |
处理技术 | 工程实验条件 | 工程实验效果 | 参考文献 |
---|---|---|---|
高温烧结 | 处理量为100t/d的回转窑,将飞灰与烧结剂按照2∶1质量比混合,窑内温度1200℃,回转窑长度为45m,混合物在45min内缓慢迁移通过回转窑,配备脱酸塔、活性炭、袋式除尘器 | 烟气中PCDD/Fs 0.019~0.025ng I-TEQ/m3,低于国际标准,烧结产物中PCDD/Fs从原始飞灰的2.593~2.704μg I-TEQ/kg,降至0.002~0.008μg I-TEQ/kg,在二次飞灰中发现14.3μg I-TEQ/kg高浓度,PCDD/Fs的破坏率较低(8.9%),烧结产物的重金属浸出浓度远低于标准限值 | [ |
高温熔融/玻璃化 | 使用柴油炉,柴油消耗量为5L/h,熔化温度为1230~1350℃、飞灰进料速率为20~25kg/h,反应时间为15~20 min,研究温度为1260℃、1320℃和1350℃ | 在1260~1350℃高温下原始飞灰与水洗飞灰的体积减量率为75%~80%,烟气中PCDD/Fs浓度约为0.053ng TEQ/m3,远低于国家标准限值,二次飞灰中的主要组分是NaCl和KCl,熔渣中重金属浸出浓度低于标准 | [ |
水泥回转窑热处理 | 飞灰经过水洗、脱氯预处理、干燥,使用气动输送机将飞灰送入窑入口的烟道气室,最大输送能力为8t/h,水泥窑为干法回转窑,配有五级旋风预热器和预分解器,熟料生产能力为2500t/d | 水泥窑热处理能够保证飞灰中二𫫇英含量显著降低,并通过指纹图谱技术揭示了水泥窑生产并未受到影响,熟料中二𫫇英含量远低于国家标准,且来源于窑内其他杂质而非飞灰二𫫇英的转移 | [ |
低温催化热解 | 低温热分解+水洗处理+蒸发结晶分盐工艺技术,每年处理飞灰量5万吨,在350~400℃绝氧的环境下进行二𫫇英解毒处理,解毒后的飞灰进行多级逆流漂洗,在MVR蒸发结晶单元将废水中的钠盐、钾盐分离 | 最高可将二𫫇英降从2500ng/kg降低至50ng/kg以下,二𫫇英降解效率大于99%,分离的钠盐、钾盐满足工业钠盐、钾盐产品标准 | [ |
固化稳定化 | 200t/d生活垃圾焚烧飞灰模袋填埋示范工程,添加螯合剂实现飞灰中重金属固化稳定,对于充灌进模袋内的飞灰增加二次螯合工艺,采用飞灰膏体制备-管道泵送-模袋充灌工艺一体化技术 | 固结后模袋体内的飞灰含水率、重金属浸出指标均满足标准要求,与常规吨袋填埋相比,飞灰模袋填埋库容率增加25%左右 | [ |
金属化学浸出与电化学分离 | 瑞士的FLUWA和FLUREC工艺,飞灰通过多级淋洗,使用酸性和中性的洗涤水进行浸出,结合电沉积回收金属 | FLUWA工艺可以提取约60%~80%的Zn、80%~95%的Cd、50%~85%的Pb和Cu,FLUREC工艺从富含重金属的滤液中回收高纯度Zn(回收率>99.995%) | [ |
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