Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (5): 2730-2738.DOI: 10.16085/j.issn.1000-6613.2020-1178
• Biochemical and pharmaceutical engineering • Previous Articles Next Articles
LEI Xin(), YAN Rong, MU Yujie, ZHANG Yuancan, FU Zhimin()
Received:
2020-06-24
Online:
2021-05-24
Published:
2021-05-06
Contact:
FU Zhimin
通讯作者:
付志敏
作者简介:
雷欣(1995—),女,硕士研究生,研究方向为水污染控制。E-mail:基金资助:
CLC Number:
LEI Xin, YAN Rong, MU Yujie, ZHANG Yuancan, FU Zhimin. Effect of iron on nitrogen removal efficiency of anaerobic ammonium oxidation bacteria[J]. Chemical Industry and Engineering Progress, 2021, 40(5): 2730-2738.
雷欣, 闫荣, 慕玉洁, 章院灿, 付志敏. 铁元素对厌氧氨氧化菌脱氮效能的影响[J]. 化工进展, 2021, 40(5): 2730-2738.
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金属 | 污泥种类 | 反应器装置 | 时长 | 污泥浓度 | 氮去除情况 | 浓度 | 参考文献 |
---|---|---|---|---|---|---|---|
nZVI | 混合活性污泥 | 序批式反应器 | 310d | 氨氮和亚硝酸盐的去除率在日常测量中增加了58% | 0.04~5000μg·L-1 | [ | |
厌氧活性污泥 | 升流式好氧 污泥床 | 150d | (2000±20)mgMLSS·L-1 | 平均NH | 5.26g·L-1 | [ | |
厌氧活性污泥 | 升流式好氧 污泥床 | 150d | (2000±20)mgMLSS·L-1 | 平均NH | 5.26g·L-1 | [ | |
Anammox污泥 | 升流式厌氧 污泥床 | 130d | 12.0gVSS·L-1 | 氮去除效率(NRE)保持在85%以上 | 1.0~200mg·L-1 | [ | |
Fe(Ⅱ) | 500mL硝化污泥和100mL Anammox污泥 | 生物滤池 | 179d | 最高总氮去除率0.58kg·m-3·d-1 | 1~5mg·L-1 | [ | |
Anammox污泥 | 500mL血清瓶 | 71个周期 /10h | 10g Anammox湿污泥 | 最高脱氨效能0.65kg·m-3·d-1 | 5mg·L-1 | [ | |
Anammox种子污泥 | 上流固定床塔式 反应器 | 144d | 3.683gVSS·L-1 | 总氮去除率8.198~9.135kg·m-3·d-1 | 0.09~0.12mmol·L-1 | [ | |
以竹炭为载体的 Anammox颗粒污泥 | 100mL上流式 反应器 | 205d | 容积总氮去除负荷2.53kg·m-3·d-1 | 0.075mmol·L-1 | [ | ||
厌氧活性污泥 | 上流柱式 反应器 | 75d | 2.54gMLSS·L-1 | 最高氮去除负荷1400gN·m-3·d-1 | 0.09mmol·L-1 | [ | |
厌氧活性污泥 | 厌氧序批式 反应器 | 210d | 平均NH | 0.085mmol·L-1 | [ | ||
Anammox | 序批式生物膜 反应器 | 216d | 氮去除率95%,氮去除率提高15%(0.04mmol·L-1) | 0.08mmol·L-1 | [ | ||
Fe0+ Fe2+ | Anammox污泥 | 升流式厌氧 污泥床 | 60d | 3.15gMLSS·L-1 | 氮去除率最大值达到88.43%,总氮去除率最大值达到80.77% | [ | |
Fe(Ⅱ) Fe(Ⅲ) | 脱氮污泥 | 序批式反应器 | 60d | 4.13gTSS·L-1 | 最高平均脱氮率250mgN·L-1·d-1 | Fe(Ⅱ)<1.3mg·L-1 Fe(Ⅲ)<0.4mg·L-1 | [ |
Fe(Ⅲ) | Anammox污泥 | 500mL血清瓶 | 71个周期 /10h | 10g Anammox湿污泥 | 最高脱氮效能0.51kg·m-3·d-1 | 5mg·L-1 | [ |
活性污泥 | 序批式反应器 | 2个月 | 总氮去除负荷0.95kg·m-3·d-1 | 6mg·L-1 | [ | ||
颗粒污泥 | 升流式厌氧 污泥床 | 97d | 11.1gSS·L-1;8.2gVSS·L-1 | 氮去除率73.6%±12.8%;最高氮去除负荷(2.6±0.9)kgN·m-3·d-1 | 3.68mg·L-1 | [ |
金属 | 污泥种类 | 反应器装置 | 时长 | 污泥浓度 | 氮去除情况 | 浓度 | 参考文献 |
---|---|---|---|---|---|---|---|
nZVI | 混合活性污泥 | 序批式反应器 | 310d | 氨氮和亚硝酸盐的去除率在日常测量中增加了58% | 0.04~5000μg·L-1 | [ | |
厌氧活性污泥 | 升流式好氧 污泥床 | 150d | (2000±20)mgMLSS·L-1 | 平均NH | 5.26g·L-1 | [ | |
厌氧活性污泥 | 升流式好氧 污泥床 | 150d | (2000±20)mgMLSS·L-1 | 平均NH | 5.26g·L-1 | [ | |
Anammox污泥 | 升流式厌氧 污泥床 | 130d | 12.0gVSS·L-1 | 氮去除效率(NRE)保持在85%以上 | 1.0~200mg·L-1 | [ | |
Fe(Ⅱ) | 500mL硝化污泥和100mL Anammox污泥 | 生物滤池 | 179d | 最高总氮去除率0.58kg·m-3·d-1 | 1~5mg·L-1 | [ | |
Anammox污泥 | 500mL血清瓶 | 71个周期 /10h | 10g Anammox湿污泥 | 最高脱氨效能0.65kg·m-3·d-1 | 5mg·L-1 | [ | |
Anammox种子污泥 | 上流固定床塔式 反应器 | 144d | 3.683gVSS·L-1 | 总氮去除率8.198~9.135kg·m-3·d-1 | 0.09~0.12mmol·L-1 | [ | |
以竹炭为载体的 Anammox颗粒污泥 | 100mL上流式 反应器 | 205d | 容积总氮去除负荷2.53kg·m-3·d-1 | 0.075mmol·L-1 | [ | ||
厌氧活性污泥 | 上流柱式 反应器 | 75d | 2.54gMLSS·L-1 | 最高氮去除负荷1400gN·m-3·d-1 | 0.09mmol·L-1 | [ | |
厌氧活性污泥 | 厌氧序批式 反应器 | 210d | 平均NH | 0.085mmol·L-1 | [ | ||
Anammox | 序批式生物膜 反应器 | 216d | 氮去除率95%,氮去除率提高15%(0.04mmol·L-1) | 0.08mmol·L-1 | [ | ||
Fe0+ Fe2+ | Anammox污泥 | 升流式厌氧 污泥床 | 60d | 3.15gMLSS·L-1 | 氮去除率最大值达到88.43%,总氮去除率最大值达到80.77% | [ | |
Fe(Ⅱ) Fe(Ⅲ) | 脱氮污泥 | 序批式反应器 | 60d | 4.13gTSS·L-1 | 最高平均脱氮率250mgN·L-1·d-1 | Fe(Ⅱ)<1.3mg·L-1 Fe(Ⅲ)<0.4mg·L-1 | [ |
Fe(Ⅲ) | Anammox污泥 | 500mL血清瓶 | 71个周期 /10h | 10g Anammox湿污泥 | 最高脱氮效能0.51kg·m-3·d-1 | 5mg·L-1 | [ |
活性污泥 | 序批式反应器 | 2个月 | 总氮去除负荷0.95kg·m-3·d-1 | 6mg·L-1 | [ | ||
颗粒污泥 | 升流式厌氧 污泥床 | 97d | 11.1gSS·L-1;8.2gVSS·L-1 | 氮去除率73.6%±12.8%;最高氮去除负荷(2.6±0.9)kgN·m-3·d-1 | 3.68mg·L-1 | [ |
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