COMPARATIVE PILOT TEST OF CATALYTIC OZONE OXIDATION AND NaClO IN TREATING TITANIUM DIOXIDE WASTEWATER
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摘要: 以山东某钛白粉厂二级压滤出水为研究对象,通过自主设计的中试设备考察了催化臭氧氧化工艺与NaClO工艺对钛白粉废水处理情况,确定催化臭氧氧化的最佳工艺实验条件为:在室温条件下,催化臭氧氧化反应时间为60 min,臭氧投加浓度为125 mg/L。对原有NaClO工艺进行优化,优化后的最佳工艺为:NaClO投加量为1.2%,反应时间为30 min。当平均进水ρ(COD)与ρ(NH3-N)分别为109.7,12.8 mg/L,则催化臭氧工艺平均出水ρ(COD)与ρ(NH3-N)分别为43.5,3.8 mg/L,平均去除率分别为60%和70.4%,NaClO工艺平均出水ρ(COD)与ρ(NH3-N)分别为49.8,4.7 mg/L,平均去除率分别为54.5%和63.1%。在30 d内,催化臭氧氧化出水达标率为100%,NaClO出水达标率为26.7%,催化臭氧氧化处理费用为1.12元/t,NaClO处理费用为12元/t,催化臭氧氧化工艺相较于NaClO氧化工艺更适用于处理钛白粉废水。Abstract: Taking the secondary pressure filtration water from a titanium dioxide plant in Shandong as the research object, the catalytic ozonation process and the treatment of titanium dioxide wastewater were investigated through a self-designed pilot plant, and the best experimental conditions for catalytic ozonation process were determined as follows:at room temperature, the catalytic ozone oxidation reaction time was 60 min, and the ozone concentration was 125 mg/L. The original NaClO process was also optimized, and the best process after optimization was as follows:NaClO dosage was 1.2%, and the reaction time was 30 minutes. When the average influent COD and ammonia nitrogen were 109.7 mg/L and 12.8 mg/L, the average effluent COD and ammonia nitrogen of the catalytic ozone process were 43.5 mg/L and 3.8 mg/L, respectively, and the average removal rates were 60% and 70.4%, respectively; and the average effluent COD and ammonia nitrogen in the NaClO process were 49.8 mg/L and 4.7 mg/L, respectively, and the average removal rates were 54.5% and 63.1%, respectively. Within 30 days, the standard-meeting rate of the catalytic ozonation process effluent was 100%, and that of the NaClO process effluent was 26.7%; the running cost of catalytic ozonation ton water treatment was RMB 1.12/t, and that of the NaClO treatment was RMB 12/t. The catalytic ozonation process was more suitable for treating titanium dioxide wastewater, compared with The NaClO oxidation process.
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Key words:
- catalytic ozone oxidation /
- NaClO /
- ammonia nitrogen /
- pilot test
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[1] 陈海平,胡越,桂晨冉,等.硫酸法钛白粉生产过程中废酸和废水的治理[J].当代化工研究,2021(11):1-3. [2] 甘永乐,黄原玲,吴小芳,等.降低硫酸法钛白粉生产工艺中废酸和废水处理成本的研究[J].轻工科技,2019,35(6):23-24. [3] 徐竟成,郭浩博,杨斯棋,等.微滤再生处理钛白粉生产三洗废水工艺研究[J].工业水处理,2015,35(11):18-22. [4] 施中华,彭新华.硫酸法生产钛白粉的废水治理措施研究[J].科技资讯,2015,13(14):105. [5] 杨瑞雪. 攀钢钛白粉厂含铬含砷废水处理工程研究[D].昆明:昆明理工大学,2012:11-15. [6] 张杰. 钛白粉废水处理新工艺的研究[D].湘潭:湘潭大学,2009:11-15. [7] 李皓. 经中和除渣处理后的钛白粉废水回用技术研究[D].湘潭:湘潭大学,2012:11-15. [8] 李晓,刘碧武,郭军.折点加氯法去除生活污水氨氮的试验研究[J].能源环境保护,2019,33(5):32-35. [9] 李婵君,贺剑明.折点加氯法处理深度处理低氨氮废水[J].广东化工,2013,40(20):43-44. [10] 杨洪新,胡金玲,姜雪松,等.折点加氯技术处理农药废水中氨氮的研究[J].现代农药,2018,17(5):19-21. [11] 费明明,沈亮,陆丹红,等.折点加氯对微污染原水中氨氮去除效果的研究[J].给水排水,2016,52(9):13-17. [12] 李敏,付丽亚,谭煜,等.Mn-Ce/γ-Al2O3催化臭氧氧化深度处理石化废水中试研究[J/OL].环境科学研究:1-12[2021-05-20].https://doi.org/10.13198/j.issn.1001-6929.2021.05.10. [13] 孙岳新,王栋栋,俞强.高级氧化集成技术深度处理造纸废水工艺研究[J].中国造纸,2021,40(4):111-115. [14] 杜虎,韦叶.FeOOH催化H2O2/O3氧化处理化工废水生化尾水的研究[J].浙江化工,2021,52(3):45-47. [15] 刘海兵,吴叶,邹小洪,等.金属氧化物催化剂催化臭氧氧化氨氮性能研究[J].江西理工大学学报,2017,38(5):57-62. [16] 黄小琴,汪晓军,王蓓蓓,等.垃圾渗滤液深度处理中试研究[J].水处理技术,2017,43(7):94-97,102. [17] 巫先坤,陈洋,赵选英, 等.催化臭氧氧化水中氨氮的研究[J].广东化工,2020,47(18):131-132,100. [18] TAGUCHI J, OKUHARA T. Selective oxidative decomposition of ammonia in neutral water to nitrogen over titania-supported platinum or palladium catalyst[J]. Applied Catalysis A:General, 2000, 194:89-97. [19] TAGUCHI J, YOSHINAGA Y, OKUHARA T. Purification of ammonia-containing water by catalytic selective decomposition with novel Pd-supported zirconia[J]. Chemistry letters, 2001, 30(2):112-113. [20] 吴宗蔚. 铝基催化剂制备、臭氧氧化有机物和氨氮性能与应用研究[D].大连:大连理工大学,2018. [21] 郭琳,刘晨,吴叶,等.MgO催化臭氧氧化水中氨氮的研究[J].工业水处理,2017,37(6):48-51. [22] 凌威,王晶日,于洪淼,等.催化臭氧氧化去除模拟海产养殖废水中氟苯尼考[J].环境工程,2019,37(10):139-144,82. [23] 张睿,徐世凯,郭风,等.折点氯化法处理鸟粪石生产废水氨氮的试验研究[J].工业用水与废水,2021,52(2):30-33. [24] 许高平,冯在玉,任婉璐,等.折点加氯去除氨氮特性[J].净水技术,2020,39(11):106-109.
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