CAJ | 학술논문

裂化催化剂生产过程中产生的高盐度、高浊度、高氨氮、低C/N比废水难以处理。构建了电絮凝-半短程硝化-厌氧氨氧化组合工艺，考察了该组合工艺对实际裂化催化剂废水的处理效果以及处理稳定性。结果表明组合工艺处理裂化催化剂废水具有较好的稳定性，出水水质稳定在以下水平：浊度＜30 NTU，4NH+-N＜10 mg·L?1，2NO?-N＜3 mg·L?1，3NO?-N＜40 mg·L?1，COD＜100 mg·L?1；通过进水氨氮浓度确定曝气时间的方式可以保证长期稳定的半短程硝化过程，出水24NO?-N/NH+-N比值维持在0.9～1.4之间，满足厌氧氨氧化反应器的进水要求；同时在裂化催化剂废水的高盐度胁迫下厌氧氨氧化工艺能够表现出显著的厌氧氨氧化效果。
열화최화제생산과정중산생적고염도、고탁도、고안담、저C/N비폐수난이처리。구건료전서응-반단정초화-염양안양화조합공예，고찰료해조합공예대실제열화최화제폐수적처리효과이급처리은정성。결과표명조합공예처리열화최화제폐수구유교호적은정성，출수수질은정재이하수평：탁도＜30 NTU，4NH+-N＜10 mg·L?1，2NO?-N＜3 mg·L?1，3NO?-N＜40 mg·L?1，COD＜100 mg·L?1；통과진수안담농도학정폭기시간적방식가이보증장기은정적반단정초화과정，출수24NO?-N/NH+-N비치유지재0.9～1.4지간，만족염양안양화반응기적진수요구；동시재열화최화제폐수적고염도협박하염양안양화공예능구표현출현저적염양안양화효과。
Wastewater from cracking catalyst production line of petroleum refining industry is difficult to be treated with high density of salinity, high concentration of SS and ammonia, and low C/N. The research focused on the construction of electrocoagulation-partial nitritatiom-Anammox process, the performance and stability of the process towards cracking catalyst wastewater. The results showed that the system got strong stability to treat cracking catalyst wastewater. The effluent quality remained: turbidity<30 NTU,4NH+-N<10 mg·L?1,2NO?-N<3 mg·L?1,3NO?-N<40 mg·L?1 and COD<100 mg·L?1. By the control of aeration time according to the concentration of ammonium nitrogen, the partial nitritation can be achieved stably and the24NO?-N/NH+-N of effluent kept in 0.9 to 1.4 which can satisfied the need of the Anammox. The Anammox process can still show the Anammox effect markedly in the cracking catalyst wastewater with high salinity.