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    • 1. 发明授权
    • 하·폐수 고도처리방법
    • 하폐폐수고도처리방법
    • KR100411413B1
    • 2003-12-18
    • KR1020010060972
    • 2001-09-29
    • 주식회사 한화건설
    • 정태천한승호허형우박승국조용주최진호최은주박종부김윤석이평호유재홍박상헌이상일
    • C02F3/30
    • PURPOSE: An advanced sewage/wastewater treatment process is provided, which is characterized in that sewage is travelled to non aeration tank via aeration tank to reduce dissolved oxygen by endogenous respiration when recycled to anoxic tank, thus predenitrification on influent organic is optimized. CONSTITUTION: In an advanced treatment process including an anoxic tank(1), an aeration tank(2), a reaeration tank(4), and settling tank(5) set in series to remove nutrients, the advanced treatment method is characterized in that sewage is travelled to non aeration tank via aeration tank to reduce dissolved oxygen by endogenous respiration when recycled to anoxic tank, thus predenitrification on influent organic is optimized, wherein an anaeration tank is optionally installed in front of the anoxic tank to remove phosphorus.
    • 目的:提供一种先进的污水/废水处理工艺,其特征在于通过曝气池将污水运送到非曝气池,以在回收到缺氧池时通过内源呼吸来减少溶解氧,从而优化了对进水有机物的预反硝化。 组成:在包括缺氧罐(1),曝气罐(2),再生罐(4)和沉淀罐(5)的先​​进处理工艺中,串联设置以除去营养物,所述先进处理方法的特征在于 污水通过曝气池进入非曝气池,当再循环至缺氧池时通过内源呼吸减少溶解氧,从而优化对进水有机物的预反硝化作用,其中在缺氧池前方可选地安装脱气池以去除磷。
    • 2. 发明公开
    • 하·폐수 고도처리방법
    • 先进的水处理/废水处理工艺
    • KR1020030027608A
    • 2003-04-07
    • KR1020010060972
    • 2001-09-29
    • 주식회사 한화건설
    • 정태천한승호허형우박승국조용주최진호최은주박종부김윤석이평호유재홍박상헌이상일
    • C02F3/30
    • PURPOSE: An advanced sewage/wastewater treatment process is provided, which is characterized in that sewage is travelled to non aeration tank via aeration tank to reduce dissolved oxygen by endogenous respiration when recycled to anoxic tank, thus predenitrification on influent organic is optimized. CONSTITUTION: In an advanced treatment process including an anoxic tank(1), an aeration tank(2), a reaeration tank(4), and settling tank(5) set in series to remove nutrients, the advanced treatment method is characterized in that sewage is travelled to non aeration tank via aeration tank to reduce dissolved oxygen by endogenous respiration when recycled to anoxic tank, thus predenitrification on influent organic is optimized, wherein an anaeration tank is optionally installed in front of the anoxic tank to remove phosphorus.
    • 目的:提供先进的污水/污水处理工艺,其特点是通过曝气池将污水运送到非曝气池,再循环到缺水罐中,通过内生呼吸减少溶解氧,从而优化流入有机物的预硝化。 构成:先进的处理方法包括缺氧罐(1),曝气池(2),再循环罐(4)和沉淀池(5),以排除营养物质,先进的处理方法的特点是 通过曝气池将污水运送到非曝气池,再循环到缺氧罐中,通过内源性呼吸减少溶解氧,从而优化进水有机物的预硝化,其中可选地,在厌氧罐前面安装一个排气池以除磷。
    • 3. 发明授权
    • 하·폐수의 영양염류 제거방법
    • 하폐폐수의영양염류제거방법
    • KR100448305B1
    • 2004-09-10
    • KR1020010029803
    • 2001-05-29
    • 주식회사 한화건설
    • 정태천한승호허형우박승국최은주조용주최진호이경성
    • C02F3/30
    • PURPOSE: A system for removing nutrients of sewage/wastewater is provided, which is characterized in that a timer and an air supplier are installed at the sewage/wastewater treatment plant. Wastewater flow and aeration/non-aeration time are controlled respectively by the timer and the air supplier. So discharge of nutrient of treated water is stable. CONSTITUTION: The system comprises a pair of primary intermittent aeration tanks(4a,4b); a pair of secondary intermittent aeration tanks(5a,5b); a pair of reaeration tanks for gas stripping; a final settling tank; a flow switch(3); and optional anaerobic tanks(7a,7b) for phosphorus release.
    • 目的:提供一种用于去除污水/废水营养物的系统,其特征在于在污水/污水处理厂中安装定时器和空气供应器。 计时器和空气供应商分别控制废水流量和曝气/非曝气时间。 所以处理后水的养分排放稳定。 组成:该系统包括一对初级间歇曝气池(4a,4b); 一对二次间歇曝气池(5a,5b); 一对用于气体剥离的再生槽; 最终沉淀池; 流量开关(3); 和用于磷释放的可选厌氧池(7a,7b)。
    • 4. 发明公开
    • 하·폐수의 영양염류 제거방법
    • 排除污水/废水营养的系统
    • KR1020020090786A
    • 2002-12-05
    • KR1020010029803
    • 2001-05-29
    • 주식회사 한화건설
    • 정태천한승호허형우박승국최은주조용주최진호이경성
    • C02F3/30
    • PURPOSE: A system for removing nutrients of sewage/wastewater is provided, which is characterized in that a timer and an air supplier are installed at the sewage/wastewater treatment plant. Wastewater flow and aeration/non-aeration time are controlled respectively by the timer and the air supplier. So discharge of nutrient of treated water is stable. CONSTITUTION: The system comprises a pair of primary intermittent aeration tanks(4a,4b); a pair of secondary intermittent aeration tanks(5a,5b); a pair of reaeration tanks for gas stripping; a final settling tank; a flow switch(3); and optional anaerobic tanks(7a,7b) for phosphorus release.
    • 目的:提供一种消除污水/废水营养的系统,其特征在于在污水/污水处理厂安装定时器和空气供应商。 污水流量和曝气/非曝气时间分别由定时器和空气供应商控制。 所以处理水的营养物质的排放是稳定的。 构成:系统包括一对初级间歇曝气池(4a,4b); 一对二次间歇曝气池(5a,5b); 一个用于气体剥离的补充池; 最后的沉淀池 流量开关(3); 和用于磷释放的任选的厌氧罐(7a,7b)。