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首页> 外文期刊>The Korean journal of chemical engineering >Control Of Corrosive Water In Advanced Water Treatment Plant By Manipulating Calcium Carbonate Precipitation Potential
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Control Of Corrosive Water In Advanced Water Treatment Plant By Manipulating Calcium Carbonate Precipitation Potential

机译:通过控制碳酸钙的沉淀电位来控制高级水处理厂中的腐蚀性水

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摘要

The corrosion of metal pipes in water distribution networks is a complex electrochemical and physico-chemical phenomenon between a metal surface and corrosive water. The level of corrosion in water distribution systems was controlled by manipulating the calcium carbonate precipitation potential (CCPP) concentration, and the corrosive water quality was controlled in two steps within the advanced water treatment plant (AWTP) constructed at the Institute of Water Quality Research (IWQR), Busan Metropolitan City, Korea. The 1st control step was located before a coagulation process included on a rapid mixer, and the 2nd control step was located after a biological activated carbon (BAC) process. The capacity of the AWTP in IWQR was 80 m~3/day. The CCPP concentration was controlled from the calcium hardness, alkalinity, and pH by adding calcium hydroxide (Ca(OH)_2), sodium carbonate (Na_2CO_3), and carbon dioxide (CO_2) in the above two steps. A CCPP control system was installed and operated according to the developed algorithm to maintain a CCPP range of 0-4 mg/L. The CCPP range was reasonably controlled to induce the formation of a CaCO_3 film on the surface of the simulated water distribution system (SWDS). From the result of the corrosive water control, the CCPP formed greater than 0.0 mg/L. The crystalloid structure of the scale produced by CCPP control in the inner surface of pipe was zinc carbonate hydroxide hydrate (Zn_4CO_3(OH)_6·H_2O).
机译:配水管网中金属管的腐蚀是金属表面和腐蚀性水之间的复杂电化学和物理化学现象。通过控制碳酸钙沉淀电位(CCPP)的浓度来控制配水系统中的腐蚀程度,并在水质研究所(AWTP)建造的高级水处理厂(AWTP)中分两步控制腐蚀性水的质量( IWQR),韩国釜山市。第一控制步骤位于快速混合器中包括的凝结过程之前,第二控制步骤位于生物活性炭(BAC)过程之后。 IWQR中AWTP的容量为80 m〜3 / day。通过在上述两个步骤中添加氢氧化钙(Ca(OH)_2),碳酸钠(Na_2CO_3)和二氧化碳(CO_2),可以根据钙硬度,碱度和pH值控制CCPP浓度。根据开发的算法安装和操作CCPP控制系统,以保持CCPP范围为0-4 mg / L。合理控制CCPP范围,以诱导在模拟水分配系统(SWDS)的表面上形成CaCO_3膜。从控制腐蚀性水的结果来看,CCPP的含量大于0.0 mg / L。通过CCPP控制在管的内表面中产生的水垢的晶体结构是氢氧化锌氢氧化物水合物(Zn_4CO_3(OH)_6·H_2O)。

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