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Development and implementation of a corrosion control algorithm based on calcium carbonate precipitation potential (CCPP) in a drinking water distribution system

机译:饮用水分配系统中基于碳酸钙沉淀电位(CCPP)的腐蚀控制算法的开发与实现

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Water corrosiveness depends mainly on the chemical factors of pH, alkalinity, Ca~(2+) concentration, dissolved oxygen, and total dissolved solids (TDS), and on the physical factors of temperature and flow velocity as well as pipe materials. The calcium carbonate precipitation potential (CCPP) control process and a simulated water distribution system (SWDS) were installed for a pilot-scale advanced water treatment process. The system was operated for 2 years. The CCPP control algorithm for anti-corrosion of a pipeline was developed and validated. The target CCPP value could be controlled by manipulating the pH and alkalinity with additions of sodium carbonate (Na_2CO_3) and carbon dioxide (CO_2) where enough calcium was present. The CCPP range of 0 ~ 4 mg L~(-1) was controlled reasonably to induce a calcium carbonate (CaCO_3) film on the surface of the pipeline, which provided the anti-corrosion effect. The proper range required of pH and alkalinity used to manipulate the range of 0 ~ 4 mg L~(-1) of CCPP was 8.0 ~ 8.3,70 ~ 100 mg L~(-1) as CaCO_3 when the Ca~(2+) concentration was in the range of 60 ~ 80 mg L~(-1) as CaCO_3, respectively, in this research. The effect of corrosion control was demonstrated by reduced iron and zinc concentrations released from the pipe material. This result might indicate the presence of the CaCO_3 film and the efficacy of its anti-corrosion effect. However, the simple proportional integral derivative (PID) controller's sensitivity seemed to be in need of further improvement.
机译:水的腐蚀性主要取决于pH,碱度,Ca〜(2+)浓度,溶解氧和总溶解固体(TDS)的化学因素,还取决于温度和流速以及管道材料的物理因素。安装了碳酸钙沉淀潜力(CCPP)控制过程和模拟水分配系统(SWDS),用于中试规模的高级水处理过程。该系统运行了2年。开发并验证了用于管道防腐的CCPP控制算法。可以通过在存在足够钙的情况下添加碳酸钠(Na_2CO_3)和二氧化碳(CO_2)来控制pH和碱度,从而控制目标CCPP值。合理控制CCPP的范围为0〜4 mg L〜(-1),使管道表面产生碳酸钙(CaCO_3)薄膜,具有防腐作用。当Ca〜(2 ++)时,用于控制CCPP的0〜4 mg L〜(-1)的pH值和碱度的合适范围为8.0〜8.3,70〜100 mg L〜(-1)作为CaCO_3。在本研究中,Ca 2 O 3的浓度分别在60〜80 mg L〜(-1)范围内。管道材料释放的铁和锌浓度降低证明了腐蚀控制的效果。该结果可能表明CaCO_3膜的存在及其抗腐蚀作用的功效。但是,简单比例积分微分(PID)控制器的灵敏度似乎需要进一步提高。

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