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Super pure water production device and production mannered null primary pure water

机译:超纯水生产装置及生产方式为零的一次纯水

摘要

PROBLEM TO BE SOLVED: To obtain a total carbonic acid concentration measuring apparatus by which a carbonic acid concentration in pure water or ultrapure water can be detected simply and with high accuracy, by a method wherein a total carbonic acid concentration is computed on the basis of the measured value of the conductivity or the resistivity of the pure water. ;SOLUTION: A resistivity sensor 6A is installed on the entrance side of a mixed-bed ion exchange apparatus 4, and the resistivity of water flowing into the exchange apparatus 4 is measured by a resistivity meter 7A. On the other hand, a resistivity sensor 6B is installed on the exit side of the exchange apparatus 4, and the resistivity of water which flows out is measured by a resistivity meter 7B. Its measurement can be performed instantaneously. Consequently, even when a change in the resistivity is large, the measurement can be performed continuously, stably and with high accuracy. Measured values including a water passage amount by a flowmeter 8 are inputted to a computing device 9. By using a specific calculating expression, the total carbonic acid concentration of the water which flows into and total carbonic acid concentration of the water which flows out are computed. In addition, also the carbonic acid load amount of the exchange apparatus 4 and the carbonic acid load factor (the utilization factor) of an ion-exchange resin can be found. As a result, it is possible to estimate the time in which the ion-exchange resin reaches a breakthrough, i.e., the replacement time or the regeneration time of the ion-exchange apparatus 4.;COPYRIGHT: (C)1999,JPO
机译:解决的问题:获得一种总碳酸浓度测量装置,通过该装置,可以通过基于以下方法计算总碳酸浓度的方法来简单且高精度地检测纯水或超纯水中的碳酸浓度。纯水的电导率或电阻率的测量值。 ;解决方案:在混合床离子交换设备4的入口侧安装一个电阻率传感器6A,用电阻率计7A测量流入交换设备4的水的电阻率。另一方面,在交换装置4的出口侧安装有电阻率传感器6B,利用电阻率计7B来测定流出的水的电阻率。它的测量可以立即执行。因此,即使电阻率的变化大,也可以连续,稳定且高精度地进行测量。包括流量计8的水通过量的测量值被输入到计算装置9。通过使用特定的计算表达式,计算流入的水的总碳酸浓度和流出的水的总碳酸浓度。 。另外,还能够求出交换装置4的碳酸负载量和离子交换树脂的碳酸负载率(利用率)。结果,可以估计离子交换树脂达到突破的时间,即离子交换设备4的更换时间或再生时间。;版权:(C)1999,JPO

著录项

  • 公开/公告号JP3817860B2

    专利类型

  • 公开/公告日2006-09-06

    原文格式PDF

  • 申请/专利权人 栗田工業株式会社;

    申请/专利号JP19970263692

  • 发明设计人 埜村 誠;古川 征弘;

    申请日1997-09-29

  • 分类号G01N27/10;

  • 国家 JP

  • 入库时间 2022-08-21 21:50:21

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