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JP5650151B2 - Method for measuring dissolved ozone concentration in ozone water - Google Patents
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JP5650151B2 - Method for measuring dissolved ozone concentration in ozone water - Google Patents

Method for measuring dissolved ozone concentration in ozone water Download PDF

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JP5650151B2
JP5650151B2 JP2012070042A JP2012070042A JP5650151B2 JP 5650151 B2 JP5650151 B2 JP 5650151B2 JP 2012070042 A JP2012070042 A JP 2012070042A JP 2012070042 A JP2012070042 A JP 2012070042A JP 5650151 B2 JP5650151 B2 JP 5650151B2
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崇 浦野
崇 浦野
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IHI Shibaura Machinery Corp
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Description

本発明は、オゾン水の溶存オゾン濃度測定方法に関する。   The present invention relates to a method for measuring the dissolved ozone concentration of ozone water.

従来から、特許文献1に開示されるように、オゾン水を用いて種々の殺菌対象物を殺菌する殺菌洗浄装置に関する技術は公知である。このようなオゾン水を用いた殺菌洗浄装置では、原料水(以下、原水という)にオゾンガスを注入することで、オゾン水が生成される。   Conventionally, as disclosed in Patent Document 1, a technique related to a sterilization cleaning apparatus that sterilizes various sterilization objects using ozone water is known. In such a sterilizing and cleaning apparatus using ozone water, ozone water is generated by injecting ozone gas into raw material water (hereinafter referred to as raw water).

また、このようなオゾン水を用いた殺菌洗浄装置では、オゾン水の溶存オゾン濃度を測定するために紫外線吸光法による溶存オゾン濃度計(特許文献1においては、オゾン水モニタ)が設けられている。当該溶存オゾン濃度計は、オゾンが紫外線を吸光する性質を利用して、オゾン水を透過する紫外線の光量の減少比率によりオゾン水の溶存オゾン濃度を測定するものである。すなわち、オゾン水を用いた殺菌洗浄装置等で用いられている従来の溶存オゾン濃度測定方法では、図11に示すように、オゾンが存在しない原水通水時の紫外線透過量とオゾンガス注入開始後のオゾン水の紫外線透過量のそれぞれを測定し、その比を求めて、溶存オゾン濃度を算出する。具体的には、先ず、オゾンガスが注入される前の原水の紫外線透過量を測定することで、溶存オゾン濃度を算出する際の基準となる溶存オゾン濃度の原点(溶存オゾン濃度が0mg/Lとなる点)を決定する。すなわち、オゾンが存在しない原水通水時の紫外線透過量をオゾン水の溶存オゾン濃度が0mg/L(原点)となる原点光量として決定する。続いて、原点光量決定後、原水にオゾンガスを注入してオゾン水を生成する際に、決定された原点光量を基準としてオゾン水による紫外線透過量の減少比率を測定し、当該減少比率によりオゾン水の溶存オゾン濃度が算出される。   Further, in such a sterilizing and cleaning apparatus using ozone water, a dissolved ozone concentration meter (in the patent document 1, an ozone water monitor) is provided by an ultraviolet absorption method in order to measure the dissolved ozone concentration of ozone water. . The dissolved ozone concentration meter measures the dissolved ozone concentration of ozone water based on the reduction ratio of the amount of ultraviolet light that passes through ozone water, utilizing the property that ozone absorbs ultraviolet light. That is, in the conventional method for measuring dissolved ozone concentration used in a sterilizing and cleaning apparatus using ozone water, as shown in FIG. 11, the amount of transmitted UV light and the amount of ozone after starting ozone gas injection when ozone is not present. Each of the amounts of ultraviolet water transmitted through ozone water is measured, the ratio is obtained, and the dissolved ozone concentration is calculated. Specifically, first, by measuring the amount of ultraviolet light transmitted through the raw water before the ozone gas is injected, the origin of the dissolved ozone concentration (the dissolved ozone concentration is 0 mg / L as a reference when calculating the dissolved ozone concentration). To be determined). That is, the amount of transmitted ultraviolet light during the passage of raw water without ozone is determined as the origin light amount at which the dissolved ozone concentration of ozone water is 0 mg / L (origin). Subsequently, after the origin light quantity is determined, when ozone gas is generated by injecting ozone gas into the raw water, the reduction rate of the amount of ultraviolet light transmitted by the ozone water is measured with reference to the determined origin light quantity, and the ozone water is determined based on the reduction ratio. The dissolved ozone concentration of is calculated.

特開2006−068095号公報JP 2006-068095 A

しかしながら、原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合、上記原点光量決定後に、オゾン水を生成するために原水にオゾンガスを注入すると、当該物質の影響で紫外線透過量が一時的に増加する方向に変動してしまい、正確な溶存オゾン濃度測定ができない。具体的には、通常、水に対するオゾン処理では、水の汚れの原因となる不純物質がオゾンにより脱色され、水の透明度が上がり紫外線透過量が増加する方向に変動する(図12(a)の矢印Aで示す部分)。この紫外線透過量の変動を、図12(b)に示すように、溶存オゾン濃度に換算した結果、紫外線透過量が変動する場合とは逆に溶存オゾン濃度が減少する方向に振れていくことになる(図12(b)の矢印Bで示す部分)。そして、さらに、オゾンガスを注入すると、当該物質との反応が終了した時点から、溶存オゾン濃度が上昇(紫外線透過量の場合は低下)してくることになる(図12(b)の矢印Cで示す部分)。当該物質による影響を考慮せずにオゾンガス注入前の原水の紫外線透過量を原点光量として決定し、オゾンガス注入後のオゾン水の溶存オゾン濃度を測定すると、本来の溶存溶存オゾン濃度よりも低い値として測定されてしまい、正確にオゾン水の溶存オゾン濃度を測定することができない。   However, if the raw water contains a substance that changes the amount of UV transmission due to the reaction with ozone, if ozone gas is injected into the raw water to generate ozone water after determining the origin light intensity, the UV light is transmitted under the influence of the substance. The amount fluctuates in the direction of increasing temporarily, and accurate dissolved ozone concentration measurement cannot be performed. Specifically, normally, in ozone treatment for water, impurities that cause water stains are decolorized by ozone, and the transparency of water increases and the amount of ultraviolet light transmitted increases (see FIG. 12A). Part indicated by arrow A). As shown in FIG. 12 (b), the fluctuation in the amount of transmitted ultraviolet light is converted into a dissolved ozone concentration. As a result, the amount of dissolved ozone is swung in the opposite direction to the case where the amount of transmitted ultraviolet light varies. (Part indicated by arrow B in FIG. 12B). Further, when ozone gas is injected, the concentration of dissolved ozone increases (decreases in the case of the amount of transmitted ultraviolet light) from the point of time when the reaction with the substance ends (as indicated by arrow C in FIG. 12B). Part shown). Without considering the influence of the substance, the amount of UV transmission of raw water before ozone gas injection was determined as the origin light amount, and when the dissolved ozone concentration of ozone water after ozone gas injection was measured, the value was lower than the original dissolved ozone concentration. Therefore, the dissolved ozone concentration of ozone water cannot be measured accurately.

そこで、本発明は、原水にオゾンとの反応により紫外線透過量が変化する物質が含まれる場合でも、紫外線透過量によりオゾン水の溶存オゾン濃度を正確に測定することができるオゾン水の溶存オゾン濃度測定方法を提供することを目的とする。   Therefore, the present invention is able to accurately measure the dissolved ozone concentration of ozone water based on the amount of transmitted ultraviolet light even when the raw water contains a substance whose amount of transmitted ultraviolet light changes due to reaction with ozone. An object is to provide a measurement method.

本発明の解決しようとする課題は以上の如くであり、次にこの課題を解決するための手段を説明する。   The problem to be solved by the present invention is as described above. Next, means for solving the problem will be described.

即ち、請求項1においては、
原水にオゾンガスを注入してオゾン水を生成する際に、当該オゾン水の紫外線透過量の変化に基づいてオゾン水の溶存オゾン濃度を測定する方法であって、
前記原水に対して前記オゾンガスを注入する前に前記原水の紫外線透過量を所定時間毎に取得する注入前透過量取得工程と、
前記注入前透過量取得工程にて取得された前記原水の紫外線透過量を原点光量として設定する原点設定工程と、
前記原水に前記オゾンガスを注入する注入工程と、
前記オゾンガス注入開始後に前記オゾン水の紫外線透過量を所定時間毎に取得する注入開始後透過量取得工程と、
前記注入開始後透過量取得工程にて取得された前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さいかどうかを判定する判定工程と、
前記判定工程にて前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さくないと判定された場合に、当該オゾン水の紫外線透過量を原点光量として再設定する原点再設定工程と、を有するものである。
That is, in claim 1,
When ozone gas is injected into raw water to generate ozone water, a method of measuring the dissolved ozone concentration of ozone water based on the change in the amount of ultraviolet light transmitted through the ozone water,
A pre-injection permeation amount acquisition step of acquiring the ultraviolet light permeation amount of the raw water every predetermined time before injecting the ozone gas into the raw water;
An origin setting step for setting the ultraviolet light transmission amount of the raw water acquired in the transmission amount acquisition step before injection as an origin light amount,
An injection step of injecting the ozone gas into the raw water;
A post-injection transmission amount acquisition step of acquiring the ultraviolet transmission amount of the ozone water every predetermined time after the ozone gas injection start;
A determination step of determining whether or not the amount of ultraviolet light transmitted through the ozone water acquired in the transmission amount acquisition step after the start of injection is smaller than the origin light amount set in the origin setting step;
The origin for resetting the ultraviolet light transmission amount of the ozone water as the origin light amount when it is determined in the determination step that the ultraviolet light transmission amount of the ozone water is not smaller than the origin light amount set in the origin setting step. A resetting step.

請求項2においては、
前記注入開始後透過量取得工程では、前記オゾンガス注入開始後に前記オゾン水の紫外線透過量を所定時間毎に検出するとともに、過去所定時間に検出された前記オゾン水の紫外線透過量の平均値を取得するものである。
In claim 2,
In the permeation amount acquisition process after the start of injection, the UV light transmission amount of the ozone water is detected every predetermined time after the ozone gas injection is started, and the average value of the UV light transmission amount detected in the past predetermined time is acquired. To do.

請求項3においては、
前記注入前透過量取得工程では、前記原水に対して前記オゾンガスを注入する前に前記原水の紫外線透過量を所定時間毎に検出するとともに、過去所定時間に検出された前記原水の紫外線透過量の平均値を取得し、当該原水の紫外線透過量の平均値と、当該原水の紫外線透過量の平均値と同様にして取得される前記過去所定時間の直前に取得した前記原水の紫外線透過量の平均値とを比較し、その差が規定値内の場合に、当該原水の紫外線透過量の平均値を前記オゾンガスを注入する前の前記原水の紫外線透過量とするものである。
In claim 3,
In the pre-injection transmission amount acquisition step, the ultraviolet transmission amount of the raw water is detected every predetermined time before the ozone gas is injected into the raw water, and the ultraviolet transmission amount of the raw water detected in the past predetermined time is detected. An average value is obtained, and an average value of the ultraviolet transmission amount of the raw water and an average value of the ultraviolet transmission amount of the raw water obtained immediately before the past predetermined time obtained in the same manner as the average value of the ultraviolet transmission amount of the raw water. When the difference is within a specified value, the average value of the amount of ultraviolet light transmitted through the raw water is set as the amount of ultraviolet light transmitted through the raw water before the ozone gas is injected.

請求項4においては、
前記判定工程にて前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さいと判定された場合に、前記オゾン水の溶存オゾン濃度が所定の目標濃度に達したかどうかを判定する目標濃度判定工程を、さらに有するものである。
In claim 4,
Whether the dissolved ozone concentration of the ozone water has reached a predetermined target concentration when it is determined in the determination step that the ultraviolet light transmission amount of the ozone water is smaller than the light amount of origin set in the origin setting step It further has a target density determination step for determining whether or not.

本発明によれば、原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合でも、オゾン水の溶存オゾン濃度を正確に測定することができる。   ADVANTAGE OF THE INVENTION According to this invention, even when the raw | natural water contains the substance from which ultraviolet-ray transmission amount changes by reaction with ozone, the dissolved ozone concentration of ozone water can be measured correctly.

オゾン水濃度計を備えたオゾン水による内視鏡殺菌装置の前面図。The front view of the endoscope sterilizer by ozone water provided with the ozone water concentration meter. 同じくオゾン水による内視鏡殺菌装置の平面図。The top view of the endoscope sterilizer by ozone water similarly. 同じくオゾン水による内視鏡殺菌装置の右側面図。The right view of the endoscope sterilizer by ozone water similarly. 同じくオゾン水による内視鏡殺菌装置の背面図。The rear view of the endoscope sterilizer by ozone water similarly. オゾン水濃度計を備えたオゾン水による内視鏡殺菌装置の内部の構成を示す前面図。The front view which shows the structure inside the endoscope sterilizer by ozone water provided with the ozone water concentration meter. 同じくオゾン水による内視鏡殺菌装置の内部の構成を示す右側面図。The right view which similarly shows the internal structure of the endoscope sterilizer by ozone water. オゾン水による内視鏡殺菌装置内に配置したオゾン水濃度計の側面図。The side view of the ozone water concentration meter arrange | positioned in the endoscope sterilizer by ozone water. 本発明の一実施形態に係るオゾン水の溶存オゾン濃度測定方法のフローを示す図。The figure which shows the flow of the dissolved ozone concentration measuring method which concerns on one Embodiment of this invention. 同じくオゾン水の溶存オゾン濃度測定方法を説明するための説明図であり、(a)は紫外線透過量の経時変化を示す図、(b)は溶存オゾン濃度の経時変化を示す図。Similarly, it is explanatory drawing for demonstrating the dissolved ozone concentration measuring method of ozone water, (a) is a figure which shows a time-dependent change of ultraviolet-ray transmission amount, (b) is a figure which shows a time-dependent change of dissolved ozone concentration. オゾン水の溶存オゾン濃度測定方法を実施するための装置の別の例であるオゾン殺菌装置の構成を示す模式図。The schematic diagram which shows the structure of the ozone sterilizer which is another example of the apparatus for implementing the dissolved ozone concentration measuring method of ozone water. 従来の溶存オゾン濃度測定方法を説明するための説明図であり、(a)は紫外線透過量の経時変化を示す図、(b)は溶存オゾン濃度の経時変化を示す図。It is explanatory drawing for demonstrating the conventional dissolved ozone concentration measuring method, (a) is a figure which shows a time-dependent change of ultraviolet-ray transmission amount, (b) is a figure which shows a time-dependent change of dissolved ozone concentration. 従来の溶存オゾン濃度測定方法の問題点を説明するための説明図であり、(a)は紫外線透過量の経時変化を示す図、(b)は溶存オゾン濃度の経時変化を示す図。It is explanatory drawing for demonstrating the problem of the conventional dissolved ozone concentration measuring method, (a) is a figure which shows a time-dependent change of ultraviolet-ray transmission amount, (b) is a figure which shows a time-dependent change of dissolved ozone concentration.

次に、発明の実施の形態を説明する。
先ず、本発明の実施形態に係るオゾン水の溶存オゾン濃度測定方法を実施するための装置の一例としてオゾン水による内視鏡殺菌装置の構成を図1から図5を用いて説明する。
Next, embodiments of the invention will be described.
First, the configuration of an endoscope sterilizer using ozone water will be described with reference to FIGS. 1 to 5 as an example of an apparatus for carrying out the dissolved ozone concentration measuring method according to the embodiment of the present invention.

オゾン水による内視鏡殺菌装置は、オゾン水を満たした殺菌槽(2)の内部に、消毒対象物品である内視鏡(10)を浸漬して、オゾン水により内視鏡(10)の内部に至るまで、殺菌消毒するものである。本体は、外装(1)を有しており、該外装(1)は、前板(1a)と側板(1b・1b)と背板(1c)と蓋体(3)等により構成されている。蓋体(3)は、内視鏡(10)を支持した状態のトレーを出し入れする際に開閉する部分であり、殺菌処理中は、該蓋体(3)が開くことのないように、蓋ロック機構によりロックしている。該外装(1)の内側に殺菌槽(2)が構成されており、トレーに設置された状態の内視鏡(10)を、殺菌槽(2)内に浸漬して、殺菌処理を行う。   The endoscope sterilization apparatus using ozone water immerses the endoscope (10), which is an article to be sterilized, inside the sterilization tank (2) filled with ozone water, and the endoscope (10) The inside is sterilized and disinfected. The main body has an exterior (1), and the exterior (1) is composed of a front plate (1a), side plates (1b and 1b), a back plate (1c), a lid (3), and the like. . The lid (3) is a part that opens and closes when the tray with the endoscope (10) supported is taken in and out, and the lid (3) is not opened during the sterilization process. Locked by the lock mechanism. The sterilization tank (2) is configured inside the exterior (1), and the endoscope (10) installed on the tray is immersed in the sterilization tank (2) to perform sterilization treatment.

オゾン水による内視鏡殺菌装置の上面には、蓋体(3)の他に、開閉不可能な部分に、タッチパネル(4)と水流確認窓(5)が設けられている。該タッチパネル(4)は、タッチパネル操作盤と状態表示用の液晶表示盤を兼用しており、該タッチパネル(4)に表示された操作内容を、タッチすることにより、殺菌消毒の操作が実行され、また現在の作業の進行状態が表示される構成となっている。また、水流確認窓(5)は、殺菌処理中に水が正常に流れていることを確認する為の窓であり、配置されたパイプの内部において水流が流れているかを、目視により確認することが出来る構成となっている。   In addition to the lid (3), a touch panel (4) and a water flow confirmation window (5) are provided on the upper surface of the endoscope sterilization apparatus using ozone water, in a portion that cannot be opened and closed. The touch panel (4) serves as both a touch panel operation panel and a liquid crystal display panel for status display. By touching the operation content displayed on the touch panel (4), a sterilization operation is performed. In addition, the progress status of the current work is displayed. Further, the water flow confirmation window (5) is a window for confirming that water is flowing normally during the sterilization treatment, and visually confirming whether the water flow is flowing inside the arranged pipe. It has a configuration that can.

図4に示す如く、(7)は電源スイッチである。(9)は電源インレットであり、電源を入力する端子である。   As shown in FIG. 4, (7) is a power switch. (9) is a power inlet, which is a terminal for inputting power.

外装(1)の背面部分に給水口(6)が設けられており、水道から水道水が、オゾン水を生成するために用いる原水として、供給されるように構成されている。外装(1)の背面には、更に排水口(12)が設けられており、殺菌処理後の水を排出すべく構成している。(13)は、オゾン水による内視鏡殺菌装置の移動を可能とするキャスタである。   The water supply port (6) is provided in the back surface part of the exterior (1), and it is comprised so that tap water may be supplied as raw | natural water used in order to produce | generate ozone water from water supply. A drain port (12) is further provided on the back surface of the exterior (1), and is configured to discharge water after sterilization treatment. (13) is a caster that enables the endoscope sterilizer to move with ozone water.

次に、図4から図6において、オゾン水による内視鏡殺菌装置の内部の詳細について説明する。   Next, details of the inside of the endoscope sterilizer using ozone water will be described with reference to FIGS.

殺菌槽(2)の内部には、内視鏡接続口(14)が設けられている。該内視鏡接続口(14)に、殺菌用チューブ(50)を介して、内視鏡(10)を取り付ける。オゾン水は、該内視鏡接続口(14)から、殺菌用チューブ(50)を介して、内視鏡(10)のチャンネル内に噴出されるように構成している。   An endoscope connection port (14) is provided inside the sterilization tank (2). The endoscope (10) is attached to the endoscope connection port (14) through the sterilizing tube (50). Ozone water is configured to be ejected from the endoscope connection port (14) into the channel of the endoscope (10) through the sterilization tube (50).

本体内には、オゾン水による内視鏡殺菌装置の為にオゾンガスを生成するオゾンガス生成ユニットが配置されている。該オゾンガス生成ユニットの内部には、オゾンガスを生成する為のオゾナイザが内包されている。酸素ボンベの酸素ガスがオゾンガス生成ユニットへ酸素供給口(41)から供給されて、オゾンガスが該酸素ガスからオゾナイザにより生成される。該生成されたオゾンガスが本体内のオゾン水生成ユニットにおいて原水に注入されて、オゾン水が生成される。   An ozone gas generation unit that generates ozone gas for an endoscope sterilizer using ozone water is disposed in the body. The ozone gas generation unit includes an ozonizer for generating ozone gas. Oxygen gas in the oxygen cylinder is supplied to the ozone gas generation unit from the oxygen supply port (41), and ozone gas is generated from the oxygen gas by an ozonizer. The generated ozone gas is injected into the raw water in the ozone water generation unit in the main body to generate ozone water.

オゾン水生成ユニットにおいて生成されたオゾン水は、本体内の内視鏡殺菌ユニットから、内視鏡接続口(14)を介して、内視鏡(10)のチャンネルの内部に流し込まれる。本体内の中段には、水供給ポンプ(37)が設けられている。該水供給ポンプ(37)により、オゾン水生成ユニットと、オゾン水濃度計(29)と、内視鏡殺菌ユニットへ送水が行われる。   The ozone water generated in the ozone water generation unit is poured into the channel of the endoscope (10) from the endoscope sterilization unit in the main body through the endoscope connection port (14). A water supply pump (37) is provided in the middle stage of the body. The water supply pump (37) supplies water to the ozone water generation unit, the ozone water concentration meter (29), and the endoscope sterilization unit.

オゾン水濃度計(29)は、オゾン水生成ユニットで生成されるオゾン水の溶存オゾン濃度を検出するための溶存オゾン濃度計である。   The ozone water concentration meter (29) is a dissolved ozone concentration meter for detecting the dissolved ozone concentration of the ozone water generated by the ozone water generation unit.

また、本体内の下段に、オゾン分解ユニットが設けられている。該オゾン分解ユニットは、殺菌槽(2)内においてオゾン水から分離したオゾンガスを安全な酸素ガスに分解して、外部に排出する為の装置である。   In addition, an ozonolysis unit is provided in the lower part of the main body. The ozone decomposing unit is an apparatus for decomposing ozone gas separated from ozone water in the sterilization tank (2) into safe oxygen gas and discharging it to the outside.

このような構成において、図6に示す如く、水供給ポンプ(37)によりオゾン水生成ユニットからオゾン水供給経路を介して送られるオゾン水の一部を連続的にサンプリングして、処理中のオゾン水の溶存オゾン濃度を検出し続ける為のオゾン水濃度計(29)が、本体内の上段に配置されている。図7に示す如く、該オゾン水濃度計(29)は、UV光源部(57)とUV受光部(58)とオゾン水注入口(59)とオゾン水排出口(60)とエア排出口(67)とから構成されている。オゾン水濃度計(29)及び水供給ポンプ(37)は、図示せぬ制御手段に接続されている。制御手段は、予め記憶しているオゾン水濃度計(29)の測定処理プログラム及び後述するオゾン水の溶存オゾン濃度測定方法に係る所定の制御プログラムを実行することができる。制御手段は、オゾン水濃度計(29)と水供給ポンプ(37)を制御して、サンプリングした原水又はオゾン水をオゾン水注入口(59)に供給して、UV光源部(57)からのUV(紫外線)をオゾン水に照射して、UV受光部(58)により受光し、このUV光の減衰度により、オゾン水の溶存オゾン濃度を決定する。すなわち、制御手段は、UV受光部(58)により検出される、原水通水時の紫外線透過量と当該原水にオゾンガスを注入することで生成されるオゾン水の紫外線透過量との比に基づいて溶存オゾン濃度を算出する。   In such a configuration, as shown in FIG. 6, a portion of the ozone water sent from the ozone water generation unit via the ozone water supply path is continuously sampled by the water supply pump (37), and the ozone being processed is An ozone water concentration meter (29) for continuously detecting the dissolved ozone concentration of water is arranged at the upper stage in the main body. As shown in FIG. 7, the ozone water concentration meter (29) includes a UV light source part (57), a UV light receiving part (58), an ozone water inlet (59), an ozone water outlet (60), and an air outlet ( 67). The ozone water concentration meter (29) and the water supply pump (37) are connected to control means (not shown). The control means can execute a predetermined control program related to a measurement process program of the ozone water concentration meter (29) stored in advance and a dissolved ozone concentration measurement method of ozone water described later. The control means controls the ozone water concentration meter (29) and the water supply pump (37) to supply the sampled raw water or ozone water to the ozone water inlet (59), and from the UV light source part (57). The ozone water is irradiated with UV (ultraviolet light) and received by the UV light receiving section (58), and the dissolved ozone concentration of the ozone water is determined by the attenuation of the UV light. That is, the control means is based on the ratio between the amount of ultraviolet light transmitted when the raw water is passed and the amount of transmitted ultraviolet light of ozone water generated by injecting ozone gas into the raw water detected by the UV light receiver (58). Calculate the dissolved ozone concentration.

しかし、オゾン水を生成する際に用いる原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合、オゾン水濃度計(29)による測定時に、本来の溶存オゾン濃度よりも低い値として測定されてしまい、オゾン水の溶存オゾン濃度を正確に測定することができない。故に、当該物質を含むような場合においても、正確に溶存オゾン濃度を測定することができるようにする必要がある。以下においては、当該物質を含むような場合においても、オゾン水濃度計(29)を制御して、オゾン水の溶存オゾン濃度を正確に測定することができるオゾン水の溶存オゾン濃度測定方法を説明する。   However, when the raw water used for generating ozone water contains a substance whose ultraviolet ray transmission amount changes due to reaction with ozone, it is lower than the original dissolved ozone concentration when measured by the ozone water concentration meter (29). It is measured as a value, and the dissolved ozone concentration of ozone water cannot be measured accurately. Therefore, it is necessary to be able to accurately measure the dissolved ozone concentration even when the substance is contained. In the following, a method for measuring the dissolved ozone concentration of ozone water that can accurately measure the dissolved ozone concentration of ozone water by controlling the ozone water concentration meter (29) even when the substance is contained is described. To do.

次に、オゾン水の溶存オゾン濃度測定方法について図8及び図9を用いて説明する。
オゾン水の溶存オゾン濃度測定方法は、原水にオゾンガスを注入してオゾン水を生成する際に、当該オゾン水の紫外線透過量の変化に基づいてオゾン水の溶存オゾン濃度を測定する方法であって、図8に示すように、注入前透過量取得工程S10と、原点C0設定工程S20と、オゾンガス注入開始工程S30と、注入開始後透過量取得工程S40と、判定工程S50と、原点C0再設定工程S60と、目標濃度判定工程S70とを主に有する。
Next, the dissolved ozone concentration measuring method of ozone water is demonstrated using FIG.8 and FIG.9.
The dissolved ozone concentration measuring method of ozone water is a method for measuring the dissolved ozone concentration of ozone water based on the change in the amount of ultraviolet light transmitted through the ozone water when ozone gas is generated by injecting ozone gas into raw water. 8, pre-injection permeation amount acquisition step S10, origin C 0 setting step S20, ozone gas injection start step S30, post-injection permeation amount acquisition step S40, determination step S50, and origin C 0. It mainly includes a resetting step S60 and a target density determination step S70.

注入前透過量取得工程S10は、原水に対してオゾンガスを注入する前に原水の紫外線透過量(以下、原水透過光量Caともいう)を所定時間毎に取得する工程である。すなわち、注入前透過量取得工程S10では、オゾン水生成ユニットにより原水に対してオゾンガスが注入される前に、オゾン水濃度計(29)により、UV光源部(57)からUV光(紫外光)を原水に照射して、当該原水を透過したUV光をUV受光部(58)により受光し、このUV光の透過光量として原水透過光量Caが取得される。   The pre-injection transmission amount acquisition step S10 is a step of acquiring the ultraviolet transmission amount of raw water (hereinafter also referred to as raw water transmitted light amount Ca) at predetermined time intervals before injecting ozone gas into the raw water. That is, in the permeation amount acquisition step S10 before injection, before ozone gas is injected into the raw water by the ozone water generation unit, the ozone light concentration meter (29) causes the UV light source (57) to emit UV light (ultraviolet light). Is irradiated to the raw water, the UV light transmitted through the raw water is received by the UV light receiving unit (58), and the raw water transmitted light amount Ca is acquired as the transmitted light amount of the UV light.

具体的には、注入前透過量取得工程S10では、原水に対してオゾンガスを注入する前に原水の紫外線透過量を所定時間毎(本実施形態では、0.2秒毎)に検出するとともに、過去所定時間(本実施形態では、5.0秒間)に検出された原水の紫外線透過量の平均値Cbを取得し、当該原水の紫外線透過量の平均値Cbと、当該原水の紫外線透過量の平均値Cbと同様にして取得される前記過去所定時間(本実施形態では、5.0秒間)の直前に取得した原水の紫外線透過量の平均値(5秒前に取得された平均値Cb)とを比較し、その差が規定値内の場合に、当該原水の紫外線透過量の平均値Cbを前記オゾンガスを注入する前の原水の紫外線透過量である原水透過光量Caとする。すなわち、本実施形態では、5.0秒間の原水の紫外線透過量の平均値Cbを取得し、当該平均値Cbと、当該平均値Cbの5.0秒前に取得された原水の紫外線透過量の平均値Cbとを比較し、その差が規定値内であれば当該平均値Cbを原水透過光量Caとする。
ここで、上記規定値を設定する理由は、原水中に泡等が存在することにより、紫外線透過が不安定となる状態で測定された原水の紫外線透過量を原水透過光量Caとして採用しないためである。上記規定値内にならない場合は、規定値内になるまで継続して平均値Cbを取得する。
Specifically, in the pre-injection transmission amount acquisition step S10, before the ozone gas is injected into the raw water, the ultraviolet transmission amount of the raw water is detected every predetermined time (in this embodiment, every 0.2 seconds), and The average value Cb of the ultraviolet transmission amount of the raw water detected in the past predetermined time (5.0 seconds in the present embodiment) is acquired, and the average value Cb of the ultraviolet transmission amount of the raw water and the ultraviolet transmission amount of the raw water are calculated. Average value of the amount of ultraviolet light transmitted through the raw water just before the predetermined time (5.0 seconds in this embodiment) acquired in the same manner as the average value Cb (average value Cb acquired five seconds before) When the difference is within the specified value, the average value Cb of the ultraviolet transmission amount of the raw water is set as the raw water transmission light amount Ca which is the ultraviolet transmission amount of the raw water before the ozone gas is injected. That is, in this embodiment, the average value Cb of the ultraviolet transmission amount of raw water for 5.0 seconds is acquired, and the ultraviolet transmission amount of raw water acquired 5.0 seconds before the average value Cb and the average value Cb. The average value Cb is compared, and if the difference is within the specified value, the average value Cb is set as the raw water transmitted light amount Ca.
Here, the reason why the specified value is set is that the ultraviolet ray transmission amount of the raw water measured in a state where the ultraviolet ray transmission becomes unstable due to the presence of bubbles or the like in the raw water is not adopted as the raw water transmission light amount Ca. is there. If the value does not fall within the specified value, the average value Cb is continuously acquired until the value falls within the specified value.

原点C0設定工程S20は、注入前透過量取得工程S10にて取得された前記原水の紫外線透過量である原水透過光量Caをオゾン水の溶存オゾン濃度が0mg/L(原点)となる原点光量C0として設定する工程である。 In the origin C 0 setting step S20, the raw water transmitted light amount Ca, which is the ultraviolet light transmitted amount of the raw water acquired in the pre-injection transmission amount acquisition step S10, is converted into the origin light amount where the dissolved ozone concentration of ozone water becomes 0 mg / L (origin) a step of setting as C 0.

オゾンガス注入開始工程S30は、原水にオゾンガスを注入する工程である。すなわち、オゾンガス注入開始工程S30では、オゾナイザにより生成されたオゾンガスがオゾン水生成ユニットにより原水に注入されて、オゾン水が生成される。   The ozone gas injection start step S30 is a step of injecting ozone gas into the raw water. That is, in the ozone gas injection start step S30, the ozone gas generated by the ozonizer is injected into the raw water by the ozone water generation unit to generate ozone water.

注入開始後透過量取得工程S40は、前記オゾンガス注入開始後にオゾン水の紫外線透過量(注入開始後透過光量C。以下、透過光量Cともいう)を所定時間毎に取得する工程である。すなわち、注入開始後透過量取得工程S40では、オゾン水生成ユニットにより原水に対してオゾンガスが注入開始された後、オゾン水濃度計(29)により、UV光源部(57)からUV光(紫外光)をオゾン水に照射して、当該オゾン水を透過したUV光をUV受光部(58)により受光し、このUV光の透過光量である紫外線透過量が所定時間毎に取得される。   The post-injection transmission amount acquisition step S40 is a step of acquiring an ultraviolet transmission amount of ozone water after the start of the ozone gas injection (transmission light amount C after the start of injection; hereinafter also referred to as transmitted light amount C) every predetermined time. That is, in the permeation amount acquisition step S40 after the start of injection, after ozone gas is started to be injected into the raw water by the ozone water generation unit, UV light (ultraviolet light) is emitted from the UV light source unit (57) by the ozone water concentration meter (29). ) Is irradiated to the ozone water, the UV light transmitted through the ozone water is received by the UV light receiving unit (58), and the amount of transmitted UV light, which is the amount of transmitted UV light, is acquired every predetermined time.

具体的には、前記注入開始後透過量取得工程S40では、前記オゾンガス注入開始後にオゾン水の紫外線透過量を所定時間毎(本実施形態では、0.2秒毎)に検出するとともに、過去所定時間(本実施形態では、1.0秒間)に検出されたオゾン水の紫外線透過量の平均値を求め、当該平均値を透過光量Cとして取得する。   Specifically, in the transmission amount acquisition step S40 after the start of injection, the ultraviolet transmission amount of ozone water is detected every predetermined time (in this embodiment, every 0.2 seconds) after the start of the ozone gas injection, The average value of the amount of ultraviolet light transmitted through ozone water detected in time (1.0 seconds in the present embodiment) is obtained, and the average value is acquired as transmitted light amount C.

判定工程S50は、注入開始後透過量取得工程S40にて取得されたオゾン水の紫外線透過量である透過光量Cが、原点C0設定工程S20にて設定された原点光量C0よりも小さいかどうかを判定する工程である。判定工程S50において、原点C0設定工程S20にて設定された原点光量C0に対して、オゾンガス注入開始後に取得された透過光量Cが小さいと判定された場合(S50の判定がYESの場合)は、目標濃度判定工程S70に移行する。一方、判定工程S50において、原点C0設定工程S20にて設定された原点光量C0に対して、オゾンガス注入開始後に取得された透過光量Cが小さくないと判定された場合(S50の判定がNOの場合)は、原点C0再設定工程S60に移行する。 In the determination step S50, is the transmitted light amount C, which is the ultraviolet light transmission amount of ozone water acquired in the transmission amount acquisition step S40 after the start of injection, smaller than the origin light amount C 0 set in the origin C 0 setting step S20? It is a step of determining whether or not. In decision step S50, (when the determination of S50 in YES) with respect to the origin amount C 0 set by the origin C 0 setting step S20, if the amount of transmitted light obtained after starting ozone injection C is determined to be smaller Shifts to the target concentration determination step S70. On the other hand, the determination in step S50, with respect to the origin C 0 setting step S20 origin amount C 0 which is set in, a determination if the transmitted light amount C which is acquired after the start ozone gas injected are determined to be smaller (S50 NO In this case), the process proceeds to the origin C 0 resetting step S60.

原点C0再設定工程S60は、判定工程S50にて前記オゾン水の紫外線透過量である透過光量Cが、原点C0設定工程S20にて設定された原点光量C0よりも小さくないと判定された場合に、当該オゾン水の紫外線透過量である透過光量Cをオゾン水の溶存オゾン濃度が0mg/L(原点)となる原点光量C0として再設定する工程である。その後、オゾン水に継続してオゾンガスを注入し(S80)、注入開始後透過量取得工程S40に戻る。 In the origin C 0 resetting step S60, it is determined in the determination step S50 that the transmitted light amount C that is the ultraviolet light transmission amount of the ozone water is not smaller than the origin light amount C 0 set in the origin C 0 setting step S20. In this case, the transmitted light amount C which is the ultraviolet light transmitted amount of the ozone water is reset as the origin light amount C 0 at which the dissolved ozone concentration of the ozone water becomes 0 mg / L (origin). Thereafter, ozone gas is continuously injected into the ozone water (S80), and the process returns to the permeation amount acquisition step S40 after the injection is started.

目標濃度判定工程S70は、判定工程S50にて前記オゾン水の紫外線透過量である透過光量Cが、原点C0設定工程S20にて設定された原点光量C0よりも小さいと判定された場合に、オゾン水の溶存オゾン濃度が所定の目標濃度に達したかどうかを判定する工程である。目標濃度判定工程S70において、オゾン水の溶存オゾン濃度が所定の目標濃度に達したと判定された場合(S70の判定がYESの場合)は、オゾンガスを注入停止し(S90)、その後注入開始後透過量取得工程S40に戻る。一方、オゾン水の溶存オゾン濃度が所定の目標濃度に達していないと判定された場合(S70の判定がNOの場合)は、オゾン水にオゾンガスを継続して注入し(S100)、注入開始後透過量取得工程S40に戻る。 In the target concentration determination step S70, when it is determined in the determination step S50 that the transmitted light amount C, which is the ultraviolet light transmission amount of the ozone water, is smaller than the origin light amount C 0 set in the origin C 0 setting step S20. This is a step of determining whether or not the dissolved ozone concentration of the ozone water has reached a predetermined target concentration. In the target concentration determination step S70, when it is determined that the dissolved ozone concentration of the ozone water has reached the predetermined target concentration (when the determination in S70 is YES), the injection of ozone gas is stopped (S90), and then the injection is started. The process returns to the transmission amount acquisition step S40. On the other hand, when it is determined that the dissolved ozone concentration of the ozone water does not reach the predetermined target concentration (when the determination in S70 is NO), ozone gas is continuously injected into the ozone water (S100), and after the injection starts The process returns to the transmission amount acquisition step S40.

図9は、本発明の一実施形態に係るオゾン水の溶存オゾン濃度測定方法を説明するための説明図であり、(a)は紫外線透過量の経時変化を示す図、(b)は溶存オゾン濃度の経時変化を示す図である。   FIG. 9 is an explanatory diagram for explaining a method for measuring the dissolved ozone concentration of ozone water according to an embodiment of the present invention. FIG. 9A is a diagram showing a change with time in the amount of transmitted UV light, and FIG. It is a figure which shows the time-dependent change of a density | concentration.

図9に示すように、原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合、オゾン水を生成するために原水にオゾンガスを注入すると、当該物質の影響で紫外線透過量が増加する方向に変動する。これに対処するため、上述したオゾン水の溶存オゾン濃度測定方法では、原水透過光量Ca(図9(a)に示す初期の原水光量)の代わりにオゾンガス注入後に取得された透過光量Cの最大値(図9(a)の矢印Aで示す部分)を修正原水光量として設定するものである。そして、図9(a)で示す透過光量Cを、図9(b)に示すように、溶存オゾン濃度に換算した結果、原水透過光量Caを原点光量C0として用いた場合では溶存オゾン濃度が小さく算出される(図9(b)に示す「修正前の濃度」)が、修正原水光量として透過光量Cの最大値を原点光量C0として用いた場合では当該物質による溶存オゾン濃度の減少分も考慮されるため、正確な溶存オゾン濃度(図9(b)に示す「修正後の濃度」)を測定することができる。また、このように、当該物質の影響により透過光量Cが設定された原点光量C0より小さくなる場合、オゾンガス注入後に取得された透過光量Cの最大値を自動的に原点光量C0として用いることができるように、制御手段に図8に示すフローに基づいて作製した制御プログラム(透過光量Cの最大値を算出するプログラムも含む)を記憶させ、制御手段が当該制御プルグラムを実行できるようにすればよい。 As shown in FIG. 9, when the raw water contains a substance whose ultraviolet ray transmission amount changes due to the reaction with ozone, if ozone gas is injected into the raw water to generate ozone water, the ultraviolet ray transmission amount is affected by the substance. Fluctuates in an increasing direction. In order to cope with this, in the dissolved ozone concentration measuring method described above, the maximum value of the transmitted light amount C acquired after ozone gas injection instead of the raw water transmitted light amount Ca (the initial raw water light amount shown in FIG. 9A). (A portion indicated by an arrow A in FIG. 9A) is set as the corrected raw water quantity. 9A is converted into a dissolved ozone concentration as shown in FIG. 9B. As a result, when the raw water transmitted light amount Ca is used as the origin light amount C 0 , the dissolved ozone concentration is When the maximum value of the transmitted light amount C is used as the corrected raw water light amount as the origin light amount C 0 (“concentration before correction” shown in FIG. 9B), the decrease in dissolved ozone concentration due to the substance is calculated. Therefore, an accurate dissolved ozone concentration (“concentration after correction” shown in FIG. 9B) can be measured. Further, in this way, when the transmitted light amount C is smaller than the set origin light amount C 0 due to the influence of the substance, the maximum value of the transmitted light amount C acquired after the ozone gas injection is automatically used as the origin light amount C 0. 8 is stored in the control means (including a program for calculating the maximum value of the transmitted light amount C) so that the control means can execute the control program. That's fine.

次に、本発明の実施形態に係るオゾン水の溶存オゾン濃度測定方法を実施するための装置の別の例としてオゾン水によるオゾン殺菌装置の構成を図10を用いて説明する。   Next, the configuration of an ozone sterilizer using ozone water will be described with reference to FIG. 10 as another example of an apparatus for carrying out the dissolved ozone concentration measuring method of ozone water according to an embodiment of the present invention.

図10に示すように、殺菌槽(300)は、殺菌対象物が収容される殺菌槽であって、当該殺菌槽(300)にオゾン水製造装置(310)、オゾン水濃度測定器(360)及び排オゾンガス分解器(330)が接続される。オゾン水製造装置(310)は、当該オゾン水製造装置(310)から殺菌槽(300)にオゾン水を供給できるようになっており、当該殺菌槽(300)にオゾン水を供給することで殺菌槽(300)内の殺菌対象物を殺菌することができる。
なお、オゾン水濃度測定器(360)は、上述したオゾン水濃度計(29)と同様に紫外線透過光量によりオゾン水の溶存オゾン水濃度を測定することができる。
As shown in FIG. 10, the sterilization tank (300) is a sterilization tank in which an object to be sterilized is accommodated, and the sterilization tank (300) includes an ozone water production apparatus (310) and an ozone water concentration measuring device (360). And an exhaust ozone gas decomposer (330). The ozone water production apparatus (310) can supply ozone water from the ozone water production apparatus (310) to the sterilization tank (300), and sterilizes by supplying ozone water to the sterilization tank (300). The object to be sterilized in the tank (300) can be sterilized.
In addition, the ozone water concentration measuring device (360) can measure the dissolved ozone water concentration of ozone water by the amount of transmitted ultraviolet light in the same manner as the ozone water concentration meter (29) described above.

殺菌槽(300)内に供給されたオゾン水は、水ポンプ(320)で排水され、殺菌槽(300)に溜まったオゾンは、排オゾンガス分解器(330)を介してブロア(340)を介して排気することができる。当該排オゾンガス分解器(330)では、オゾンが分解されてブロア(340)ヘ排出されるようになっている。   The ozone water supplied into the sterilization tank (300) is drained by the water pump (320), and the ozone accumulated in the sterilization tank (300) passes through the exhaust ozone gas decomposer (330) and the blower (340). Can be exhausted. In the exhaust ozone gas decomposer (330), ozone is decomposed and discharged to the blower (340).

殺菌槽(300)には、オゾン水濃度測定器(360)が設けられ、そのオゾン水濃度測定器(360)の検出値が、電気信号として制御回路(370)に入力され、その制御回路(370)で、オゾン水濃度・時間の積(CT値)が一定となるように制御することができる。例えば、オゾン水濃度測定器(360)で溶存オゾン濃度を測定し、制御回路(370)の演算回路(380)とタイマー回路(390)で溶存オゾン水濃度を積分してその積分値(CT)が所定になったときに殺菌を停止するようにすることができる。   The sterilization tank (300) is provided with an ozone water concentration measuring device (360), and the detected value of the ozone water concentration measuring device (360) is input to the control circuit (370) as an electric signal, and the control circuit ( 370), the product of ozone water concentration and time (CT value) can be controlled to be constant. For example, the dissolved ozone concentration is measured by the ozone water concentration measuring device (360), the dissolved ozone water concentration is integrated by the arithmetic circuit (380) and the timer circuit (390) of the control circuit (370), and the integrated value (CT). The sterilization can be stopped when becomes a predetermined value.

具体的には、制御回路(370)は、演算回路(380)とタイマー回路(390)からなり、演算回路(380)が、オゾン水濃度測定器(360)から出力された溶存オゾン水濃度(C)の電気信号を、タイマー回路(390)から出力される時間(T)で積分して積分値(CT)を演算し、その値が予め殺菌対象物毎に定めた値になったとき、殺菌工程を停止するように制御することができる。   Specifically, the control circuit (370) includes an arithmetic circuit (380) and a timer circuit (390). The arithmetic circuit (380) outputs the dissolved ozone water concentration (360) output from the ozone water concentration measuring device (360). When the electrical value of C) is integrated by the time (T) output from the timer circuit (390) to calculate the integral value (CT), and the value becomes a value determined in advance for each sterilization target, It can be controlled to stop the sterilization process.

この際、制御回路(370)は、ブロア(340)、オゾン水製造装置(310)、水ポンプ(320)を制御してオゾン水供給量、排水量、排オゾンガス量を制御する。   At this time, the control circuit (370) controls the blower (340), the ozone water production device (310), and the water pump (320) to control the ozone water supply amount, the drainage amount, and the exhaust ozone gas amount.

またオゾン水濃度測定器(360)の代わりに液相オゾンCT値検出器で、CT値を直接検出し制御回路(370)がそのCT値が所定に達したときに殺菌を停止するようにしてもよい。   Further, instead of the ozone water concentration measuring device (360), a liquid phase ozone CT value detector detects the CT value directly, and the control circuit (370) stops sterilization when the CT value reaches a predetermined value. Also good.

このような構成されたオゾン水によるオゾン殺菌装置では、上述したオゾン水による内視鏡殺菌装置と同様に原水通水時の紫外線透過量と当該原水にオゾンガスを注入することで生成されるオゾン水の紫外線透過量との比に基づいて溶存オゾン濃度が算出される。   In the ozone sterilizer using ozone water configured as described above, the ozone water generated by injecting ozone gas into the raw water and the amount of transmitted ultraviolet light when the raw water is passed, as in the above-described endoscope sterilizer using ozone water. The dissolved ozone concentration is calculated on the basis of the ratio to the amount of UV transmitted.

しかし、オゾン水を生成する際に用いる原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合、オゾン水濃度測定器(360)による測定時に、本来の溶存オゾン濃度よりも低い値として測定されてしまい、オゾン水の溶存オゾン濃度を正確に測定することができない。故に、当該物質を含むような場合においても、正確に溶存オゾン濃度を測定することができるようにする必要がある。そこで、このオゾン殺菌装置においても、上記オゾン水の溶存オゾン濃度測定方法を用いることで、当該物質を含むような場合においても、オゾン水濃度測定器(360)を制御して、オゾン水の溶存オゾン濃度を正確に測定することができる。   However, when the raw water used for generating ozone water contains a substance whose ultraviolet transmission amount changes due to the reaction with ozone, it is more than the original dissolved ozone concentration when measured by the ozone water concentration meter (360). It is measured as a low value, and the dissolved ozone concentration of ozone water cannot be measured accurately. Therefore, it is necessary to be able to accurately measure the dissolved ozone concentration even when the substance is contained. Therefore, even in this ozone sterilization apparatus, the ozone water concentration measuring device (360) is controlled by using the method for measuring the dissolved ozone concentration of the ozone water, so that the ozone water concentration measuring device (360) is dissolved. The ozone concentration can be measured accurately.

以上の如く、本実施形態に係るオゾン水の溶存オゾン濃度測定方法によれば、原水にオゾンとの反応により紫外線透過量が変化する物質が含まれている場合でも、当該物質に影響されることなく、オゾン水の溶存オゾン濃度を正確に測定することができる。本明細書で説明したように、当該物質を含む場合、原点光量を修正しないと、本来の溶存オゾン濃度よりも低い値としてオゾン水の溶存オゾン濃度が測定されてしまうため、溶存オゾン濃度を所定の目標濃度に保つ際に、過剰のオゾンガスを注入することになる。しかし、本実施形態の如く、当該物質を含む場合、原点光量を適宜修正することで、このような過剰のオゾンガスを注入することを防止できる。過剰なオゾンガスの注入を防止できれば、オゾンガス生成によるエネルギーの過剰消費、設定よりも高い溶存オゾン濃度による部材の劣化、オゾン分解ユニットが有する触媒等のオゾン分解機能の早期劣化なども抑制することができる。   As described above, according to the method for measuring the dissolved ozone concentration of ozone water according to the present embodiment, even when the raw water contains a substance that changes the amount of transmitted ultraviolet light by reaction with ozone, it is affected by the substance. The dissolved ozone concentration of ozone water can be accurately measured. As described in the present specification, when the substance is included, if the origin light amount is not corrected, the dissolved ozone concentration is measured as a value lower than the original dissolved ozone concentration. When maintaining the target concentration, excess ozone gas is injected. However, when the substance is contained as in the present embodiment, it is possible to prevent such excessive ozone gas from being injected by appropriately correcting the light amount at the origin. If injection of excessive ozone gas can be prevented, excessive consumption of energy due to generation of ozone gas, deterioration of members due to dissolved ozone concentration higher than the setting, early deterioration of ozone decomposition function such as a catalyst of the ozone decomposition unit can be suppressed. .

1 外装
2 殺菌槽
3 蓋体
4 タッチパネル
5 水流確認窓
6 給水口
10 内視鏡
14 内視鏡接続口
29 オゾン水濃度計
37 水供給ポンプ
50 殺菌用チューブ
57 UV光源部
58 UV受光部
59 オゾン水注入口
67 エア排出口
DESCRIPTION OF SYMBOLS 1 Exterior 2 Sterilization tank 3 Lid 4 Touch panel 5 Water flow confirmation window 6 Water supply port 10 Endoscope 14 Endoscope connection port 29 Ozone water concentration meter 37 Water supply pump 50 Sterilization tube 57 UV light source unit 58 UV light receiving unit 59 Ozone Water inlet 67 Air outlet

Claims (4)

原水にオゾンガスを注入してオゾン水を生成する際に、当該オゾン水の紫外線透過量の変化に基づいてオゾン水の溶存オゾン濃度を測定する方法であって、
前記原水に対して前記オゾンガスを注入する前に前記原水の紫外線透過量を所定時間毎に取得する注入前透過量取得工程と、
前記注入前透過量取得工程にて取得された前記原水の紫外線透過量を原点光量として設定する原点設定工程と、
前記原水に前記オゾンガスを注入する注入工程と、
前記オゾンガス注入開始後に前記オゾン水の紫外線透過量を所定時間毎に取得する注入開始後透過量取得工程と、
前記注入開始後透過量取得工程にて取得された前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さいかどうかを判定する判定工程と、
前記判定工程にて前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さくないと判定された場合に、当該オゾン水の紫外線透過量を原点光量として再設定する原点再設定工程と、を有することを特徴とするオゾン水の溶存オゾン濃度測定方法。
When ozone gas is injected into raw water to generate ozone water, a method of measuring the dissolved ozone concentration of ozone water based on the change in the amount of ultraviolet light transmitted through the ozone water,
A pre-injection permeation amount acquisition step of acquiring the ultraviolet light permeation amount of the raw water every predetermined time before injecting the ozone gas into the raw water;
An origin setting step for setting the ultraviolet light transmission amount of the raw water acquired in the transmission amount acquisition step before injection as an origin light amount,
An injection step of injecting the ozone gas into the raw water;
A post-injection transmission amount acquisition step of acquiring the ultraviolet transmission amount of the ozone water every predetermined time after the ozone gas injection start;
A determination step of determining whether or not the amount of ultraviolet light transmitted through the ozone water acquired in the transmission amount acquisition step after the start of injection is smaller than the origin light amount set in the origin setting step;
The origin for resetting the ultraviolet light transmission amount of the ozone water as the origin light amount when it is determined in the determination step that the ultraviolet light transmission amount of the ozone water is not smaller than the origin light amount set in the origin setting step. A method for measuring the dissolved ozone concentration of ozone water, comprising: a resetting step.
前記注入開始後透過量取得工程では、前記オゾンガス注入開始後に前記オゾン水の紫外線透過量を所定時間毎に検出するとともに、過去所定時間に検出された前記オゾン水の紫外線透過量の平均値を取得することを特徴とする請求項1に記載のオゾン水の溶存オゾン濃度測定方法。   In the permeation amount acquisition process after the start of injection, the UV light transmission amount of the ozone water is detected every predetermined time after the ozone gas injection is started, and the average value of the UV light transmission amount detected in the past predetermined time is acquired. The method for measuring a dissolved ozone concentration of ozone water according to claim 1. 前記注入前透過量取得工程では、前記原水に対して前記オゾンガスを注入する前に前記原水の紫外線透過量を所定時間毎に検出するとともに、過去所定時間に検出された前記原水の紫外線透過量の平均値を取得し、当該原水の紫外線透過量の平均値と、当該原水の紫外線透過量の平均値と同様にして取得される前記過去所定時間の直前に取得した前記原水の紫外線透過量の平均値とを比較し、その差が規定値内の場合に、当該原水の紫外線透過量の平均値を前記オゾンガスを注入する前の前記原水の紫外線透過量とすることを特徴とする請求項1または請求項2に記載のオゾン水の溶存オゾン濃度測定方法。   In the pre-injection transmission amount acquisition step, the ultraviolet transmission amount of the raw water is detected every predetermined time before the ozone gas is injected into the raw water, and the ultraviolet transmission amount of the raw water detected in the past predetermined time is detected. An average value is obtained, and an average value of the ultraviolet transmission amount of the raw water and an average value of the ultraviolet transmission amount of the raw water obtained immediately before the past predetermined time obtained in the same manner as the average value of the ultraviolet transmission amount of the raw water. When the difference is within a prescribed value, the average value of the amount of ultraviolet light transmitted through the raw water is set as the amount of ultraviolet light transmitted through the raw water before the ozone gas is injected. The dissolved ozone concentration measuring method of the ozone water according to claim 2. 前記判定工程にて前記オゾン水の紫外線透過量が、原点設定工程にて設定された原点光量よりも小さいと判定された場合に、前記オゾン水の溶存オゾン濃度が所定の目標濃度に達したかどうかを判定する目標濃度判定工程を、さらに有することを特徴とする請求項1から請求項3の何れか一項に記載のオゾン水の溶存オゾン濃度測定方法。   Whether the dissolved ozone concentration of the ozone water has reached a predetermined target concentration when it is determined in the determination step that the ultraviolet light transmission amount of the ozone water is smaller than the light amount of origin set in the origin setting step The method for measuring a dissolved ozone concentration of ozone water according to any one of claims 1 to 3, further comprising a target concentration determination step of determining whether or not.
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