JPS6291289A - Apparatus for purifying drinking water - Google Patents

Apparatus for purifying drinking water

Info

Publication number
JPS6291289A
JPS6291289A JP23265185A JP23265185A JPS6291289A JP S6291289 A JPS6291289 A JP S6291289A JP 23265185 A JP23265185 A JP 23265185A JP 23265185 A JP23265185 A JP 23265185A JP S6291289 A JPS6291289 A JP S6291289A
Authority
JP
Japan
Prior art keywords
temp
drinking water
ozone
water
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP23265185A
Other languages
Japanese (ja)
Inventor
Tokumitsu Ezaki
徳光 江崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP23265185A priority Critical patent/JPS6291289A/en
Publication of JPS6291289A publication Critical patent/JPS6291289A/en
Pending legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To facilitate the efficiency of deodorizing/sterilizing treatment, etc., by controlling the temp. of raw drinking water in an ozone reaction tower by a temp. controller and aerating said raw drinking water with ozonized gas from an air-diffusing device. CONSTITUTION:A water receiving valve 8 is opened to supply raw drinking water to an ozone reaction tower 7 and the temp. of the stored raw drinking water is detected by a temp. detector 11 and the detection signal is sent to a temp. controller 13. When the temp of raw drinking water is lower than preset temp. the temp. controller 13 operates a heating device 12 to heat the raw drinking water to the preset temp. After the temp. of the raw drinking water has reached the preset temp., aeration by ozonized gas and the removal of dissolved ozone by sterilized air are performed. By this method, treatment time can be shortened.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は飲料に供される飲料水をより健康的にするため
にオゾン化ガスと滅菌空気により、衛生的でおいしい飲
料水を精製する飲料水精製装置に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is directed to a beverage purification system that purifies hygienic and delicious drinking water using ozonized gas and sterilized air in order to make the drinking water more healthy. Regarding water purification equipment.

[従来の技術] 第2図は、従来から使用されている飲料水m製装置の具
体例を示す。第2図において、(1)は空気供給装置、
(2)はオゾン発生装置、(3)は後述するオゾン反応
塔にオゾン化ガスを供給するラインに取付けられたバル
ブ、(4)はオゾン化ガスを後述するオゾン分解装置を
とおして製造した滅菌空気をオゾン反応塔に供給するラ
インに取付けられたバルブ、(5)はオゾン分解装置、
(6)は供給されたオゾンまたは滅菌空気であるオゾン
分解装置をとおしたガスを散気するための散気管、(7
1はオゾン反応塔、(8)は受水用バルブ、(9)は精
製水を取出すための排出管に取付けられた排出用バルブ
、色はオゾン反応塔より排出するオゾンを分解する排オ
ゾン分解装置である。
[Prior Art] FIG. 2 shows a specific example of a conventionally used drinking water production apparatus. In Fig. 2, (1) is an air supply device;
(2) is an ozone generator, (3) is a valve attached to the line that supplies ozonized gas to the ozone reaction tower (described later), and (4) is a sterilizer that produces ozonized gas through an ozone decomposition device (described later). A valve attached to the line that supplies air to the ozone reaction tower, (5) is an ozone decomposition device,
(6) is a diffuser pipe for diffusing the supplied ozone or sterilized air through the ozone decomposition device; (7)
1 is the ozone reaction tower, (8) is the water receiving valve, (9) is the discharge valve attached to the discharge pipe to take out purified water, and the color is the exhaust ozone decomposition that decomposes the ozone discharged from the ozone reaction tower. It is a device.

第3図は水温が、約5℃、約15℃、または20〜30
℃で、11時間水にオゾン化ガスを曝気したばあいの溶
存オゾン濃度と、その減衰特性との関係を示したグラフ
である。T2 、T3 、T4はそれぞれ水温が約5℃
、約15℃、20〜30℃でのオゾン化ガスを曝気した
のち、滅菌空気で曝気し、溶存オゾンが減衰してオゾン
がなくなるまでの時間を示す。
Figure 3 shows that the water temperature is about 5℃, about 15℃, or 20-30℃.
3 is a graph showing the relationship between dissolved ozone concentration and its attenuation characteristic when water is aerated with ozonized gas for 11 hours at .degree. T2, T3, and T4 each have a water temperature of approximately 5℃.
, about 15°C, and after aerating ozonized gas at 20 to 30°C, aerating with sterile air shows the time taken until dissolved ozone is attenuated and ozone disappears.

第2図において、オゾン化ガスの製造に用いられる空気
は空気供給装置(1)からオゾン発生装置(2)に供給
され、オゾン化されたガスがバルブ(3)により散気管
(6)をとおってオゾン反応塔(′7)に供給される。
In Figure 2, air used to produce ozonized gas is supplied from an air supply device (1) to an ozone generator (2), and the ozonized gas is passed through a diffuser pipe (6) by a valve (3). and supplied to the ozone reaction tower ('7).

供給されたオゾン化ガスは、オゾン反応塔(9内の貯水
飲料原水に殺菌、脱臭に必要な時間である第3図に示す
T+時間曝気される。オゾン化ガスの曝気完了後バルブ
(3)が閉じられ、バルブ(4)が開放され、オゾン発
生装置(2から発生したオゾン化ガスはオゾン分解触媒
を含有するオゾン分解装置(5)を経由して滅菌空気と
なり、溶存オゾンが除去される時間であるT2 、T3
あるいは14時間、散気管(6)に供給される。殺菌、
脱臭された飲料水は精製接水出用バルブ(9)により飲
料水として供給される。受水用バルブ(8)は飲料原水
をオゾン反応塔(7)内に注入するためのものである。
The supplied ozonated gas is aerated to the raw drinking water stored in the ozone reaction tower (9) for T+ time shown in Figure 3, which is the time required for sterilization and deodorization. After the aeration of the ozonated gas is completed, the valve (3) is closed, the valve (4) is opened, and the ozonized gas generated from the ozone generator (2) becomes sterile air via the ozone decomposition device (5) containing an ozone decomposition catalyst, and dissolved ozone is removed. time T2, T3
Alternatively, it is supplied to the diffuser pipe (6) for 14 hours. Sterilization,
The deodorized drinking water is supplied as drinking water by the purified water outlet valve (9). The water receiving valve (8) is for injecting drinking raw water into the ozone reaction tower (7).

[発明が解決しようとする問題点] 従来の飲料水精製装置では、第3図に示されるように1
1時間水にオゾン化ガスを曝気したとき、水温により最
終溶存オゾンの濃度が変化するため、殺菌、脱臭効果の
現れる溶存オゾン濃度に到達する時間および滅菌空気を
曝気する時間を調節しなければならないという問題があ
った。
[Problems to be solved by the invention] In the conventional drinking water purification device, as shown in FIG.
When water is aerated with ozonized gas for one hour, the final concentration of dissolved ozone changes depending on the water temperature, so the time to reach the dissolved ozone concentration that produces sterilizing and deodorizing effects and the time to aerate sterile air must be adjusted. There was a problem.

本発明は上記のような問題点を解決するためになされた
もので、脱臭、殺菌時間を安定化させるとともに、脱臭
あるいは殺菌など処理効率を容易に調整しうる飲料水精
製装置を提供することを目的とするものである。
The present invention has been made in order to solve the above problems, and aims to provide a drinking water purification device that can stabilize the deodorization and sterilization time and easily adjust the processing efficiency such as deodorization and sterilization. This is the purpose.

[問題点を解決するための手段] 本発明はオゾン発生装置、散気装置、オゾン反応塔、オ
ゾン分解装置、温度検出器、加温装置および温度調節器
からなり、オゾン反応塔内の飲料原水が温度調節器で温
度制御され、オゾン化ガスを散気装置から曝気すること
により滅菌かつ脱臭された飲料原水の溶存オゾンが滅菌
空気で除去されるように構成されてなる飲料水精製装置
に関する。
[Means for Solving the Problems] The present invention comprises an ozone generator, an aeration device, an ozone reaction tower, an ozone decomposition device, a temperature detector, a heating device, and a temperature controller, The present invention relates to a drinking water purification device in which the temperature is controlled by a temperature controller, and dissolved ozone in drinking water that has been sterilized and deodorized is removed by aeration of ozonized gas from an aeration device using sterilized air.

[作 用〕 本発明の飲料水精製装置は、加温装置によりオゾン反応
塔内の貯水飲料原水が一定温度まで加温されるので、脱
臭、殺菌などの処理効率を一定に調整することができる
ようにしたものである。
[Function] In the drinking water purification device of the present invention, the drinking raw water stored in the ozone reaction tower is heated to a constant temperature by the heating device, so that treatment efficiency such as deodorization and sterilization can be adjusted to a constant level. This is how it was done.

[実施例] 本発明の一実施態様を第1図にもとづき説明する。[Example] One embodiment of the present invention will be described based on FIG.

第1図において、01)はオゾン反応塔(7)に取付け
られた温度検出器、(12)はオゾン反応塔(力に取付
けられた加温装置、■は温度調節器である。
In FIG. 1, 01) is a temperature detector attached to the ozone reaction tower (7), (12) is a heating device attached to the ozone reaction tower (2), and 2 is a temperature regulator.

飲料原水は受水用バルブ(8)を開にしてオゾン反応塔
(力内に供給され、温度検出器01)によって貯水され
た飲料原水の水温を検出し、その信号を温度調節器0へ
送る。温度調節器■は、飲料原水の水温があらかじめ設
定された温度以下のばあい、加温装置02Jを作動させ
、設定温度になるまで加温される。飲料原水の水温が設
定温度に達したら、従来と同様にしてオゾン化ガスによ
る曝気および滅菌空気による溶存オゾンの除去を行なう
For drinking raw water, open the receiving valve (8), detect the temperature of the stored drinking raw water using the ozone reaction tower (supplied to the inside, and temperature sensor 01), and send the signal to temperature controller 0. . When the temperature of the raw drinking water is lower than a preset temperature, the temperature regulator (2) activates the heating device 02J and is heated until it reaches the set temperature. When the temperature of the raw drinking water reaches the set temperature, aeration with ozonized gas and removal of dissolved ozone with sterilized air are performed in the same manner as in the past.

飲料原水の水温を5℃、15℃あるいは20〜30℃と
し、オゾン化ガスを曝気したときの溶存オゾン量の変化
と外気滅菌空気による溶存オゾン除去特性を第3図に示
す。第3図に示されるようにT1時間後の溶存オゾン量
は水温が高いばあいは少なく、また滅菌空気による溶存
オゾン除去時間も短くなる。
Figure 3 shows the change in the amount of dissolved ozone when the temperature of the drinking raw water is set to 5°C, 15°C, or 20 to 30°C and the ozonized gas is aerated, and the dissolved ozone removal characteristics by sterilized outside air. As shown in FIG. 3, the amount of dissolved ozone after T1 hours is small when the water temperature is high, and the time taken to remove dissolved ozone by sterilized air is also shortened.

ところで、飲料原水中の溶存オゾン濃度は、ある値以上
であれば脱臭、殺菌効果が充分にえられるが、本発明に
おいては飲料原水の水温は20〜30℃の範囲であるの
が好ましい。
By the way, if the dissolved ozone concentration in the drinking raw water is above a certain value, sufficient deodorizing and sterilizing effects can be obtained, but in the present invention, the temperature of the drinking raw water is preferably in the range of 20 to 30°C.

なお、前記実施態様では水温を高くして飲料原水を処理
したばあいを示したが、水温が高くてオゾン処理を充分
に行なうことができないばあいは、加温装置のかわりに
冷却装置を用いてオゾン処理が可能となる水温まで冷却
して処理してもよく、また加温装置および冷却装置の両
方を具備して任意の温度で処理することができるように
してもよい。また前記実施態様ではオゾン反応塔(71
内に飲料原水を貯水し設定温度になるまで加温したが、
第4図に示されるように受水用バルブ(8)とオゾン反
応塔(刀との配管途中に加温装置を設けてもよい。
In addition, although the above embodiment shows the case where drinking raw water is treated by raising the water temperature, if the water temperature is too high to perform sufficient ozone treatment, a cooling device may be used instead of the heating device. The water may be cooled to a water temperature at which ozone treatment is possible, or the water may be treated at any temperature by providing both a heating device and a cooling device. Further, in the embodiment, the ozone reaction tower (71
I stored drinking water inside and heated it until it reached the set temperature, but
As shown in FIG. 4, a heating device may be provided in the middle of the piping between the water receiving valve (8) and the ozone reaction tower.

[発明の効果] 以上述べたように、本発明の装置を用いると、飲料原水
の水温による処理効果への影響がなく、常に一定の品質
の精製水がえられ、また滅菌および脱臭処理時間を短く
することができるという効果を奏する。
[Effects of the Invention] As described above, when the apparatus of the present invention is used, the treatment effect is not affected by the temperature of drinking raw water, purified water of a constant quality can always be obtained, and the time required for sterilization and deodorization treatment can be reduced. This has the effect of being able to be made shorter.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の飲料水精製装置の一実施態様を示す説
明図、第2図は従来の飲料水精製装置を示す説明図、第
3図は水温の相違による溶存オゾン量の変化および滅菌
空気による減衰特性を示すグラフ、第4図は本発明の飲
料水精製装置の他の一実施態様を示す説明図である。 (図面の主要符号) (1):空気供給装置 +2) ニオシン発生装置 (3):バルブ (6)二数気管 (刀ニオシン反応塔 (8):受水用バルブ (9):排出用バルブ 00):排オゾン分解装置 01):温度検出器 az:加温装置 ■:温度調節器
Fig. 1 is an explanatory diagram showing one embodiment of the drinking water purification device of the present invention, Fig. 2 is an explanatory diagram showing a conventional drinking water purification device, and Fig. 3 is an explanatory diagram showing changes in the amount of dissolved ozone due to differences in water temperature and sterilization. A graph showing attenuation characteristics due to air, FIG. 4 is an explanatory diagram showing another embodiment of the drinking water purification apparatus of the present invention. (Main symbols in the drawing) (1): Air supply device + 2) Niosin generator (3): Valve (6) Two trachea (niosin reaction tower (8): Receiving valve (9): Discharge valve 00 ): Exhaust ozone decomposition device 01): Temperature detector az: Warming device ■: Temperature regulator

Claims (1)

【特許請求の範囲】[Claims] (1)オゾン発生装置、散気装置、オゾン反応塔、温度
検出器、加温装置および温度調節器からなり、オゾン反
応塔内の飲料原水が温度調節器で温度制御され、オゾン
化ガスを散気装置から曝気することにより滅菌かつ脱臭
された飲料原水の溶存オゾンが滅菌空気で除去されるよ
うに構成されてなる飲料水精製装置。
(1) Consists of an ozone generator, an aeration device, an ozone reaction tower, a temperature detector, a heating device, and a temperature controller. A drinking water purification device configured to remove dissolved ozone from sterilized and deodorized drinking water by aeration from an air device.
JP23265185A 1985-10-17 1985-10-17 Apparatus for purifying drinking water Pending JPS6291289A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23265185A JPS6291289A (en) 1985-10-17 1985-10-17 Apparatus for purifying drinking water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23265185A JPS6291289A (en) 1985-10-17 1985-10-17 Apparatus for purifying drinking water

Publications (1)

Publication Number Publication Date
JPS6291289A true JPS6291289A (en) 1987-04-25

Family

ID=16942636

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23265185A Pending JPS6291289A (en) 1985-10-17 1985-10-17 Apparatus for purifying drinking water

Country Status (1)

Country Link
JP (1) JPS6291289A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0312291A (en) * 1989-06-12 1991-01-21 Nippon Neichiyua Roman:Kk Apparatus for improving quality of drinking water
JPH0722753B2 (en) * 1989-06-19 1995-03-15 ヴェデコ・ウンヴェルトテクノロジー・ヴァッサー―ボーデン―ルフト・ゲーエムベーハー Method and device for treating liquid contaminated with harmful substances

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0312291A (en) * 1989-06-12 1991-01-21 Nippon Neichiyua Roman:Kk Apparatus for improving quality of drinking water
JPH0722753B2 (en) * 1989-06-19 1995-03-15 ヴェデコ・ウンヴェルトテクノロジー・ヴァッサー―ボーデン―ルフト・ゲーエムベーハー Method and device for treating liquid contaminated with harmful substances

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