JPH0221997A - Water treatment by ozone and device therefor - Google Patents
Water treatment by ozone and device thereforInfo
- Publication number
- JPH0221997A JPH0221997A JP17203688A JP17203688A JPH0221997A JP H0221997 A JPH0221997 A JP H0221997A JP 17203688 A JP17203688 A JP 17203688A JP 17203688 A JP17203688 A JP 17203688A JP H0221997 A JPH0221997 A JP H0221997A
- Authority
- JP
- Japan
- Prior art keywords
- water
- ozone
- treated
- contact
- conduit
- 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.)
- Granted
Links
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 title claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 abstract description 21
- 239000000463 material Substances 0.000 abstract description 5
- 230000000717 retained effect Effects 0.000 abstract description 2
- 239000007792 gaseous phase Substances 0.000 abstract 1
- 239000006185 dispersion Substances 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000007788 liquid Substances 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 239000002270 dispersing agent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- PUZPDOWCWNUUKD-UHFFFAOYSA-M sodium fluoride Chemical compound [F-].[Na+] PUZPDOWCWNUUKD-UHFFFAOYSA-M 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はオゾンを用いて主として廃水の殺菌を効率J=
<行イイう水処理法およびその装置に関する6〔従来の
技術〕
オゾンは古くから殺菌の目的で水処理に利用されCさた
が、最近その強い酸化力による説色性、脱臭性等が認識
され、各種産業廃水処理に用いられている。[Detailed Description of the Invention] [Industrial Application Field] The present invention mainly uses ozone to sterilize wastewater with efficiency J=
<Regarding effective water treatment methods and equipment 6 [Prior art] Ozone has been used in water treatment for the purpose of sterilization since ancient times, but recently it has been recognized for its strong oxidizing power, color rendering properties, deodorizing properties, etc. It is used in various industrial wastewater treatment.
オゾンを水処理に用いる場合には、被処理水とオゾン含
有ガスとを効率」;り接触さけることが必要で、従来、
スプレー塔、充填塔、プレート塔、或いは亜流分散基、
向流分散基、加圧オゾン分散Jt)、機械撹拌式分散基
、■ジエクター式分散塔などの気泡分散基が実用化され
ている。When using ozone for water treatment, it is necessary to efficiently avoid contact between the water to be treated and the ozone-containing gas.
Spray tower, packed tower, plate tower, or subflow dispersion group,
Bubble dispersion groups such as countercurrent dispersion groups, pressurized ozone dispersion groups (Jt), mechanical stirring type dispersion groups, and diector type dispersion towers have been put into practical use.
しかし、スプレー塔、充填塔、プレート塔は、処理水中
の被処理物とオゾンどの反応速度が大ぎいことが必要と
され、特に充填塔はヂレンネリングが起り易い。また、
加圧オゾン分散剤は系を加圧状態に保持しな(−)れば
ならず、機械撹拌式分散基は強力な撹拌を必要どするた
め、設備費、運転]ス1〜が高くなり、ニジ」、フタ一
方式は、液循環に要する動力が大ぎいなどの欠点がある
。ざらに加圧オゾン分散基以外は、オゾンと接触した処
理水が、人気と接1−ろ水路または槽に導出され、溶存
したオゾンがただちに大気中に放散J−るので、オゾン
の有効利用に難点があった。However, spray towers, packed towers, and plate towers require a high rate of reaction between the to-be-treated material in the treated water and ozone, and packed towers in particular are susceptible to dylene ringing. Also,
Pressurized ozone dispersants require the system to be kept under pressure (-), and mechanically stirred dispersants require strong stirring, which increases equipment costs and operating costs. The single-lid type has drawbacks such as the large amount of power required to circulate the liquid. With the exception of roughly pressurized ozone dispersion groups, the treated water that has come into contact with ozone is led out to a filtration channel or tank, and the dissolved ozone is immediately dissipated into the atmosphere, making effective use of ozone possible. There was a problem.
本発明は上記の事情に鑑み、簡単な装置を用いて、被処
理液に吸収されたオゾンを有効利用出来るオゾンによる
水処理法おJ:びその装置を提供することを目的とする
。In view of the above-mentioned circumstances, an object of the present invention is to provide a water treatment method using ozone and an apparatus therefor, which can effectively utilize ozone absorbed in a liquid to be treated using a simple device.
上記の目的を達成するため、本発明の方法においては、
オゾン濃度が20ppm以上のオゾン含有ガスと被処理
水とを接触させた後、この被処理水を大気圧下で、気相
に接触させることなく滞留させる。In order to achieve the above object, in the method of the present invention,
After bringing the ozone-containing gas having an ozone concentration of 20 ppm or more into contact with the water to be treated, the water to be treated is allowed to stay under atmospheric pressure without contacting the gas phase.
また、装置においては、内底部にオゾン含有ガスのスパ
ーシレーを右し、上部に被処理水の供給管が接続された
接触槽と、下部が上記接触槽の下部に連通管ににっで接
続され、高さが上記接触槽のl−※ν1;J、り低い密
閉槽と、この密閉槽の最上部に基部が取(qりられて上
方に延在し、上記接触槽の上端より低い側部の位置に、
1)1出管が取1」(プられ上端部が人気に開放されて
いる導管とを右1−る。In addition, the equipment has a contact tank with an ozone-containing gas spur relay installed at the inner bottom, a contact tank connected to the supply pipe for water to be treated at the top, and a communication pipe connected to the bottom of the contact tank at the bottom. , a closed tank whose height is l-*ν1; in the position of
1) Take 1 outlet pipe and turn it to the right with the conduit whose top end is open.
〔作用)
本発明の方法d3よび装置は上記の構成となっているの
で被処理水に接触吸収されICオゾンは、放散されるこ
となく、有効に被処理物に作用する。[Operation] Since the method d3 and the apparatus of the present invention have the above-described configuration, the IC ozone that is contacted and absorbed by the water to be treated effectively acts on the object to be treated without being dissipated.
(実fル例)
本発明の方法に用いられるオゾン含有jJス中のオゾン
)門度は201]11m以上(゛あることが必要τ・あ
る3、濃度が201111m未満ではオゾンの溶解14
が少なく、滞留さlIC溶存オゾンを利用Jる効果が少
ない。(Actual example) The degree of ozone in the ozone-containing gas used in the method of the present invention is 201]11m or more (it is necessary to be 3), and if the concentration is less than 201111m, ozone dissolution14
There is little effect on utilizing the retained IC dissolved ozone.
上記201]r)m以上のオゾン含有ガスは、空気を原
料としたしので′は放電電力が過大どなり実用的ではな
く、酸素富化ガスを無声放電して得られる。The ozone-containing gas above 201]r)m uses air as a raw material, so the discharge power is too loud and is not practical, so it can be obtained by silently discharging oxygen-enriched gas.
酸素を富化するブj法は、いずれの方法を用いてもJ:
いが、通常モレキュラシーブス等の吸着剤を用い、加圧
吸盾、減J]−Jl+)着するブレラシル−スイング方
式が安価に酸素富化することが出来るので好ましい。No matter which method is used to enrich oxygen, J:
However, the Brellasil swing method, which uses an adsorbent such as molecular sieves, pressurized shielding, and deposits (reduced J]-Jl+), is preferable because oxygen enrichment can be achieved at low cost.
第1図は本発明の装置の一実施例を示すもので、図中符
号1は一ト端部から排ガスを放出するオゾンの接触槽で
ある。この接触槽1に近接して密閉槽2が設(′)られ
、これら接触槽1と密閉槽2の下部は連通管3によって
接続されている。上記密閉槽2の最−ト部には密閉槽2
内上部に気相が生じないように、上端部4aが人気に解
放され上記接触槽1の上端部より高い導管4の基部4b
が取イ」りられている。この導管4の上記接触槽1の上
端部より所定寸法低い側部の位置には排出管5が取付(
プられている。FIG. 1 shows an embodiment of the apparatus of the present invention, and reference numeral 1 in the figure is an ozone contact tank which releases exhaust gas from one end. A closed tank 2 is provided (') adjacent to the contact tank 1, and the lower portions of the contact tank 1 and the closed tank 2 are connected by a communicating pipe 3. At the top of the sealed tank 2, there is a sealed tank 2.
The base 4b of the conduit 4 is higher than the upper end of the contact tank 1, with the upper end 4a being open so as not to generate a gas phase in the inner upper part.
is being taken away. A discharge pipe 5 is attached (
is being pulled.
まIC1上記接触槽1の上部には、生物処理系などから
導出される被処理水6を供給する供給管6aが接続され
ている。また、接触槽1の底部にはオゾン含有ガスを分
散して吹込むスパーシレ−7が取付(プられている。ス
パージャ−7には、プレフシ11−スイング方式等にに
る酸素富化ガスを無声放電によってオーシン化したオゾ
ン含有ガス8を加圧供給ザる圧送管8aか接続されてい
る。A supply pipe 6a for supplying water to be treated 6 derived from a biological treatment system or the like is connected to the upper part of the contact tank 1 of the IC1. In addition, a sparger 7 is attached to the bottom of the contact tank 1 to disperse and blow in ozone-containing gas. A pressure feed pipe 8a for pressurized supply of ozone-containing gas 8 which has been converted into ozone by discharge is connected thereto.
上記装置を用いC水処理を行なうには、被処理水6を所
定の流mで導管6aより導入するとともにオゾン含有ガ
ス8を所定の流徂でスパージ1?7を介して分散供給J
−る。分散されたオーシン含有ガスは、被処理水と向流
接触して吸収されながら、被処理水中の被処理物と反応
して接触槽1の上端部より次の酸素を利用する工程に導
くか、オゾン分M設備を経て大気に放出される。To perform C water treatment using the above-mentioned apparatus, the water to be treated 6 is introduced from the conduit 6a at a predetermined flow rate m, and the ozone-containing gas 8 is distributed and supplied via the sparge 1 to 7 at a predetermined flow width.
-ru. The dispersed osin-containing gas is brought into countercurrent contact with the water to be treated and absorbed, while reacting with the substances to be treated in the water to be treated, leading to the next step of utilizing oxygen from the upper end of the contact tank 1, or The ozone is released into the atmosphere through the M equipment.
上記連通管3近くで、スパージ17−7より噴出するm
度の高いオゾンと接触した被処理水は、連通管3を通っ
て密閉槽2に移行し滞留する。この滞留中に、溶存する
オゾンは被処理物を引続いて酸化する。m spouted from the sparge 17-7 near the communication pipe 3.
The water to be treated that has come into contact with highly concentrated ozone passes through the communication pipe 3 and moves to the closed tank 2, where it stays there. During this residence, the dissolved ozone subsequently oxidizes the material to be treated.
また上記密閉槽2は接触槽1と連通しているため、接触
槽1に被処理水を導入すると、導管4を通って排水管5
より流出する。その際接触槽1内にはオゾン含有ガス気
泡が分散しているため、接触槽1の液面は排出管5の位
置より高くなるが、自然流下で動力を必要どしない。ま
た導管4は上端部4aが人気に開放されているが、細長
くぞの面積は小さいので、密閉槽2は実質的に密閉され
、これに対する大気の影響はない。したがって密閉槽2
内に滞留する被処理水中に溶存するオゾンは、有効に消
費される。In addition, since the sealed tank 2 is in communication with the contact tank 1, when water to be treated is introduced into the contact tank 1, it passes through the conduit 4 and into the drain pipe 5.
More leakage. At this time, since ozone-containing gas bubbles are dispersed in the contact tank 1, the liquid level in the contact tank 1 becomes higher than the position of the discharge pipe 5, but it is a natural flow and no power is required. Further, although the upper end 4a of the conduit 4 is open, the area of the elongated groove is small, so the closed tank 2 is substantially sealed, and there is no influence of the atmosphere on it. Therefore, closed tank 2
The ozone dissolved in the water to be treated that remains inside the tank is effectively consumed.
実施例1〜4、比較例1〜7
被処理水として下水の活性汚泥処理水を流量を変えて流
して接触槽における接触時間を変えた。Examples 1 to 4, Comparative Examples 1 to 7 Activated sludge treated water of sewage was flowed as the water to be treated at different flow rates to change the contact time in the contact tank.
オゾン含有ガスとしては、プレッシ+7−スイング方式
によって酸素m tt約9QVO1%の酸素富化ガスを
つくり、オゾン発生器を通しく種々なi度のオゾン含有
ガスとし、これを流量を変えて流し被処理水中に注入さ
れるオゾン量を調整し、被処理水の処理前、処理後の大
腸菌群の数を測定した。As the ozone-containing gas, an oxygen-enriched gas of approximately 9QVO1% is created using a pressure +7-swing method, and is passed through an ozone generator to produce ozone-containing gas of various i degrees. The amount of ozone injected into the treated water was adjusted, and the number of coliform bacteria in the treated water before and after treatment was measured.
また、装置は、内径100a++X高さ4000mmの
接触槽を用い、滞留させない場合には、導管4を連通管
3に数句り、また、密閉槽2の滞留時間を変化させる場
合には容量の異なる密閉槽を用いた。結果を第1表ない
し第3表に示す。In addition, the device uses a contact tank with an inner diameter of 100 a A closed tank was used. The results are shown in Tables 1 to 3.
第1表ないし第3表にり明らかなように、密閉槽に滞留
さけることにより、大腸菌群数が大幅に減少するが、オ
ゾン含有濃度が1511pmでは満足2i結果が111
られないことがわかる。As is clear from Tables 1 to 3, the number of coliform bacteria is significantly reduced by avoiding retention in a closed tank, but when the ozone content concentration is 1511 pm, the satisfactory 2i result is 111.
I know that I can't.
以上述へたJ、うに、本発明の方払は、装置が簡111
で、自然流下となっているので、装置費、運転費が安価
となり、′a度の高いオーシン含有ガスど接触した被処
理水が密閉槽に入って滞留し、被処理物と反応りるので
、溶存するオゾンの利用率が高く、処理機能が優れてい
る等多くの長所を有する。As mentioned above, the method of the present invention is easy to use.
Since it is a gravity flow, the equipment cost and operating cost are low, and the water to be treated that has come into contact with gas containing ossin with a high degree of a content enters the closed tank, stagnates, and reacts with the material to be treated. It has many advantages such as high utilization rate of dissolved ozone and excellent treatment function.
第1図は、本発明の装置の一実施例を示す図である。
1・・・接触槽、2・・・密閉槽、3・・・連通管、4
・・・導管、/Ia・・・上端部、4b・・・基部、5
・・・刊出管、6・・・被処理水、6a・・・供給管、
7・・・スパージャ8・・・オゾン含有ガス、8a・・
・圧送管。FIG. 1 is a diagram showing an embodiment of the apparatus of the present invention. 1... Contact tank, 2... Closed tank, 3... Communication pipe, 4
... Conduit, /Ia ... Upper end, 4b ... Base, 5
... Publication pipe, 6... Water to be treated, 6a... Supply pipe,
7...Sparger 8...Ozone-containing gas, 8a...
・Pressure pipe.
Claims (2)
被処理水とを接触させた後、この被処理水を大気圧下、
気相に接触させることなく滞留させることを特徴とする
オゾンによる水処理法。(1) After bringing the ozone-containing gas with an ozone concentration of 20 ppm or more into contact with the water to be treated, the water to be treated is heated under atmospheric pressure.
A water treatment method using ozone, which is characterized by allowing water to remain in the water without coming into contact with the gas phase.
上部に被処理水の供給管が接続された接触槽と、下部が
上記接触槽の下部に連通管によつて接続され、高さが上
記接触槽の上端より低い密閉槽と、この密閉槽の最上部
に基部が取付けられて上方に延在し、上記接触槽の上端
より低い側部の位置に、排出管が取付けられ、上端部が
大気に開放さている導管とを有することを特徴とするオ
ゾンによる水処理装置。(2) Has an ozone-containing gas sparger at the inner bottom;
A contact tank having an upper part connected to a supply pipe for water to be treated, a closed tank having a lower part connected to the lower part of the contact tank by a communicating pipe and having a height lower than the upper end of the contact tank, A conduit having a base attached to the top and extending upward, a discharge pipe attached to a side lower than the upper end of the contact tank, and an upper end open to the atmosphere. Water treatment equipment using ozone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17203688A JPH0221997A (en) | 1988-07-11 | 1988-07-11 | Water treatment by ozone and device therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17203688A JPH0221997A (en) | 1988-07-11 | 1988-07-11 | Water treatment by ozone and device therefor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0221997A true JPH0221997A (en) | 1990-01-24 |
JPH0558795B2 JPH0558795B2 (en) | 1993-08-27 |
Family
ID=15934339
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17203688A Granted JPH0221997A (en) | 1988-07-11 | 1988-07-11 | Water treatment by ozone and device therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0221997A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5546458A (en) * | 1994-05-18 | 1996-08-13 | Mitsubishi Denki Kabushiki Kaisha | Handsfree communication apparatus |
US7120261B1 (en) | 1999-11-19 | 2006-10-10 | Gentex Corporation | Vehicle accessory microphone |
US8163173B1 (en) * | 2008-07-16 | 2012-04-24 | Dellecave Steven F | Water treatment system |
US8224012B2 (en) | 1999-11-19 | 2012-07-17 | Gentex Corporation | Vehicle accessory microphone |
-
1988
- 1988-07-11 JP JP17203688A patent/JPH0221997A/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5546458A (en) * | 1994-05-18 | 1996-08-13 | Mitsubishi Denki Kabushiki Kaisha | Handsfree communication apparatus |
US7120261B1 (en) | 1999-11-19 | 2006-10-10 | Gentex Corporation | Vehicle accessory microphone |
US7443988B2 (en) | 1999-11-19 | 2008-10-28 | Gentex Corporation | Vehicle accessory microphone |
US8224012B2 (en) | 1999-11-19 | 2012-07-17 | Gentex Corporation | Vehicle accessory microphone |
US8163173B1 (en) * | 2008-07-16 | 2012-04-24 | Dellecave Steven F | Water treatment system |
Also Published As
Publication number | Publication date |
---|---|
JPH0558795B2 (en) | 1993-08-27 |
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