JP2006158986A - Water treatment method and device using ultraviolet light with ozone - Google Patents

Water treatment method and device using ultraviolet light with ozone Download PDF

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JP2006158986A
JP2006158986A JP2004349380A JP2004349380A JP2006158986A JP 2006158986 A JP2006158986 A JP 2006158986A JP 2004349380 A JP2004349380 A JP 2004349380A JP 2004349380 A JP2004349380 A JP 2004349380A JP 2006158986 A JP2006158986 A JP 2006158986A
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ozone
water
ultraviolet light
water treatment
space
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Hideki Yamamoto
秀樹 山本
Hitoshi Yonetani
仁志 米谷
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MANNA KK
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<P>PROBLEM TO BE SOLVED: To provide a water treatment device using ultraviolet light with ozone which enables the compactification of a system and can decompose hardly decomposable organic substances and the like while suppressing a water treatment cost. <P>SOLUTION: The water treatment device using ultraviolet light with ozone comprises an outer vessel 2 for water treatment, an inner vessel 3 disposed in the outer vessel 2, an ultraviolet lamp 6 disposed in the inner vessel 3, a suction pipe 7 of which one end communicates with and is connected to a space 4 for ozone generation between the inner vessel and the ultraviolet lamp, and of which the other end communicates with and is connected to a space 5 for passing water between the outer and inner vessels, and an air feeder 8 for supplying a gas in the suction pipe 7 toward the space 5 side for passing water from the space 4 side for ozone generation. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、例えば生活排水、産業排水等の水に含有される有機物質等を紫外光とオゾンを利用して分解処理する水処理方法及び水処理装置に関する。   The present invention relates to a water treatment method and a water treatment apparatus for decomposing organic substances contained in water such as domestic wastewater and industrial wastewater using ultraviolet light and ozone.

近年、化学製造業等における製造物の高度化等にともない、従来の生物処理や凝集沈殿処理では完全に除去できない難分解性の有機物質が増加してきており、工場排水等が十分に浄化されないまま環境中に排出されていることが多くなってきている。このような現状に対して排水の高度処理の要求が急速に高まってきている中、紫外光、オゾン、酸化力の強い物質(酸化チタン、過酸化水素等)を利用した水処理方法の技術開発が進められており、その中でも紫外線処理とオゾン処理を組み合わせた促進酸化処理法(Advanced Oxidation Process)が注目されている。   In recent years, with the advancement of products in the chemical manufacturing industry, etc., the number of persistent organic substances that cannot be completely removed by conventional biological treatment or coagulation sedimentation treatment has increased, and factory wastewater has not been sufficiently purified. It is increasingly being discharged into the environment. While the demand for advanced treatment of wastewater is rapidly increasing against this situation, technological development of water treatment methods using ultraviolet light, ozone, and substances with strong oxidizing power (titanium oxide, hydrogen peroxide, etc.) Among them, an advanced oxidation process combining ultraviolet treatment and ozone treatment (Advanced Oxidation Process) is attracting attention.

例えば、被処理水にオゾンを溶解せしめた後、この被処理水に紫外線を照射することによってオゾンよりも酸化力の強いラジカル種(ヒドロキシラジカル等)を生成させて難分解性有機物質等を分解処理する方法が種々提案されている(特許文献1〜4参照)。これらいずれの方法でも、効果の差はあるものの、被処理水中の難分解性有機物質の分解処理を行うことができる。
特開2004−275969号公報 特開2003−266088号公報 特開2002−153891号公報 特開2000−51875号公報
For example, after ozone is dissolved in the water to be treated, the water to be treated is irradiated with ultraviolet rays to generate radical species (hydroxy radicals, etc.) that have stronger oxidizing power than ozone, thereby decomposing refractory organic substances. Various processing methods have been proposed (see Patent Documents 1 to 4). In any of these methods, although there is a difference in effect, it is possible to perform the decomposition treatment of the hardly decomposable organic substance in the water to be treated.
JP 2004-275969 A JP 2003-266088 A JP 2002-153891 A JP 2000-51875 A

しかしながら、上記特許文献1〜4に記載の水処理装置では、いずれもオゾンをオゾン発生装置(オゾナイザー)を用いて発生させているが、このオゾン発生装置は、装置として大型のものとなるし、高価であることから、上記特許文献1〜4の水処理装置では、コンパクト化を図ることは到底困難であるし、設備コストも高くなって水処理のコストが高くなるという問題があった。   However, in each of the water treatment devices described in Patent Documents 1 to 4, ozone is generated using an ozone generator (ozonizer), but this ozone generator is a large-sized device. Since it is expensive, the water treatment devices of Patent Documents 1 to 4 have difficulty in achieving downsizing, and there is a problem that the cost of water treatment increases due to high equipment costs.

この発明は、かかる技術的背景に鑑みてなされたものであって、設備のコンパクト化を図ることができると共に水処理コストも抑制しつつ、難分解性有機物質等を分解処理することのできる、紫外光とオゾンを併用した水処理方法及び水処理装置を提供する。   This invention has been made in view of such a technical background, and it is possible to decompose a hardly decomposable organic substance or the like while reducing the cost of water treatment while reducing the size of equipment. Provided are a water treatment method and a water treatment apparatus using both ultraviolet light and ozone.

前記目的を達成するために、本発明は以下の手段を提供する。   In order to achieve the above object, the present invention provides the following means.

[1]オゾンを添加した被処理水に紫外線ランプからの紫外光を照射することによって、被処理水に含有される有機物質等を分解処理する水処理方法において、
前記添加オゾンとして、前記紫外線ランプの周囲に存在する酸素に対して該ランプからの紫外光が照射されることによって生成したオゾンを用いることを特徴とする紫外光とオゾンを併用した水処理方法。
[1] In a water treatment method for decomposing an organic substance or the like contained in water to be treated by irradiating the water to be treated with ozone with ultraviolet light from an ultraviolet lamp,
A water treatment method using ultraviolet light and ozone in combination, wherein as the added ozone, ozone generated by irradiating oxygen present around the ultraviolet lamp with ultraviolet light from the lamp is used.

[2]水処理用外槽と、前記外槽の内部に配置された内槽と、前記内槽内に配置された紫外線ランプと、一端が前記内槽と前記紫外線ランプの間のオゾン生成用空間に連通接続され、他端が前記外槽と内槽の間の通水用空間に連通接続された吸気管と、前記吸気管内の気体を前記オゾン生成用空間側から通水用空間側に向けて送気する送気装置とを備えることを特徴とする紫外光とオゾンを併用した水処理装置。   [2] A water treatment outer tub, an inner tub disposed inside the outer tub, an ultraviolet lamp disposed in the inner tub, and one end for generating ozone between the inner tub and the ultraviolet lamp An intake pipe connected to the space and having the other end connected to a water passage space between the outer tank and the inner tank, and a gas in the intake pipe from the ozone generation space side to the water passage side A water treatment device using ultraviolet light and ozone in combination, comprising an air supply device for supplying air.

[3]水処理用外槽と、前記外槽の内部に配置された内槽と、前記内槽内に配置された紫外線ランプと、一端が前記内槽と前記紫外線ランプの間のオゾン生成用空間に連通接続され、他端が前記外槽と内槽の間の通水用空間に連通接続された吸気管と、前記吸気管の途中位置に取り付けられたアスピレーターとを備えることを特徴とする紫外光とオゾンを併用した水処理装置。   [3] An outer tub for water treatment, an inner tub disposed in the outer tub, an ultraviolet lamp disposed in the inner tub, and one end for ozone generation between the inner tub and the ultraviolet lamp An intake pipe connected to the space and having the other end connected to a water passing space between the outer tub and the inner tub, and an aspirator attached to an intermediate position of the intake pipe. Water treatment equipment that uses both ultraviolet light and ozone.

[4]前記吸気管におけるアスピレーターから通水用空間までの位置の少なくとも一部が螺旋状に形成されている前項3に記載の紫外光とオゾンを併用した水処理装置。   [4] The water treatment apparatus using both ultraviolet light and ozone according to item 3 above, wherein at least a part of the position from the aspirator to the water passage space in the intake pipe is formed in a spiral shape.

[5]前記外槽が、内方側に紫外光を反射する反射板で構成されている前項2〜4のいずれか1項に記載の紫外光とオゾンを併用した水処理装置。   [5] The water treatment apparatus using the ultraviolet light and ozone according to any one of the above items 2 to 4, wherein the outer tub is configured by a reflector that reflects ultraviolet light inward.

[6]前記外槽の外側または内側に、内方側に紫外光を反射する反射板が配置されている前項2〜4のいずれか1項に記載の紫外光とオゾンを併用した水処理装置。   [6] A water treatment apparatus using both ultraviolet light and ozone according to any one of items 2 to 4 above, wherein a reflector that reflects ultraviolet light is arranged on the inner side outside or inside the outer tank. .

[1]の発明では、紫外光とオゾンを併用して、被処理水に含有される有機物質等を分解処理するものであるから、易分解性有機物質のみならず、難分解性有機物質等も分解処理することができる。更に、被処理水に添加するオゾンとして、紫外光を発生させるのに用いる紫外線ランプの周囲に存在する酸素に対して該ランプからの紫外光が照射されることによって生成したオゾンを用いており、オゾン発生のために別途オゾン発生装置等の専用設備を設けなくて済むので、装置のコンパクト化を図ることができるし、水処理コストも抑制することができる。   In the invention of [1], since ultraviolet light and ozone are used in combination to decompose organic substances contained in the water to be treated, not only easily decomposable organic substances but also hardly decomposable organic substances etc. Can also be decomposed. Furthermore, as ozone added to the water to be treated, ozone generated by irradiating ultraviolet light from the lamp to oxygen present around the ultraviolet lamp used to generate ultraviolet light is used. Since it is not necessary to provide a dedicated facility such as an ozone generator for generating ozone, the apparatus can be made compact and water treatment costs can be reduced.

[2]の発明では、紫外線ランプの紫外光が、外槽と内槽の間の通水用空間を通過する被処理水に照射されるから、被処理水中の有機物質等が分解処理される。また、内槽と紫外線ランプの間のオゾン生成用空間の酸素にランプからの紫外光が照射されることによって生成したオゾンは、送気装置によって吸気管を介して外槽と内槽の間の通水用空間に送流される。この通水用空間では、オゾンの作用によって被処理水中の有機物質等が分解処理されると共に、このオゾンの一部は、ランプからの紫外光照射により酸化力の強いラジカル種(ヒドロキシラジカル等)になり該ラジカル種によって被処理水中の難分解性有機物質も分解処理される。この水処理装置では、オゾン発生のために別途オゾン発生装置等の専用設備を設けなくて済むので、装置のコンパクト化を図ることができると共に、水処理コストも抑制することができる。   In the invention of [2], since the ultraviolet light from the ultraviolet lamp is irradiated to the water to be treated that passes through the water passage space between the outer tank and the inner tank, the organic substances and the like in the water to be treated are decomposed. . Moreover, the ozone generated by irradiating the ultraviolet light from the lamp to the oxygen in the ozone generating space between the inner tank and the ultraviolet lamp is generated between the outer tank and the inner tank by the air supply device via the intake pipe. It is sent to the space for water flow. In this water flow space, organic substances, etc. in the water to be treated are decomposed by the action of ozone, and a part of this ozone is a radical species (hydroxy radical, etc.) that has strong oxidizing power when irradiated with ultraviolet light from the lamp. Thus, the radical species also decomposes the hardly decomposable organic substance in the water to be treated. In this water treatment apparatus, it is not necessary to provide a dedicated facility such as an ozone generation apparatus separately for generating ozone, so that the apparatus can be made compact and water treatment costs can be reduced.

[3]の発明では、紫外線ランプの紫外光が、外槽と内槽の間の通水用空間を通過する被処理水に照射されるから、被処理水中の有機物質等が分解処理される。また、内槽と紫外線ランプの間のオゾン生成用空間の酸素に対してランプからの紫外光が照射されることによって生成したオゾンは、被処理水がアスピレーターを通過することによって生じた減圧による吸引作用により吸気管を介して外槽と内槽の間の通水用空間に送流される。この通水用空間では、オゾンの作用によって被処理水中の有機物質等が分解処理されると共に、このオゾンの一部は、ランプからの紫外光照射により酸化力の強いラジカル種(ヒドロキシラジカル等)になり該ラジカル種によって被処理水中の難分解性有機物質も分解処理される。この水処理装置では、オゾン発生のために別途オゾン発生装置等の専用設備を設けなくて済むので、装置のコンパクト化を図ることができると共に、水処理コストも抑制することができる。また、オゾン生成用空間で生成したオゾンの通水用空間への送気は、簡易なアスピレーターを利用して行うことができ、別途専用の設備を設けなくて済むから、装置全体をよりコンパクト化できる利点がある。   In the invention of [3], since the ultraviolet light from the ultraviolet lamp is irradiated to the water to be treated that passes through the water passage space between the outer tank and the inner tank, the organic substances in the water to be treated are decomposed. . In addition, the ozone generated by irradiating the ultraviolet light from the lamp to the oxygen in the ozone generation space between the inner tank and the ultraviolet lamp is sucked by the reduced pressure generated when the water to be treated passes through the aspirator. Due to the action, the air is sent to the water passing space between the outer tank and the inner tank via the intake pipe. In this water flow space, organic substances, etc. in the water to be treated are decomposed by the action of ozone, and a part of this ozone is a radical species (hydroxy radical, etc.) that has strong oxidizing power when irradiated with ultraviolet light from the lamp. Thus, the radical species also decomposes the hardly decomposable organic substance in the water to be treated. In this water treatment apparatus, it is not necessary to provide a dedicated facility such as an ozone generation apparatus separately for generating ozone, so that the apparatus can be made compact and water treatment costs can be reduced. In addition, the ozone generated in the ozone generation space can be supplied to the water flow space by using a simple aspirator, and there is no need for a separate dedicated facility, making the entire device more compact. There are advantages you can do.

[4]の発明では、前記吸気管におけるアスピレーターから通水用空間までの位置の少なくとも一部が螺旋状に形成されているから、この螺旋状部を被処理水及びオゾンが通過する際に被処理水とオゾンが十分に混合されるものとなり、オゾンが被処理水中に十分に溶解するので、分解作用をより向上させることができる利点がある。   In the invention of [4], since at least a part of the position from the aspirator to the water flow space in the intake pipe is formed in a spiral shape, when the treated water and ozone pass through the spiral portion, The treated water and ozone are sufficiently mixed, and the ozone is sufficiently dissolved in the treated water, so that there is an advantage that the decomposition action can be further improved.

[5]の発明では、外槽が、内方側に紫外光を反射する反射板で構成されているから、外槽に到達した紫外光を外に逃がすことなく内側に戻して再利用に供することができ、これにより有機物質等の分解効率を一層向上させることができる。   In the invention of [5], since the outer tub is composed of a reflecting plate that reflects ultraviolet light toward the inner side, the ultraviolet light that has reached the outer tub is returned to the inner side without being released to the outside for reuse. This can further improve the decomposition efficiency of organic substances and the like.

[6]の発明でも、[5]の発明と同様に、外槽の方に到達した紫外光を外に逃がすことなく内側に戻して再利用に供することができ、これにより有機物質等の分解効率を一層向上させることができる。   In the invention of [6], similarly to the invention of [5], the ultraviolet light that has reached the outer tub can be returned to the inner side without being released to be reused. Efficiency can be further improved.

この発明に係る紫外光とオゾンを併用した水処理装置(1)の一実施形態を図1〜3に示す。これらの図において、(2)は水処理用外槽、(3)は内槽、(6)は紫外線ランプ、(7)は吸気管、(8)はアスピレーターである。   One Embodiment of the water treatment apparatus (1) which used together the ultraviolet light and ozone which concern on this invention is shown to FIGS. In these drawings, (2) is an outer tank for water treatment, (3) is an inner tank, (6) is an ultraviolet lamp, (7) is an intake pipe, and (8) is an aspirator.

前記水処理用外槽(2)は石英ガラス製の透明な筒状体で形成され、この外槽(2)の内部に内槽(3)が配置されており、該内槽(3)も石英ガラス製の透明な筒状体で形成されている。前記外槽(2)の内径は、前記内槽(3)の外径よりも大きく設計され、これにより前記外槽(2)と前記内槽(3)の間に通水用空間(5)が確保されている(図2、3参照)。前記外槽(2)と前記内槽(3)の上端には上蓋部(13)が接合される一方、前記外槽(2)と前記内槽(3)の下端には底蓋部(14)が接合されている。前記上蓋部(13)の送出口(22)に、処理後の水を送出するための処理水送出管(11)が接続固定されている。なお、本実施形態では、前記外槽(2)の外周面に、内方側に紫外光を反射する筒状の鏡面紫外光反射板(図示しない)が積層一体化されている。   The water treatment outer tub (2) is formed of a transparent cylindrical body made of quartz glass, and an inner tub (3) is disposed inside the outer tub (2). It is formed of a transparent cylindrical body made of quartz glass. The inner diameter of the outer tub (2) is designed to be larger than the outer diameter of the inner tub (3), whereby a water passage space (5) is provided between the outer tub (2) and the inner tub (3). Is secured (see FIGS. 2 and 3). An upper lid (13) is joined to the upper ends of the outer tub (2) and the inner tub (3), while a bottom lid (14) is joined to the lower ends of the outer tub (2) and the inner tub (3). ) Is joined. A treated water delivery pipe (11) for delivering treated water is connected and fixed to the delivery port (22) of the upper lid (13). In the present embodiment, a cylindrical specular ultraviolet light reflector (not shown) that reflects ultraviolet light inward is laminated and integrated on the outer peripheral surface of the outer tub (2).

前記内槽(3)の内部には紫外線ランプ(6)が配置されており、この紫外線ランプ(6)と前記内槽(3)との間にオゾン生成用空間(4)が形成されている(図2、3参照)。本実施形態では、前記紫外線ランプ(6)として低圧水銀ランプを用いている。なお、図1において、(10)は紫外線ランプの電源部である。   An ultraviolet lamp (6) is disposed inside the inner tank (3), and an ozone generation space (4) is formed between the ultraviolet lamp (6) and the inner tank (3). (See FIGS. 2 and 3). In this embodiment, a low-pressure mercury lamp is used as the ultraviolet lamp (6). In FIG. 1, reference numeral (10) denotes a power supply unit of the ultraviolet lamp.

前記オゾン生成用空間(4)には吸気管(7)の一端が配置されている。本実施形態では、吸気管(7)の一端が前記オゾン生成用空間(4)の高さの2等分位置より下の位置になるように配置されている(図1、3参照)。前記吸気管(7)の他端は、前記底蓋部(14)の導入口(21)に接続固定されることによって前記通水用空間(5)に連通接続されている。   One end of an intake pipe (7) is disposed in the ozone generation space (4). In the present embodiment, the one end of the intake pipe (7) is disposed so as to be lower than the bisected position of the height of the ozone generation space (4) (see FIGS. 1 and 3). The other end of the intake pipe (7) is connected and connected to the water flow space (5) by being connected and fixed to the introduction port (21) of the bottom cover part (14).

また、前記吸気管(7)の途中位置にアスピレーター(水流ポンプ)(8)が取り付けられている。そして、前記吸気管(7)におけるアスピレーター(8)から通水用空間(5)までの位置の大部分が螺旋状に捲回されて吸気用螺旋管部(7X)が構成されている。図1に示すように、前記アスピレーター(8)の三方接続口のうちの1つ(上端接続口)には前記吸気管(7)が接続され、左端接続口には吸気用螺旋管部(7X)の一端が接続され、残る右端接続口に送水管(12)が接続されている。この送水管(12)には送水機(9)が取り付けられており、この送水機(9)の駆動によって被処理水が、送水管(12)、アスピレーター(8)、吸気用螺旋管部(7X)、底蓋部の導入口(21)を順に通過して前記通水用空間(5)内に送流される。そして、被処理水がアスピレーター(8)内を通過した際にアスピレーター(8)内に減圧が生じ、この減圧によって前記吸気管(7)から管(7)内の気体が吸気用螺旋管部(7X)に取り込まれる、即ち前記オゾン生成用空間(4)で発生したオゾンが前記吸気管(7)経由で前記吸気用螺旋管部(7X)に取り込まれて、オゾンが前記通水用空間(5)内に送流されるものとなる。なお、本実施形態では、前記送水機(9)としてポンプを用いている。また、図3において、(15)は酸素導入用開口部であり、本実施形態では、大気(空気)がこの酸素導入用開口部(15)を介してオゾン生成用空間(4)内に取り込まれる。   Further, an aspirator (water flow pump) (8) is attached to a midway position of the intake pipe (7). And most of the position from the aspirator (8) to the water flow space (5) in the intake pipe (7) is spirally wound to constitute the intake spiral pipe part (7X). As shown in FIG. 1, the intake pipe (7) is connected to one of the three-way connection ports (upper connection port) of the aspirator (8), and the intake spiral tube (7X) is connected to the left end connection port. ) Is connected, and the water pipe (12) is connected to the remaining right end connection port. A water feeder (9) is attached to the water pipe (12), and the water to be treated is driven by the water feeder (9) into the water pipe (12), the aspirator (8), and the spiral pipe for intake air ( 7X), and sequentially passes through the inlet (21) of the bottom cover portion and is sent into the water passage space (5). Then, when the water to be treated passes through the aspirator (8), a reduced pressure is generated in the aspirator (8), and the gas in the pipe (7) from the intake pipe (7) is reduced by this pressure reduction. 7X), that is, ozone generated in the ozone generation space (4) is taken into the intake spiral tube portion (7X) via the intake pipe (7), and ozone is supplied to the water flow space (7X). 5) It will be sent in. In this embodiment, a pump is used as the water feeder (9). In FIG. 3, reference numeral (15) denotes an oxygen introduction opening. In this embodiment, the atmosphere (air) is taken into the ozone generation space (4) through the oxygen introduction opening (15). It is.

しかして、前記電源部(10)のスイッチを入れて紫外線ランプ(6)を点灯すると共に前記送水機(9)を駆動させて水処理装置(1)を運転状態にすると、被処理水が送水管(12)、アスピレーター(8)、吸気用螺旋管部(7X)、底蓋部(14)の導入口(21)を順に通過して前記通水用空間(5)内に送流される。また、被処理水がアスピレーター(8)内を通過した際に生じたアスピレーター(8)内の減圧によって、即ち吸引作用によって、前記オゾン生成用空間(4)で発生したオゾンが吸気管(7)を経由してアスピレーター(8)内に取り込まれ、ここでオゾンが前記被処理水に混合されつつ吸気用螺旋管部(7X)、底蓋部(14)の導入口(21)を順に通過して前記通水用空間(5)内に送流される。この時、被処理水及びオゾンが吸気用螺旋管部(7X)を通過することによって被処理水とオゾンが十分に混合されるから、オゾンは被処理水中に十分に溶解する。こうして前記通水用空間(5)内にオゾンが十分に溶解した被処理水が送流される。   Then, when the power supply unit (10) is turned on to turn on the ultraviolet lamp (6) and the water feeder (9) is driven to bring the water treatment device (1) into operation, the water to be treated is fed. The water pipe (12), the aspirator (8), the intake spiral pipe part (7X), and the inlet (21) of the bottom cover part (14) are passed through in this order to be sent into the water flow space (5). Further, the ozone generated in the ozone generating space (4) is reduced by the pressure reduction in the aspirator (8) generated when the water to be treated passes through the aspirator (8), that is, by the suction action, and the intake pipe (7). And is then taken into the aspirator (8) through which the ozone passes through the inlet spiral tube (7X) and the inlet (21) of the bottom lid (14) in order while being mixed with the water to be treated. And is sent into the water flow space (5). At this time, since the water to be treated and ozone are sufficiently mixed by passing through the intake spiral pipe portion (7X), the ozone is sufficiently dissolved in the water to be treated. In this way, the water to be treated in which ozone is sufficiently dissolved is sent into the water flow space (5).

前記通水用空間(5)内では、オゾンが十分に溶解した被処理水に対して紫外線ランプ(6)からの紫外光が照射されるので、被処理水中の有機物質等が分解処理される。また、オゾンの作用によって被処理水中の有機物質等が分解処理されると共に、このオゾンの一部は、紫外線ランプ(6)からの紫外光照射により酸化力の強いラジカル種(ヒドロキシラジカル等)になり該ラジカル種によって被処理水中の難分解性有機物質も分解処理される。このようにして分解処理された処理水は、上昇移動して前記上蓋部(13)の送出口(22)を介して処理水送出管(11)に送出される。送出された処理水は、紫外光の作用、オゾンの酸化作用及びオゾンへの紫外光照射により生成したラジカル種による酸化作用等によって易分解性有機物質は勿論のこと難分解性有機物質も十分に分解処理されたものとなっている。   In the water flow space (5), since the ultraviolet light from the ultraviolet lamp (6) is irradiated to the water to be treated in which ozone is sufficiently dissolved, the organic substances in the water to be treated are decomposed. . In addition, organic substances in the water to be treated are decomposed by the action of ozone, and a part of the ozone is converted into radical species (hydroxy radicals, etc.) having strong oxidizing power by ultraviolet light irradiation from the ultraviolet lamp (6). The hardly decomposable organic substance in the water to be treated is also decomposed by the radical species. The treated water thus decomposed moves upward and is sent to the treated water delivery pipe (11) through the delivery port (22) of the upper lid part (13). The treated water sent out is not only easily decomposable organic substances, but also sufficiently degradable organic substances due to the action of ultraviolet light, the oxidizing action of ozone, and the oxidizing action of radical species generated by irradiation of ozone with ultraviolet light. It has been decomposed.

前記水処理装置(1)によれば、オゾン発生のために別途オゾン発生装置等の専用設備を設けなくて済むので、装置(1)のコンパクト化を図ることができると共に、水処理コストも低減することができる。   According to the water treatment device (1), since it is not necessary to provide a dedicated facility such as an ozone generation device separately for generating ozone, the device (1) can be made compact and the water treatment cost can be reduced. can do.

なお、前記実施形態では、前記外槽(2)の外周面に、内方側に紫外光を反射する反射板を積層一体化した構成を採用しているが、このような紫外光反射板を設けない構成を採用しても良い。また、紫外光反射板を設ける構成を採用する場合に、例えば、前記外槽(2)の内周面に、内方側に紫外光を反射する反射板を積層一体化した構成を採用しても良いし、或いは前記外槽(2)そのものを内方側に紫外光を反射する反射板で構成しても良い。   In addition, in the said embodiment, the structure which laminated | stacked and integrated the reflecting plate which reflects an ultraviolet light on the inner side is employ | adopted on the outer peripheral surface of the said outer tank (2), but such an ultraviolet light reflecting plate is used. You may employ | adopt the structure which does not provide. Further, when adopting a configuration in which an ultraviolet light reflection plate is provided, for example, a configuration in which a reflection plate that reflects ultraviolet light on the inner side is laminated and integrated on the inner peripheral surface of the outer tub (2) is adopted. Alternatively, the outer tub (2) itself may be composed of a reflector that reflects ultraviolet light inward.

また、前記実施形態では、吸気管(7)におけるアスピレーター(8)から通水用空間(5)までの位置の一部が螺旋状に形成された吸気用螺旋管部(7X)が設けられているが、特にこのような螺旋管部を設けない構成を採用しても良い。ただ、オゾンを被処理水中に十分に溶解せしめて分解作用をより向上させる観点から、吸気管(7)におけるアスピレーター(8)から通水用空間(5)までの位置の少なくとも一部が螺旋状に形成された構成を採用するのが好ましい。   Moreover, in the said embodiment, the spiral pipe part (7X) for intake in which a part of position from the aspirator (8) in the intake pipe (7) to the water flow space (5) was formed in a spiral shape is provided. However, a configuration in which such a spiral tube portion is not particularly provided may be employed. However, at least a part of the position from the aspirator (8) to the water flow space (5) in the intake pipe (7) is spiral from the viewpoint of further dissolving ozone in the water to be treated and further improving the decomposition action. It is preferable to adopt the configuration formed in the above.

また、前記実施形態では、内槽(3)は、石英ガラスで構成されているが、特にこのような素材に限定されるものではなく、紫外光を透過できる素材(紫外光透過性素材)であればどのようなものでも良い。また、内槽(3)は、その一部が紫外光を内方に反射する反射材で構成されていても良く、この場合にはオゾン生成用空間(4)におけるオゾン生成効率をより向上させることができる利点がある。或いはまた、内槽(3)は、例えば紫外光を50%透過し、残りの50%を内方側に反射する材料で構成されていても良い。   Moreover, in the said embodiment, although the inner tank (3) is comprised with quartz glass, it is not specifically limited to such a material, It is a material (ultraviolet light transmissive material) which can permeate | transmit an ultraviolet light. Anything is acceptable. Moreover, the inner tank (3) may be made of a reflective material that partially reflects ultraviolet light inward. In this case, the ozone generation efficiency in the ozone generation space (4) is further improved. There are advantages that can be made. Alternatively, the inner tank (3) may be made of a material that transmits, for example, 50% of ultraviolet light and reflects the remaining 50% to the inner side.

また、前記実施形態では、吸気管(7)にアスピレーター(8)を取り付けることによって、吸気用螺旋管部(7X)において被処理水とオゾンを十分に混合せしめて、この吸気用螺旋管部(7X)から被処理水とオゾンの両方(即ちオゾンが十分に溶解した被処理水)を通水用空間(5)に送流するようにしているが、特にこのような構成(被処理水とオゾンの両方を同一の管から通水用空間に供給する構成)に限定されるものではなく、例えば図6に示すように、一端がオゾン生成用空間(4)に連通接続された吸気管(7)の他端を底蓋部(14)の吸気口(23)を介して通水用空間(5)に連通接続する一方、送水機(9)が取り付けられた送水管(12)を底蓋部(14)の吸水口(24)を介して通水用空間(5)に連通接続し、前記吸気管(7)に送気装置(8)を取り付けた構成を採用しても良い。この図6の構成では、被処理水は、底蓋部(14)の吸水口(24)から通水用空間(5)内に送水される一方、オゾンは、底蓋部(14)の吸気口(23)から通水用空間(5)内に送気される。   Further, in the embodiment, by attaching the aspirator (8) to the intake pipe (7), the water to be treated and ozone are sufficiently mixed in the intake spiral pipe section (7X), and this intake spiral pipe section ( 7X), both treated water and ozone (that is, treated water in which ozone is sufficiently dissolved) are sent to the water space (5). It is not limited to the configuration in which both ozone are supplied from the same pipe to the water passage space. For example, as shown in FIG. 6, an intake pipe having one end connected to the ozone generation space (4) ( 7) The other end of 7) is connected to the water flow space (5) through the air inlet (23) of the bottom cover (14), while the water pipe (12) to which the water feeder (9) is attached is connected to the bottom. Connected to the water flow space (5) through the water inlet (24) of the lid (14) , The intake pipe (7) to the insufflation device (8) may be adopted fitted with. In the configuration of FIG. 6, the water to be treated is fed from the water inlet (24) of the bottom lid (14) into the water flow space (5), while ozone is sucked into the bottom lid (14). Air is fed into the water passage space (5) from the mouth (23).

また、前記実施形態では、前記オゾン生成用空間(4)で生成したオゾンが吸気管(7)内に吸気されるのに伴い、上蓋部(13)の酸素導入用開口部(15)から大気(空気)が前記オゾン生成用空間(4)内に取り込まれるものとなされているが、例えば図4に示すように、酸素ボンベ等の酸素供給器(31)から延ばされた酸素供給管(32)を前記オゾン生成用空間(4)内に配置せしめた構成を採用することによって、前記オゾン生成用空間(4)で生成したオゾンが吸気管(7)内に吸気されるのに伴い、前記オゾン生成用空間(4)内に新たに酸素が導入(供給)されるようにしても良い。   Further, in the embodiment, as the ozone generated in the ozone generation space (4) is sucked into the intake pipe (7), air is introduced into the atmosphere from the oxygen introduction opening (15) of the upper lid (13). (Air) is taken into the ozone generation space (4). For example, as shown in FIG. 4, an oxygen supply pipe (31) extended from an oxygen supply (31) such as an oxygen cylinder ( By adopting a configuration in which 32) is disposed in the ozone generation space (4), the ozone generated in the ozone generation space (4) is taken into the intake pipe (7). Oxygen may be newly introduced (supplied) into the ozone generation space (4).

また、本発明の水処理装置(1)の複数個を直列に連結した構成を採用することもできる。例えば、図5に示すように、一方の水処理装置(1A)の処理水送出管(11)を他方の水処理装置(1B)のアスピレーター(8)に接続した構成を採用することもできる。   Moreover, the structure which connected the some of the water treatment apparatus (1) of this invention in series is also employable. For example, as shown in FIG. 5, the structure which connected the treated water delivery pipe | tube (11) of one water treatment apparatus (1A) to the aspirator (8) of the other water treatment apparatus (1B) is also employable.

この発明に係る、紫外光とオゾンを併用した水処理方法及び水処理装置は、特に限定されるものではないが、例えば難分解性有機物質を含む排水の分解処理、着色排水の脱色処理、BOD(生物化学的酸素要求量)削減、COD(化学的酸素要求量)削減などに用いられ、またこれら以外の多様な分野への応用が可能である。前記難分解性有機物質としては、例えばフェノール、p−クレゾール、p−クロロフェノール等を例示できる。   The water treatment method and water treatment apparatus using ultraviolet light and ozone according to the present invention are not particularly limited. For example, the waste water containing a hard-to-decompose organic substance is decomposed, the colored waste water is decolorized, and BOD is used. It is used for (biochemical oxygen demand) reduction, COD (chemical oxygen demand) reduction and the like, and can be applied to various other fields. Examples of the hardly decomposable organic substance include phenol, p-cresol, and p-chlorophenol.

次に、この発明の具体的実施例について説明する。   Next, specific examples of the present invention will be described.

<実施例1>
図1〜3に示す構成の水処理装置(1)を用いて、フェノール、p−クレゾール、p−クロロフェノールを微量含有した被処理水の分解処理を行った。即ち、フェノール153mg/dm3、p−クレゾール156mg/dm3、p−クロロフェノール112mg/dm3を含有した被処理水を1L容量のタンク内に入れ、このタンクの内部空間の底部付近に送水管(12)の先端を配置する一方、前記タンクの内部空間の上部付近に処理水送出管(11)の先端を配置せしめ、この状態で電源部(10)のスイッチを入れて紫外線ランプ(6)を点灯すると共に送水機(9)を駆動させて水処理装置(1)を150分間運転状態にすることによって、前記被処理水を一定流量でタンクと水処理装置(1)内を順に循環させた。
<Example 1>
The water treatment apparatus (1) having the structure shown in FIGS. 1 to 3 was used to decompose the water to be treated containing trace amounts of phenol, p-cresol, and p-chlorophenol. That is, water to be treated containing phenol 153 mg / dm 3 , p-cresol 156 mg / dm 3 , and p-chlorophenol 112 mg / dm 3 is placed in a 1 L tank, and a water pipe is placed near the bottom of the internal space of the tank. While the tip of (12) is placed, the tip of the treated water delivery pipe (11) is placed near the upper part of the internal space of the tank, and in this state, the power supply unit (10) is turned on and the ultraviolet lamp (6) Is turned on and the water supply device (9) is driven to bring the water treatment device (1) into an operation state for 150 minutes, whereby the water to be treated is circulated through the tank and the water treatment device (1) in order at a constant flow rate. It was.

なお、外槽(2)の外周面に積層する紫外光反射板としては、アルミニウム箔を用いた。また、外槽(2)と内槽(3)の間の通水用空間(5)の容積は230cm3であり、通水用空間(5)へのオゾン供給量は8.4mg/hであった。また紫外線ランプ(6)として用いた低圧水銀ランプの主波長は185nmと254nmであった。こうして水処理装置(1)を150分間運転した後にタンク内の水を採取し、キャピラリーガスクロマトグラフ(GC−17A、島津製作所製)を用いて定量分析を行い、水処理前後の物質収支から、フェノール、p−クレゾール、p−クロロフェノールそれぞれの分解率を算出した。 In addition, an aluminum foil was used as the ultraviolet light reflection plate laminated on the outer peripheral surface of the outer tub (2). The volume of the water passage space (5) between the outer tank (2) and the inner tank (3) is 230 cm 3 , and the ozone supply amount to the water passage space (5) is 8.4 mg / h. there were. The main wavelengths of the low-pressure mercury lamp used as the ultraviolet lamp (6) were 185 nm and 254 nm. After operating the water treatment device (1) for 150 minutes, water in the tank is collected and quantitative analysis is performed using a capillary gas chromatograph (GC-17A, manufactured by Shimadzu Corporation). From the material balance before and after the water treatment, phenol is obtained. , P-cresol and p-chlorophenol were calculated.

<実施例2>
水処理装置(1)として、図1〜3に示す構成の水処理装置であって紫外光反射板を省略した構成(紫外光反射板がない構成)のものを用いた以外は、実施例1と同様にして被処理水の分解処理を行った。
<Example 2>
Example 1 except that the water treatment apparatus (1) is a water treatment apparatus having the configuration shown in FIGS. In the same manner, the water to be treated was decomposed.

<実施例3>
水処理装置(1)として、図1〜3に示す構成の水処理装置であって吸気用螺旋管部(7X)を直管に置き換えた構成(螺旋管部がない構成)のものを用いた以外は、実施例1と同様にして被処理水の分解処理を行った。
<Example 3>
As the water treatment device (1), a water treatment device having the configuration shown in FIGS. 1 to 3 and having a configuration in which the spiral pipe portion for intake (7X) is replaced with a straight pipe (configuration without the spiral pipe portion) was used. Except for the above, the water to be treated was decomposed in the same manner as in Example 1.

<実施例4>
水処理装置(1)として、図1〜3に示す構成の水処理装置であって紫外光反射板を省略し(紫外光反射板がない)且つ吸気用螺旋管部(7X)を省略した(直管に置き換えた)ものを用いた以外は、実施例1と同様にして被処理水の分解処理を行った。
<Example 4>
As the water treatment device (1), the water treatment device having the configuration shown in FIGS. 1 to 3, the ultraviolet light reflection plate is omitted (there is no ultraviolet light reflection plate), and the intake spiral tube portion (7X) is omitted ( The water to be treated was decomposed in the same manner as in Example 1 except that a straight pipe was used.

<比較例1>
水処理装置(1)として、図1〜3に示す構成の水処理装置であって吸気管を省略した構成(吸気管がない構成)のものを用いた以外は、実施例1と同様にして被処理水の分解処理を行った(紫外光照射のみ、オゾン利用なし)。
<Comparative Example 1>
The water treatment apparatus (1) is the same as that of the first embodiment except that the water treatment apparatus having the configuration shown in FIGS. 1 to 3 and having a configuration in which the intake pipe is omitted (a configuration having no intake pipe) is used. The water to be treated was decomposed (only ultraviolet light irradiation, not using ozone).

<比較例2>
水処理装置(1)として、図1〜3に示す構成の水処理装置であって内槽の内面にアルミニウム箔を貼着した構成のものを用いた以外は、実施例1と同様にして被処理水の分解処理を行った(オゾン生成用空間への紫外光照射により生じたオゾン利用のみ、通水用空間への紫外光照射はなし)。
<Comparative example 2>
The water treatment apparatus (1) is the same as in Example 1 except that the water treatment apparatus having the configuration shown in FIGS. 1 to 3 and having an aluminum tank attached to the inner surface of the inner tank is used. Treated water was decomposed (only use of ozone produced by irradiation of ultraviolet light into the ozone generation space, no irradiation of ultraviolet light into the water passage space).

Figure 2006158986
Figure 2006158986

表から明らかなように、この発明の処理装置を用いた処理方法で処理された実施例1〜4の処理水は、フェノール、p−クレゾール、p−クロロフェノールのいずれも十分に分解処理されていた。また、実施例1〜4における分解率は、フェノール、p−クレゾール、p−クロロフェノールのいずれにおいても、紫外光のみにより処理された比較例1での分解率とオゾンのみにより処理された比較例2での分解率との和よりも高い数値を示していた。これは、オゾンに紫外光が照射されてヒドロキシラジカルが生成し、このヒドロキシラジカルによって分解反応がより促進されたものと考えられる。   As is apparent from the table, the treated water of Examples 1 to 4 treated by the treatment method using the treatment apparatus of the present invention is sufficiently decomposed for phenol, p-cresol, and p-chlorophenol. It was. Moreover, the decomposition rate in Examples 1-4 is the comparative example processed only by the decomposition rate and ozone in the comparative example 1 processed only by ultraviolet light in any of phenol, p-cresol, and p-chlorophenol. 2 was higher than the sum of the decomposition rate in 2. It is considered that this is because ozone was irradiated with ultraviolet light to generate hydroxy radicals, and the decomposition reaction was further promoted by the hydroxy radicals.

また、外槽の外周面に紫外光反射板を積層した実施例3の分解率は、紫外光反射板を設けていない実施例4の分解率よりも高い数値であった。また、螺旋管部を設けた実施例2の分解率は、螺旋管部を設けていない実施例4の分解率よりも高い数値であった。更に、外槽の外周面に紫外光反射板を積層し且つ螺旋管部を設けた実施例1の分解率は、紫外光反射板及び螺旋管部を設けていない実施例4の分解率よりも顕著に高い数値であった。   Moreover, the decomposition rate of Example 3 which laminated | stacked the ultraviolet light reflecting plate on the outer peripheral surface of an outer tank was a numerical value higher than the decomposition rate of Example 4 which does not provide the ultraviolet light reflecting plate. Moreover, the decomposition rate of Example 2 in which the spiral tube portion was provided was higher than that in Example 4 in which the spiral tube portion was not provided. Furthermore, the decomposition rate of Example 1 in which the ultraviolet light reflector is laminated on the outer peripheral surface of the outer tub and the spiral tube portion is provided is higher than the decomposition rate of Example 4 in which the ultraviolet light reflector and the spiral tube portion are not provided. It was a remarkably high number.

この発明の水処理装置の一実施形態を示す斜視図である。It is a perspective view which shows one Embodiment of the water treatment apparatus of this invention. 図1の水処理装置の横断面図である。It is a cross-sectional view of the water treatment apparatus of FIG. 図1の水処理装置の縦断面図である。It is a longitudinal cross-sectional view of the water treatment apparatus of FIG. この発明の水処理装置の他の実施形態を示す斜視図である。It is a perspective view which shows other embodiment of the water treatment apparatus of this invention. この発明の水処理装置の他の実施形態を示す斜視図である。It is a perspective view which shows other embodiment of the water treatment apparatus of this invention. この発明の水処理装置のさらに他の実施形態を示す斜視図である。It is a perspective view which shows other embodiment of the water treatment apparatus of this invention.

符号の説明Explanation of symbols

1…水処理装置
2…外槽
3…内槽
4…オゾン生成用空間
5…通水用空間
6…紫外線ランプ
7…吸気管
7A…吸気用螺旋管部
8…アスピレーター(送気装置)
9…送水機
DESCRIPTION OF SYMBOLS 1 ... Water treatment apparatus 2 ... Outer tank 3 ... Inner tank 4 ... Space for ozone generation 5 ... Space for water flow 6 ... Ultraviolet lamp 7 ... Intake pipe 7A ... Spiral pipe part for intake 8 ... Aspirator (air supply device)
9 ... Water feeder

Claims (6)

オゾンを添加した被処理水に紫外線ランプからの紫外光を照射することによって、被処理水に含有される有機物質等を分解処理する水処理方法において、
前記添加オゾンとして、前記紫外線ランプの周囲に存在する酸素に対して該ランプからの紫外光が照射されることによって生成したオゾンを用いることを特徴とする紫外光とオゾンを併用した水処理方法。
In the water treatment method for decomposing organic substances contained in the water to be treated by irradiating the water to be treated with ozone with ultraviolet light from an ultraviolet lamp,
A water treatment method using ultraviolet light and ozone in combination, wherein as the added ozone, ozone generated by irradiating oxygen present around the ultraviolet lamp with ultraviolet light from the lamp is used.
水処理用外槽と、
前記外槽の内部に配置された内槽と、
前記内槽内に配置された紫外線ランプと、
一端が前記内槽と前記紫外線ランプの間のオゾン生成用空間に連通接続され、他端が前記外槽と内槽の間の通水用空間に連通接続された吸気管と、
前記吸気管内の気体を前記オゾン生成用空間側から通水用空間側に向けて送気する送気装置とを備えることを特徴とする紫外光とオゾンを併用した水処理装置。
An outer tank for water treatment,
An inner tank disposed inside the outer tank;
An ultraviolet lamp disposed in the inner tank;
An intake pipe having one end connected in communication with the ozone generating space between the inner tank and the ultraviolet lamp, and the other end connected in communication with the water passing space between the outer tank and the inner tank;
A water treatment device using ultraviolet light and ozone in combination, comprising: an air supply device for supplying the gas in the intake pipe from the ozone generation space side to the water flow space side.
水処理用外槽と、
前記外槽の内部に配置された内槽と、
前記内槽内に配置された紫外線ランプと、
一端が前記内槽と前記紫外線ランプの間のオゾン生成用空間に連通接続され、他端が前記外槽と内槽の間の通水用空間に連通接続された吸気管と、
前記吸気管の途中位置に取り付けられたアスピレーターとを備えることを特徴とする紫外光とオゾンを併用した水処理装置。
An outer tank for water treatment,
An inner tank disposed inside the outer tank;
An ultraviolet lamp disposed in the inner tank;
An intake pipe having one end connected in communication with the ozone generating space between the inner tank and the ultraviolet lamp, and the other end connected in communication with the water passing space between the outer tank and the inner tank;
A water treatment apparatus using ultraviolet light and ozone in combination, comprising: an aspirator attached to an intermediate position of the intake pipe.
前記吸気管におけるアスピレーターから通水用空間までの位置の少なくとも一部が螺旋状に形成されている請求項3に記載の紫外光とオゾンを併用した水処理装置。   The water treatment apparatus using both ultraviolet light and ozone according to claim 3, wherein at least a part of a position from the aspirator to the water passage space in the intake pipe is formed in a spiral shape. 前記外槽が、内方側に紫外光を反射する反射板で構成されている請求項2〜4のいずれか1項に記載の紫外光とオゾンを併用した水処理装置。   The water treatment apparatus which used together the ultraviolet light and ozone of any one of Claims 2-4 by which the said outer tank is comprised with the reflecting plate which reflects an ultraviolet light inward. 前記外槽の外側または内側に、内方側に紫外光を反射する反射板が配置されている請求項2〜4のいずれか1項に記載の紫外光とオゾンを併用した水処理装置。   The water treatment apparatus using ultraviolet light and ozone according to any one of claims 2 to 4, wherein a reflection plate that reflects ultraviolet light is disposed on the inner side of the outer tank or the inner side thereof.
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KR100835585B1 (en) 2008-02-11 2008-06-09 유네코개발 주식회사 Water treatment apparatus utilizing advanced oxidation process
CN101962213A (en) * 2010-10-21 2011-02-02 东南大学 Energy-saving multitube photochemical excitation/oxidation water advanced treatment device
WO2015130156A1 (en) * 2014-02-27 2015-09-03 Worldwide Industries Pte Ltd. Water purification device
CN106396072A (en) * 2016-09-05 2017-02-15 深圳市开天源自动化工程有限公司 Advanced oxidation water treatment device
CN111484176A (en) * 2020-05-26 2020-08-04 清华大学 Dual-waveband ultraviolet light catalytic advanced oxidation device and process

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JPS63130186A (en) * 1986-11-21 1988-06-02 Fumio Denpo Recirculation type sterilization and purification of liquid tank
JPH0281687U (en) * 1988-12-01 1990-06-25
JP2000093953A (en) * 1998-09-25 2000-04-04 Kubota Corp Apparatus for decomposing hardly decomposable organic substance and method for removing using the same hardly decomposable organic substance

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100835585B1 (en) 2008-02-11 2008-06-09 유네코개발 주식회사 Water treatment apparatus utilizing advanced oxidation process
CN101962213A (en) * 2010-10-21 2011-02-02 东南大学 Energy-saving multitube photochemical excitation/oxidation water advanced treatment device
WO2015130156A1 (en) * 2014-02-27 2015-09-03 Worldwide Industries Pte Ltd. Water purification device
CN106396072A (en) * 2016-09-05 2017-02-15 深圳市开天源自动化工程有限公司 Advanced oxidation water treatment device
CN111484176A (en) * 2020-05-26 2020-08-04 清华大学 Dual-waveband ultraviolet light catalytic advanced oxidation device and process

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