JP2000176247A - Waste ozone decomposing device - Google Patents

Waste ozone decomposing device

Info

Publication number
JP2000176247A
JP2000176247A JP10361732A JP36173298A JP2000176247A JP 2000176247 A JP2000176247 A JP 2000176247A JP 10361732 A JP10361732 A JP 10361732A JP 36173298 A JP36173298 A JP 36173298A JP 2000176247 A JP2000176247 A JP 2000176247A
Authority
JP
Japan
Prior art keywords
ozone
catalyst
decomposing
ozone decomposing
layer
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
JP10361732A
Other languages
Japanese (ja)
Inventor
Takahiro Fujiwara
高広 藤原
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP10361732A priority Critical patent/JP2000176247A/en
Publication of JP2000176247A publication Critical patent/JP2000176247A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Abstract

PROBLEM TO BE SOLVED: To provide a waste ozone decomposing device capable of efficiently decomposing waste ozone by using an ozone decomposing catalyst an capable of easily replacing the catalyst having lost its decomposing capacity. SOLUTION: In the waste ozone decomposing device arranging an ozone decomposing catalyst layer 6 inside a tank body 1, the gas flow passage 5 passing downward through the ozone decomposing catalyst layer 6 is provided by providing a gas inlet 3 at above the ozone decomposing catalyst layer 6 and providing a gas outlet 4 under the ozone decomposing catalyst layer 6. The catalyst becoming small by the wear can be retained and also replacing only upper side catalyst having lost the decomposing capacity is possible since the wear of the ozone decomposing catalyst such as activated carbon 8 is generated at the upper part of the layer.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、オゾン接触池など
のオゾン処理装置や設備から排出された排オゾンを分解
する排オゾン分解装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for decomposing ozone discharged from an ozone treatment apparatus or equipment such as an ozone contact pond.

【0002】[0002]

【従来の技術】従来、浄水処理や廃水処理などの水処理
分野では、オゾンの持つ強い酸化分解作用を利用して、
殺菌、鉄・マンガンなどの色度成分の除去、シアン化合
物やフェノールの分解、廃水の最終処理などを行ってい
る。
2. Description of the Related Art Conventionally, in the field of water treatment such as water purification treatment and wastewater treatment, the strong oxidative decomposition action of ozone is utilized.
It performs sterilization, removal of chromatic components such as iron and manganese, decomposition of cyanide and phenol, and final treatment of wastewater.

【0003】その際にオゾン処理装置や設備から排出さ
れた排オゾンは、排オゾン分解装置に導入してオゾン分
解触媒と接触させることにより酸素と酸化触媒とに分解
し、無害な気体として大気中に放出するようにしてい
る。
[0003] At that time, the exhausted ozone discharged from the ozone treatment device or equipment is introduced into the exhausted ozone decomposing device and brought into contact with the ozone decomposing catalyst to be decomposed into oxygen and an oxidizing catalyst. To be released.

【0004】[0004]

【発明が解決しようとする課題】ところが、従来の排オ
ゾン分解装置では、排オゾン(またはそれを含有する排
ガス)はオゾン分解触媒層の下方に流入して層内を上向
きに通流するようになっているので、オゾンとの接触率
が高い層下部のオゾン分解触媒が消耗し易く、消耗した
触媒はそのタイプによって、オゾン分解能力をなくした
まま留まるか、小さくなって触媒支持材の通気孔をすり
抜けてしまうかのいずれかである。そのためオゾン分解
効率、触媒利用率とも悪く、またオゾン分解能力をなく
した触媒の交換も容易ではない。
However, in the conventional exhaust ozone decomposition apparatus, the exhaust ozone (or the exhaust gas containing the same) flows below the ozone decomposition catalyst layer and flows upward in the layer. The ozone decomposing catalyst in the lower part of the layer, which has a high contact rate with ozone, is easily consumed, and depending on the type, the exhausted catalyst can remain with its ozone decomposing ability lost or become smaller and become a vent hole in the catalyst support material. Either. Therefore, both the ozone decomposition efficiency and the catalyst utilization rate are poor, and it is not easy to replace the catalyst which has lost the ozone decomposition ability.

【0005】本発明は上記問題を解決するもので、オゾ
ン分解触媒を有効に利用して効率よく排オゾンを分解で
きるとともに、分解能力をなくした触媒は容易に交換で
きる排オゾン分解装置を提供することを目的とするもの
である。
The present invention solves the above-mentioned problems, and provides an exhaust ozone decomposing apparatus capable of effectively decomposing exhaust ozone by effectively using an ozone decomposition catalyst and easily replacing a catalyst having no decomposition ability. It is intended for that purpose.

【0006】[0006]

【課題を解決するための手段】上記問題を解決するため
に本発明は、槽体の内部にオゾン分解触媒層を配置した
排オゾン分解装置において、オゾン分解触媒層の上方に
ガス流入部を設け、下方にガス流出部を設けて、オゾン
分解触媒層を下向きに通流するガス流路を形成したこと
を特徴とする。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to a waste ozonolysis apparatus having an ozonolysis catalyst layer disposed inside a tank body, wherein a gas inflow section is provided above the ozonolysis catalyst layer. , A gas outlet is provided below, and a gas flow path that flows downward through the ozone decomposition catalyst layer is formed.

【0007】上記した構成によれば、排オゾンはオゾン
分解触媒層を下向きに通流するので、層上部のオゾン分
解触媒が消耗し易くなり、オゾン分解能力を失ったり、
小さくなったりする。
[0007] According to the above structure, the exhausted ozone flows downward through the ozone decomposition catalyst layer, so that the ozone decomposition catalyst in the upper part of the layer is easily consumed, and the ozone decomposition ability is lost.
Or become smaller.

【0008】しかし、小さくなったオゾン分解触媒は触
媒層自体で支持されるので、このタイプのオゾン分解触
媒は従来より長い期間、触媒能力を発揮することにな
る。また、オゾン分解能力を失うタイプのオゾン分解触
媒は適当な時期に上層部分だけ交換すればよく、交換が
容易であるとともに、従来より有効に利用できる。
However, since the reduced ozonolysis catalyst is supported by the catalyst layer itself, this type of ozonolysis catalyst will exert its catalytic ability for a longer period of time than before. Further, the ozone decomposing catalyst of the type that loses the ozone decomposing ability only has to be replaced at an appropriate time only in the upper layer portion, and it is easy to replace and can be used more effectively than before.

【0009】つまり、いずれのタイプのオゾン分解触媒
を使用した場合も、従来より有効に利用して効率よく排
オゾンを分解することができ、後者の場合は交換も容易
である。
That is, no matter which type of ozone decomposing catalyst is used, the exhausted ozone can be decomposed more efficiently and efficiently than in the past, and in the latter case, replacement is easy.

【0010】[0010]

【発明の実施の形態】以下、本発明の実施形態を図面を
参照しながら説明する。図1に示した排オゾン分解装置
において、槽体1は上部開口を覆う蓋体2を有して密閉
式に構成されている。この槽体1には、上部に設けられ
たガス流入口3と下部に設けられた複数のガス流出口4
とにより上下方向の槽体内流路5が形成されており、こ
の槽体内流路5の途中にオゾン分解触媒層6が設けられ
ている。
Embodiments of the present invention will be described below with reference to the drawings. In the waste ozonolysis apparatus shown in FIG. 1, the tank body 1 has a lid 2 that covers the upper opening, and is configured as a closed type. The tank 1 has a gas inlet 3 provided at an upper portion and a plurality of gas outlets 4 provided at a lower portion.
Thus, a vertical flow path 5 in the tank is formed, and an ozone decomposition catalyst layer 6 is provided in the middle of the flow path 5 in the tank.

【0011】詳細にはオゾン分解触媒層6は、槽体内流
路5を横切る方向に沿って配置され周縁部が槽体内周面
に摺接するメッシュ状の触媒支持体7の上に、オゾン分
解触媒としての粒状活性炭8を積層したものであり、ガ
ス流入口3より下方かつガス流出口4より上方に位置し
ている。
More specifically, the ozone decomposition catalyst layer 6 is disposed on a mesh-shaped catalyst support 7 which is arranged along the direction traversing the flow path 5 in the tank and whose peripheral edge is in sliding contact with the peripheral surface of the tank. And is located below the gas inlet 3 and above the gas outlet 4.

【0012】上記した構成における作用を説明する。排
オゾンを含んだ排ガス9はガス流入口3より槽体1に導
入されて槽体内流路5を下降し、オゾン分解触媒層6を
通過し、活性炭8との接触によりオゾンを分解され、オ
ゾンの分解生成物たる酸素とともにガス流出口4より大
気中に流出していく。
The operation of the above configuration will be described. Exhaust gas 9 containing exhausted ozone is introduced into the tank 1 through the gas inlet 3, descends through the inside of the tank flow path 5, passes through the ozone decomposition catalyst layer 6, and is decomposed by contact with the activated carbon 8 to decompose ozone. Flows out into the atmosphere from the gas outlet 4 together with oxygen as a decomposition product of the gas.

【0013】排ガス9の導入を続けるうちに、排オゾン
との接触機会が大きい上部の活性炭8から順に小さくな
るが、小さくなった活性炭8もそれより下方の活性炭8
の層に支持されて触媒支持体7をすり抜けることなく留
まり、触媒能力を発揮するので、オゾン分解触媒層6に
おける排オゾン分解効率は高く維持される。
As the introduction of the exhaust gas 9 is continued, the activated carbon 8 having a greater chance of contact with the exhausted ozone is reduced in order from the upper activated carbon 8.
, And stays without slipping through the catalyst support 7 to exhibit the catalytic ability, so that the efficiency of the exhausted ozone decomposition in the ozone decomposition catalyst layer 6 is kept high.

【0014】排オゾン分解効率がある程度まで低下した
ら活性炭8を交換するが、その時には、蓋体2を開いて
上部開口より容易に交換作業を行える。小さくなった上
層部の活性炭8のみ交換してもよい。
When the efficiency of decomposing ozone is reduced to some extent, the activated carbon 8 is replaced. At this time, the cover 2 is opened and the replacement operation can be easily performed through the upper opening. Only the activated carbon 8 in the upper layer which has become smaller may be replaced.

【0015】上記した粒状活性炭8に代えて、オゾン分
解触媒として一般に使用されている酸化マンガン触媒9
を使用してもよい。この場合、排オゾンとの接触機会が
大きい上部の酸化マンガン触媒9より順にオゾン分解能
力を失うので、排オゾン分解効率が低下した時には、上
部の酸化マンガン触媒9のみを交換するようにすればよ
い。
Instead of the above-mentioned granular activated carbon 8, a manganese oxide catalyst 9 generally used as an ozone decomposition catalyst is used.
May be used. In this case, since the upper manganese oxide catalyst 9 having the greatest chance of contact with the exhausted ozone loses the ozone decomposition ability in order, when the efficiency of the exhausted ozone decomposition is reduced, only the upper manganese oxide catalyst 9 may be replaced. .

【0016】また、図2に示したように、下層部に酸化
マンガン触媒9を積層し、上層部に粒状活性炭8を積層
して、オゾン分解触媒層6を2層構造としてもよい。こ
の場合、排オゾンとの接触機会が大きい上部の活性炭8
から順に小さくなり、酸化マンガン触媒9の上部より順
にオゾン分解能力を失うが、小さくなった活性炭8はそ
れより下方の活性炭8の層のみならず酸化マンガン触媒
9の層に支持されて留まる。したがって、排オゾン分解
効率が低下した時には、活性炭8の層と酸化マンガン触
媒9の上部のみを交換するようにすればよい。
Further, as shown in FIG. 2, the manganese oxide catalyst 9 may be laminated on the lower part, and the granular activated carbon 8 may be laminated on the upper part, so that the ozone decomposition catalyst layer 6 may have a two-layer structure. In this case, the activated carbon 8 in the upper part, which has a large chance of contact with the exhausted ozone,
From the top, and loses the ozone decomposition ability in order from the top of the manganese oxide catalyst 9, but the reduced activated carbon 8 remains supported not only by the layer of the activated carbon 8 below but also by the layer of the manganese oxide catalyst 9. Therefore, when the waste ozone decomposition efficiency decreases, only the layer of the activated carbon 8 and the upper part of the manganese oxide catalyst 9 need to be replaced.

【0017】上記したように、いずれのタイプのオゾン
分解触媒を使用した場合も、従来より有効に利用して効
率よく排オゾンを分解できるとともに、オゾン分解能力
を失った触媒のみを交換することができ、交換作業が容
易になり、維持費も節減できる。
As described above, no matter which type of ozone decomposing catalyst is used, it is possible to effectively decompose exhausted ozone by using the catalyst more effectively than before, and to replace only the catalyst which has lost the ozone decomposing ability. Replacement work becomes easier and maintenance costs can be reduced.

【0018】[0018]

【発明の効果】以上のように、本発明によれば、オゾン
分解触媒層を下向きに通流するガス流路を形成すること
により、オゾン分解触媒の消耗を層上部で発生させるよ
うにしたので、消耗によって小さくなった触媒も保持し
て効率よく排オゾンを分解できるとともに、オゾン分解
能力を失った触媒のみ交換することができ、維持費も節
減できる。
As described above, according to the present invention, the exhaustion of the ozone decomposition catalyst occurs at the upper part of the layer by forming the gas flow path that flows downward through the ozone decomposition catalyst layer. The exhausted ozone can be efficiently decomposed by holding the catalyst which has been reduced by exhaustion, and only the catalyst having lost the ozone decomposing ability can be replaced, so that the maintenance cost can be reduced.

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

【図1】本発明の一実施形態における排オゾン分解装置
を示した説明図である。
FIG. 1 is an explanatory diagram showing a waste ozone decomposing device according to an embodiment of the present invention.

【図2】同排オゾン分解装置でオゾン分解触媒層を2層
構造にした状態を示した説明図である。
FIG. 2 is an explanatory diagram showing a state in which an ozone decomposition catalyst layer has a two-layer structure in the waste ozone decomposition apparatus.

【符号の説明】[Explanation of symbols]

1 槽体 3 ガス流入部 4 ガス流出部 5 ガス流路 6 オゾン分解触媒層 9 排ガス(排オゾン) DESCRIPTION OF SYMBOLS 1 Tank body 3 Gas inflow part 4 Gas outflow part 5 Gas flow path 6 Ozone decomposition catalyst layer 9 Exhaust gas (exhausted ozone)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 槽体の内部にオゾン分解触媒層を配置し
た排オゾン分解装置において、オゾン分解触媒層の上方
にガス流入部を設け、下方にガス流出部を設けて、オゾ
ン分解触媒層を下向きに通流するガス流路を形成したこ
とを特徴とする排オゾン分解装置。
1. An exhaust ozonolysis device having an ozonolysis catalyst layer disposed inside a tank body, wherein a gas inflow portion is provided above the ozonolysis catalyst layer, and a gas outflow portion is provided below the ozonolysis catalyst layer. An exhaust ozone decomposer characterized by forming a gas flow path flowing downward.
JP10361732A 1998-12-21 1998-12-21 Waste ozone decomposing device Pending JP2000176247A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10361732A JP2000176247A (en) 1998-12-21 1998-12-21 Waste ozone decomposing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10361732A JP2000176247A (en) 1998-12-21 1998-12-21 Waste ozone decomposing device

Publications (1)

Publication Number Publication Date
JP2000176247A true JP2000176247A (en) 2000-06-27

Family

ID=18474697

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10361732A Pending JP2000176247A (en) 1998-12-21 1998-12-21 Waste ozone decomposing device

Country Status (1)

Country Link
JP (1) JP2000176247A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015085308A (en) * 2013-11-01 2015-05-07 トヨタ自動車株式会社 Atmosphere purification device for vehicle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015085308A (en) * 2013-11-01 2015-05-07 トヨタ自動車株式会社 Atmosphere purification device for vehicle

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