JPH07280242A - Offensive gas incinerator - Google Patents
Offensive gas incineratorInfo
- Publication number
- JPH07280242A JPH07280242A JP6576494A JP6576494A JPH07280242A JP H07280242 A JPH07280242 A JP H07280242A JP 6576494 A JP6576494 A JP 6576494A JP 6576494 A JP6576494 A JP 6576494A JP H07280242 A JPH07280242 A JP H07280242A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- gas
- chamber
- xylene
- offensive
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、悪臭ガス焼却装置、特
にキシレンやトルエン等を含む悪臭ガスを焼却するため
の装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for burning offensive odor gas, and more particularly to an apparatus for incinerating offensive odor gas containing xylene, toluene and the like.
【0002】[0002]
【発明の背景】近年、キシレンやトルエン等悪臭源とな
るガスを取り扱う工場から、これらの悪臭ガスを大気中
に放出することが問題とされており、平成6年4月から
は悪臭防止法が施行される。いけす用の網や漁網のメー
カーでは、網に海草やこけ類あるいは汚れが付着するこ
とを防止する目的で、網をキシレンで処理しており、従
来ではキシレンを含む悪臭ガスを生ガスで薄めて大気中
に放出していたが、今後は大きく規制されることとな
る。BACKGROUND OF THE INVENTION In recent years, it has been a problem to release these malodorous gases into the atmosphere from a factory that handles gases such as xylene and toluene, which are sources of malodorous substances. Will be enforced. Manufacturers of nets for fishing and fishing nets treat the nets with xylene for the purpose of preventing seaweeds, moss and dirt from adhering to the nets. Conventionally, the malodorous gas containing xylene is diluted with raw gas. Although it was released into the atmosphere, it will be greatly regulated in the future.
【0003】ところで、ペイント製造業や塗布業等のキ
シレンやトルエンを大量に取り扱う工場では、解媒方式
によって悪臭ガスを分解している。しかし、解媒方式で
は大規模な設備を必要とし、中小の工場向きではない。
中小の工場では、ガスバーナで悪臭ガスを焼くことが考
えられるが、これでは多量の燃料ガスを必要とし、ラン
ニングコストが高く付いてしまう。By the way, in factories handling a large amount of xylene and toluene in the paint manufacturing industry and the coating industry, the malodorous gas is decomposed by a desolvation method. However, the dissolution method requires large-scale equipment and is not suitable for small and medium-sized factories.
In small and medium-sized factories, it is possible to burn offensive odor gas with a gas burner, but this requires a large amount of fuel gas, which results in high running costs.
【0004】[0004]
【発明の目的、構成、作用、効果】そこで、本発明の目
的は、簡単な構成からなり、ランニングコストの安い悪
臭ガス焼却装置を提供することにある。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a malodorous gas incinerator having a simple structure and a low running cost.
【0005】以上の目的を達成するため、本発明に係る
悪臭ガス焼却装置は、多数の小孔を形成したステンレス
製の焼却皿と、この焼却皿を赤熱させるガスバーナとを
備え、ガスバーナで赤熱された焼却皿に悪臭ガスを送り
込んで大気中に放出することを特徴とする。In order to achieve the above object, the malodorous gas incinerator according to the present invention comprises a stainless steel incinerator plate having a large number of small holes and a gas burner for heating the incinerator plate to red heat. The odorous gas is sent to the incinerator and released into the atmosphere.
【0006】赤熱された焼却皿の小孔を悪臭ガスが通過
することにより、キシレン、トルエン等の成分が分解
し、これらの成分が殆んど零になる。本発明は、焼却皿
とその赤熱用ガスバーナを主要な構成として、焼却皿へ
の悪臭ガス送込み手段及び排気手段と付設するという簡
単な構成からなる。しかも、燃料はステンレス製の焼却
皿を赤熱させるガスバーナへ供給するガス(通常プロパ
ンガスを使用)だけで済み、焼却用燃料費が極めて安
く、ラニングコストが安く付く。When the malodorous gas passes through the small holes of the incinerator which is heated red, the components such as xylene and toluene are decomposed, and these components become almost zero. The present invention has a simple structure in which the incinerator and the red-hot gas burner are the main components, and the malodorous gas feeding means and the exhaust means are attached to the incinerator. Moreover, the fuel is only the gas (usually propane gas is used) supplied to the gas burner that heats the stainless incinerator red, and the fuel cost for incineration is extremely low and the running cost is low.
【0007】さらに、本発明に係る悪臭ガス焼却装置に
おいては、前記焼却皿の下方に水密室を設け、悪臭ガス
をこの水密室を通じて焼却皿へ送り込むことが好まし
い。ガスの誘爆を回避するためである。Further, in the malodorous gas incinerator according to the present invention, it is preferable that a watertight chamber is provided below the incinerator and the malodorous gas is sent to the incinerator through the watertight chamber. This is to avoid the gas explosion.
【0008】[0008]
【実施例】以下、本発明に係る悪臭ガス焼却装置の実施
例について添付図面を参照して説明する。図1は本焼却
装置の設置状況を示し、1は工場、2は防爆タンク、3
は防火壁、4は焼却装置本体、5はコンクリート製の台
座である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the malodorous gas incinerator according to the present invention will be described below with reference to the accompanying drawings. Figure 1 shows the installation status of the incinerator, 1 is a factory, 2 is an explosion-proof tank, 3
Is a fire wall, 4 is an incinerator body, and 5 is a pedestal made of concrete.
【0009】工場1内ではキシレンが使用され、100
〜200ppmのキシレンを含む悪臭ガスが発生してい
るとする。工場1内には吸収管11,11が配設され、
2基のエアポンプ12,12によって悪臭ガスが防爆タ
ンク2へ導かれる。防爆タンク2は所定量の水を満たし
たもので、吸収管11,11の末端は水中に沈められて
いる。防爆タンク2の上部からはステンレス製の配管2
1が導出され、この配管21は防火壁3を貫通して焼却
装置本体4へ接続されている。即ち、工場1内の悪臭ガ
スは、吸収管11,11で吸い込まれ、防爆タンク2内
の水をくぐり、配管21を通じて焼却装置本体4へ送り
込まれる。Xylene is used in the factory 1, and 100
It is assumed that a foul-smelling gas containing ~ 200 ppm xylene is generated. Absorption pipes 11, 11 are installed in the factory 1,
Malodorous gas is guided to the explosion-proof tank 2 by the two air pumps 12, 12. The explosion-proof tank 2 is filled with a predetermined amount of water, and the ends of the absorption tubes 11 and 11 are submerged in water. Piping 2 made of stainless steel from the top of the explosion-proof tank 2
1 is drawn out, and this pipe 21 penetrates the fire wall 3 and is connected to the incinerator main body 4. That is, the malodorous gas in the factory 1 is sucked by the absorption pipes 11 and 11, passes through the water in the explosion-proof tank 2, and is sent to the incinerator body 4 through the pipe 21.
【0010】図2は焼却装置本体4の内部構成を示し、
下から順次、水密室41、加熱室45、焼却室50、排
気筒55にて構成されている。焼却室50の下部にはド
ーム状の焼却皿51が設置されている。この焼却皿51
はステンレス材からなり、表裏に貫通する多数の小孔5
2が全面に一様に形成されている。加熱室45内にはプ
ロパンガスバーナ46が設置され、供給管47からプロ
パンガスと空気の混合燃料が送り込まれてくる。このプ
ロパンガスバーナ46は前記ステンレス製の焼却皿51
を赤熱させるためのものである。FIG. 2 shows the internal structure of the incinerator body 4,
It is composed of a watertight chamber 41, a heating chamber 45, an incinerator chamber 50, and an exhaust stack 55 in order from the bottom. A dome-shaped incinerator 51 is installed below the incinerator 50. This incineration dish 51
Is made of stainless steel and has a large number of small holes 5 that penetrate the front and back.
2 are formed uniformly on the entire surface. A propane gas burner 46 is installed in the heating chamber 45, and a mixed fuel of propane gas and air is fed from a supply pipe 47. This propane gas burner 46 is the stainless steel incinerator 51 described above.
It is for making the red hot.
【0011】水密室41は所定量の水が吸水口42から
満たされ、前記配管21の末端が水中に沈められてい
る。この水密室41も前記防爆タンク2と同様に工場1
内のガスの誘発を防止するために設置されている。ま
た、水密室41の上部には多数の小孔44を形成した隔
壁43が設置されている。The watertight chamber 41 is filled with a predetermined amount of water through the water inlet 42, and the end of the pipe 21 is submerged in water. This watertight chamber 41 is the same as the explosion-proof tank 2 in the factory 1
It is installed to prevent the induction of gas inside. Further, a partition wall 43 having a large number of small holes 44 is installed above the watertight chamber 41.
【0012】以上の構成からなる本焼却装置において、
吸収管11,11で吸収された工場1内のキシレンガス
(濃度100〜200ppm)は防爆タンク2を介して
水密室41へ導かれ、ガスバーナ46の隙間部を通じて
焼却皿51へ上昇する。焼却皿51はガスナーナ46に
よって赤熱された状態にあり、焼却皿51の小孔52を
キシレンガスが通過していく、この通過時にキシレンが
水及び炭酸ガスとなり、最終的に水素、酸素、炭酸ガス
に分解され、排気筒55から放出される。この放出され
るガスに悪臭の元となるキシレンは殆んど含まれていな
い。In the incinerator having the above structure,
The xylene gas (concentration 100 to 200 ppm) in the factory 1 absorbed by the absorption pipes 11, 11 is guided to the watertight chamber 41 via the explosion-proof tank 2 and rises to the incinerator 51 through the gap of the gas burner 46. The incinerator 51 is in a state of being red-heated by the gas nanar 46, and xylene gas passes through the small holes 52 of the incinerator 51. During this passage, xylene becomes water and carbon dioxide gas, and finally hydrogen, oxygen, carbon dioxide gas. And is discharged from the exhaust pipe 55. The released gas contains almost no xylene, which causes odor.
【0013】本実施例は、内積1500m3の工場で、
1分間に0.4m3のキシレンガス(100ppm)が
発生することを前提に設計されたものである。大きさ
は、水密室41と加熱室45を合わせた高さが1m、焼
却室50の高さが1.5m、これらの直径が80cm、
排気筒55の高さが2m、その直径が40cm、フード
56の高さが30cmである。This embodiment is a factory with an inner product of 1500 m 3 ,
It is designed on the assumption that 0.4 m 3 of xylene gas (100 ppm) is generated in 1 minute. As for the size, the total height of the watertight chamber 41 and the heating chamber 45 is 1 m, the height of the incineration chamber 50 is 1.5 m, and the diameter of these is 80 cm.
The height of the exhaust pipe 55 is 2 m, the diameter thereof is 40 cm, and the height of the hood 56 is 30 cm.
【0014】エアポンプ12はそれぞれ毎分0.2m3
の風量を有し、焼却室50を通過するガスの速度は毎分
0.8mである。また、ガスバーナ46は5段階に火力
を調整可能であり、焼却皿51は約700〜800℃に
加熱される。エアポンプ12の風量やガスバーナ46の
火力は、キシレンの発生量によって適宜調整される。Each air pump 12 has a flow rate of 0.2 m 3 / min.
And the velocity of the gas passing through the incineration chamber 50 is 0.8 m / min. Further, the gas burner 46 can adjust the heating power in five stages, and the incinerator 51 is heated to about 700 to 800 ° C. The air volume of the air pump 12 and the heating power of the gas burner 46 are appropriately adjusted depending on the amount of xylene generated.
【0015】なお、本発明に係る悪臭ガス焼却装置は前
記実施例に限定するものではなく、その要旨の範囲内で
種々に変更可能なことは勿論である。The malodorous gas incinerator according to the present invention is not limited to the above-described embodiment, and it goes without saying that various modifications can be made within the scope of the gist.
【図1】本発明に係る悪臭ガス焼却装置の配置を示す立
面図。FIG. 1 is an elevational view showing an arrangement of a malodorous gas incinerator according to the present invention.
【図2】前記焼却装置の本体部分の垂直断面図。FIG. 2 is a vertical sectional view of a main body portion of the incineration device.
4…焼却装置本体 12…エアポンプ 41…水密室 45…加熱室 46…ガスバーナ 50…焼却室 51…焼却皿 52…小孔 55…排気筒 4 ... Incinerator body 12 ... Air pump 41 ... Watertight chamber 45 ... Heating chamber 46 ... Gas burner 50 ... Incineration chamber 51 ... Incinerator 52 ... Small hole 55 ... Exhaust stack
Claims (2)
却皿と、 前記焼却皿を赤熱させるガスバーナと、 前記焼却皿へ悪臭ガスを送り込む手段と、 前記焼却皿で焼却されたガスを大気中へ排出する手段
と、 を備えたことを特徴とする悪臭ガス焼却装置。1. A stainless steel incinerator having a large number of small holes, a gas burner for making the incinerator red heat, a means for feeding a malodorous gas to the incinerator, and a gas incinerated by the incinerator in the atmosphere. And a means for discharging the odorous gas to the incinerator.
ガスをこの水密室を通じて焼却皿へ送り込むことを特徴
とする請求項1記載の悪臭ガス焼却装置。2. The malodorous gas incinerator according to claim 1, wherein a watertight chamber is provided below the incinerator dish, and malodorous gas is sent to the incinerator dish through the watertight chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6576494A JPH07280242A (en) | 1994-04-04 | 1994-04-04 | Offensive gas incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6576494A JPH07280242A (en) | 1994-04-04 | 1994-04-04 | Offensive gas incinerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07280242A true JPH07280242A (en) | 1995-10-27 |
Family
ID=13296421
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6576494A Pending JPH07280242A (en) | 1994-04-04 | 1994-04-04 | Offensive gas incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07280242A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011094861A (en) * | 2009-10-29 | 2011-05-12 | Chugai Ro Co Ltd | Combustion detoxifying method and device for multicomponent-based volatile organic solvent |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5235761A (en) * | 1975-09-17 | 1977-03-18 | Tokyo Seni Kogyo Kk | Deodorizing filter |
JPS5537450A (en) * | 1978-09-07 | 1980-03-15 | Fujitsu Ltd | Production of glass for light transmission body |
JPS57157391A (en) * | 1981-03-25 | 1982-09-28 | Hosoya Fireworks | Smoke ball |
-
1994
- 1994-04-04 JP JP6576494A patent/JPH07280242A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5235761A (en) * | 1975-09-17 | 1977-03-18 | Tokyo Seni Kogyo Kk | Deodorizing filter |
JPS5537450A (en) * | 1978-09-07 | 1980-03-15 | Fujitsu Ltd | Production of glass for light transmission body |
JPS57157391A (en) * | 1981-03-25 | 1982-09-28 | Hosoya Fireworks | Smoke ball |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011094861A (en) * | 2009-10-29 | 2011-05-12 | Chugai Ro Co Ltd | Combustion detoxifying method and device for multicomponent-based volatile organic solvent |
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