JPS6246120A - Foul odor gas treating method - Google Patents
Foul odor gas treating methodInfo
- Publication number
- JPS6246120A JPS6246120A JP18365685A JP18365685A JPS6246120A JP S6246120 A JPS6246120 A JP S6246120A JP 18365685 A JP18365685 A JP 18365685A JP 18365685 A JP18365685 A JP 18365685A JP S6246120 A JPS6246120 A JP S6246120A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- foul odor
- odor
- blown
- air
- 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
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は、し尿処理装置及び下水処理装置から発生す
る悪臭ガスの処理方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a method for treating malodorous gas generated from human waste treatment equipment and sewage treatment equipment.
(従来技術及びその問題点)
し尿処理装置から発生する悪臭ガス(高濃度臭気及び低
濃度臭気)は、一般に薬剤による洗浄と活(主炎による
吸着とを組合せて処理された後、大気放出されている。(Prior art and its problems) Malodorous gases (high-concentration odor and low-concentration odor) generated from human waste treatment equipment are generally treated by a combination of cleaning with chemicals and activation (adsorption by main flame), and then released into the atmosphere. ing.
また下水処理装置から発生する悪臭ガス(汚泥乾燥機排
ガス)についても一般に同様の処理がなされてい、る。Similar treatment is also generally applied to foul-smelling gas (sludge dryer exhaust gas) generated from sewage treatment equipment.
しかし、この処理方法は、イニシャルコスト特にランニ
ングコスト分が碌めて高い問題がある。However, this processing method has a problem in that the initial cost, particularly the running cost, is extremely high.
(発明が解決しようとする問題点)
この発明は、し尿処理装置や下水処理装置から発生する
悪臭ガスにつき、ごみ焼却炉を利用して安価に臭気処理
できる方法を得んとするものである。(Problems to be Solved by the Invention) The present invention aims to provide a method for inexpensively treating foul-smelling gases generated from human waste treatment equipment and sewage treatment equipment using a garbage incinerator.
(発明の構成)
即ちこの発明は、し尿処理装置及び下水処理装置の少な
くとも一方から発生する高濃度臭気を含む排ガス及び汚
泥乾燥機の排ガスをごみ焼却炉の燃焼室に炉温制御用空
気として吹込み、かつ前記両処理装置の少なくとも一方
から発生する低濃度臭気を含む排ガスの一部又は全部を
ごみ焼却炉の火格子下から燃焼用空気として吹き込む悪
臭ガス処理方法である。(Structure of the Invention) That is, the present invention blows exhaust gas containing highly concentrated odor generated from at least one of a human waste treatment device and a sewage treatment device and exhaust gas from a sludge dryer into the combustion chamber of a garbage incinerator as air for controlling furnace temperature. In this method, a part or all of the exhaust gas containing low-concentration odor generated from at least one of the two treatment devices is blown as combustion air from under the grate of the garbage incinerator.
(実施例) 以下この発明を図示する実施例を参照して説明する。(Example) The present invention will be described below with reference to illustrative embodiments.
し尿処理装all及び下水処理装置2の少なくとも一方
から発生する高濃度臭気を含む排ガスを送風a3により
ごみ焼却炉4の燃焼室5に炉温制御用空気として吹込む
。Exhaust gas containing a highly concentrated odor generated from at least one of the human waste treatment equipment all and the sewage treatment equipment 2 is blown into the combustion chamber 5 of the waste incinerator 4 as air for furnace temperature control by the air blower a3.
このことにより排ガス中の臭気が熱分解されて臭気処理
がなされる。As a result, the odor in the exhaust gas is thermally decomposed and odor treatment is performed.
この排ガスを燃焼用空気として吹込まず、炉温制御用空
気として吹込むのは次の理由による。The reason why this exhaust gas is not blown in as combustion air but as furnace temperature control air is as follows.
前記高濃度臭気を含む排ガスは、多量の硫化水素H,S
を含んでいる。このためこの排ガス全ごみ処理施設の通
風系統?利用して、燃焼用空気としてごみビットの臭気
と一緒に火格子下から吹込むと、送風機や火格子、その
池焼却炉関係機器の腐食の問題が生じる。そこでこの発
明では前記排ガスを直接燃焼室5に吹込んで、腐食を防
止している。The exhaust gas containing the high concentration odor contains a large amount of hydrogen sulfide H, S.
Contains. Is this the ventilation system for this exhaust gas waste treatment facility? If the combustion air is blown from below the grate along with the odor of the waste bits, corrosion of the blower, grate, and equipment related to the pond incinerator will occur. Therefore, in this invention, the exhaust gas is directly blown into the combustion chamber 5 to prevent corrosion.
汚泥乾燥機6の排ガスについても、これをごみ焼却炉4
の燃焼室5に送風機7により炉温制御用空気として吹込
む。このこと、にエリ排ガス中の臭気が熱分解されて臭
気処理がなされる。The exhaust gas from the sludge dryer 6 is also transferred to the waste incinerator 4.
The air is blown into the combustion chamber 5 by the blower 7 as air for controlling the furnace temperature. As a result, the odor in the exhaust gas is thermally decomposed and odor treatment is performed.
この排ガスを燃焼用空気として吹込まず、炉温制御用空
気として吹込むのは次の理由による。The reason why this exhaust gas is not blown in as combustion air but as furnace temperature control air is as follows.
汚泥乾燥機排ガスの温度は約80℃であり、冷やされる
と強い酸性のドレンができる。このためこの排ガスをご
み処理施設の通風系統を利用して、燃焼用空気として火
格子下から吹込むと焼却炉機器の腐食の問題が生じる。The temperature of the sludge dryer exhaust gas is approximately 80°C, and when it is cooled, a strongly acidic drain is formed. Therefore, if this exhaust gas is blown from below the grate as combustion air using the ventilation system of the waste treatment facility, the problem of corrosion of the incinerator equipment will occur.
そこでこの排ガスを直接燃焼室5に吹込んで腐食を防止
している。Therefore, this exhaust gas is blown directly into the combustion chamber 5 to prevent corrosion.
一方前記処理装置?、2の少なくとも一方から発生する
低濃度臭気を含む排ガスは、送風機8によりチャンバ9
に導き、ごみビット10の臭気と一緒にし、これを押込
送風機11によりガス式空気予熱器12を介して火格子
下から燃焼用空気として吹込む、また一部を燃焼室5へ
炉温制御用空気として吹込む、このようにして低濃度臭
気とゴミビット臭気とを同時に脱臭処理できる。On the other hand, the processing device? , 2 containing low concentration odor is sent to a chamber 9 by a blower 8
This is combined with the odor of the waste bits 10, and is blown into combustion air from below the grate via a gas air preheater 12 by a forced air blower 11, and a portion is also sent into the combustion chamber 5 for furnace temperature control. In this way, low-concentration odors and trash bit odors can be deodorized at the same time.
低濃度臭気を燃焼空気として吹込めるのは、低濃度臭気
が高濃度臭気に比べて硫化水素H,Sが極度に少なく、
ごみ焼却炉機器の腐食の心配もないためである。The reason why low-concentration odor can be injected as combustion air is because low-concentration odor contains extremely less hydrogen sulfide H and S than high-concentration odor.
This is because there is no need to worry about corrosion of waste incinerator equipment.
なお実操業では、炉の立上げ、立下げ時及び停電時など
の炉内温度が低い時又休炉時でし尿処理のみ運転してい
る場合には、高濃度臭気及び汚泥乾燥排ガスを脱臭炉1
3に導き、熱分解によ一す脱臭を行った後大気へ放出す
る。また低濃度臭気は、活性炭I4により脱臭した後大
気へ放出する。In actual operation, when the temperature inside the furnace is low such as when the furnace is started up, shut down, or during a power outage, or when the furnace is out of operation and only human waste treatment is being performed, highly concentrated odors and sludge drying exhaust gas are removed from the deodorizing furnace. 1
3, deodorized by thermal decomposition, and then released into the atmosphere. In addition, low-concentration odors are deodorized with activated carbon I4 and then released into the atmosphere.
(発明の効果)
この発明によれば、し尿処理装置及び下水処理装置から
発生する悪臭がスを燃焼中のごみ焼却炉に吹込むことに
より低いランニングコストで熱分解して脱臭することが
できる。しかもこれら悪臭ガスのうち腐食性の強い高濃
度臭気ガスや汚泥乾燥機排ガスについては、直接燃焼室
に炉温制御用空気として吹込むのでごみ焼却炉機器の腐
食を防止することができる。(Effects of the Invention) According to the present invention, bad smells generated from human waste treatment equipment and sewage treatment equipment can be pyrolyzed and deodorized at low running costs by being blown into a burning garbage incinerator. Moreover, among these malodorous gases, highly corrosive highly concentrated malodorous gases and sludge dryer exhaust gas are directly blown into the combustion chamber as air for furnace temperature control, thereby preventing corrosion of the waste incinerator equipment.
図面は本発明の一実施例を示す悪臭ガス処理方法の説明
図である。
1・・・し尿処理装置、2・・・下水処理装置、3・・
・送風機、4・・・ごみ焼却炉、5・・・燃焼室、6・
・・汚泥乾燥機、7・・・送風機、8・・・送風機、9
−・・チャンバ、10・・・ごみビット、11・・・押
込送風機、12・・・ガス式空気予熱器、I3・・・脱
臭炉、I4・・・活性炭。The drawing is an explanatory diagram of a malodorous gas treatment method showing an embodiment of the present invention. 1... Human waste treatment equipment, 2... Sewage treatment equipment, 3...
・Blower, 4... Garbage incinerator, 5... Combustion chamber, 6.
...Sludge dryer, 7...Blower, 8...Blower, 9
-...Chamber, 10...Garbage bit, 11...Forced air blower, 12...Gas type air preheater, I3...Deodorizing furnace, I4...Activated carbon.
Claims (1)
生する高濃度臭気を含む排ガス及び汚泥乾燥機の排ガス
をごみ焼却炉の燃焼室に炉温制御用空気として吹込み、
かつ前記両処理装置の少なくとも一方から発生する低濃
度臭気を含む排ガスの一部又は全部をごみ焼却炉の火格
子から燃焼用空気として吹き込む悪臭ガス処理方法。Blowing exhaust gas containing highly concentrated odor generated from at least one of the human waste treatment equipment and the sewage treatment equipment and the exhaust gas from the sludge dryer into the combustion chamber of the garbage incinerator as air for furnace temperature control,
and a malodorous gas treatment method in which part or all of the exhaust gas containing low concentration odor generated from at least one of the two treatment devices is blown as combustion air through the grate of the garbage incinerator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18365685A JPS6246120A (en) | 1985-08-21 | 1985-08-21 | Foul odor gas treating method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18365685A JPS6246120A (en) | 1985-08-21 | 1985-08-21 | Foul odor gas treating method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6246120A true JPS6246120A (en) | 1987-02-28 |
Family
ID=16139623
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18365685A Pending JPS6246120A (en) | 1985-08-21 | 1985-08-21 | Foul odor gas treating method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6246120A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008253963A (en) * | 2007-04-09 | 2008-10-23 | Kawasaki Plant Systems Ltd | Treating method and treatment facility of waste and sewage |
JP2009045612A (en) * | 2007-07-20 | 2009-03-05 | Chugoku Electric Power Co Inc:The | Waste recycling method and recycling facility |
JP2016130623A (en) * | 2015-01-07 | 2016-07-21 | リブラン株式会社 | Log fuel combustion device, log fuel boiler system, method for supplying combustion gas using log fuel, and system for supplying electricity within region using log fuel |
RU2650018C1 (en) * | 2017-05-30 | 2018-04-06 | Федеральное государственное казенное военное образовательное учреждение высшего образования "ВОЕННАЯ АКАДЕМИЯ МАТЕРИАЛЬНО-ТЕХНИЧЕСКОГО ОБЕСПЕЧЕНИЯ имени генерала армии А.В. Хрулева" | Power plant with the active recovery boiler of the high-temperature boiling bed |
WO2023112862A1 (en) * | 2021-12-14 | 2023-06-22 | 日立造船株式会社 | Waste incineration facility |
-
1985
- 1985-08-21 JP JP18365685A patent/JPS6246120A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008253963A (en) * | 2007-04-09 | 2008-10-23 | Kawasaki Plant Systems Ltd | Treating method and treatment facility of waste and sewage |
JP2009045612A (en) * | 2007-07-20 | 2009-03-05 | Chugoku Electric Power Co Inc:The | Waste recycling method and recycling facility |
JP2016130623A (en) * | 2015-01-07 | 2016-07-21 | リブラン株式会社 | Log fuel combustion device, log fuel boiler system, method for supplying combustion gas using log fuel, and system for supplying electricity within region using log fuel |
JP2019082327A (en) * | 2015-01-07 | 2019-05-30 | リブラン株式会社 | Combustion device for log fuel, boiler system for log fuel, supply method of combustion gas using log fuel, and in-district power supply system using log fuel |
RU2650018C1 (en) * | 2017-05-30 | 2018-04-06 | Федеральное государственное казенное военное образовательное учреждение высшего образования "ВОЕННАЯ АКАДЕМИЯ МАТЕРИАЛЬНО-ТЕХНИЧЕСКОГО ОБЕСПЕЧЕНИЯ имени генерала армии А.В. Хрулева" | Power plant with the active recovery boiler of the high-temperature boiling bed |
WO2023112862A1 (en) * | 2021-12-14 | 2023-06-22 | 日立造船株式会社 | Waste incineration facility |
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