JPS5888095A - Treatment of exhaust gas from fermenting vat - Google Patents
Treatment of exhaust gas from fermenting vatInfo
- Publication number
- JPS5888095A JPS5888095A JP56185163A JP18516381A JPS5888095A JP S5888095 A JPS5888095 A JP S5888095A JP 56185163 A JP56185163 A JP 56185163A JP 18516381 A JP18516381 A JP 18516381A JP S5888095 A JPS5888095 A JP S5888095A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- aerating
- sludge
- treatment
- gas
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は発酵槽内において発生する排ガスの処理方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating exhaust gas generated within a fermenter.
一般に汚泥をコンポスト化するときは、発酵槽内に悪臭
成分を含んだ排ガスが発生するが、この排ガス中には5
00〜110007)pのアンモニアヤ0.1〜12P
711ツメチルメルカプタン、0.5−5−57F硫化
メチル等の悪臭成分が含まれているため、これをそのま
ま大気に放出することはできない。そこで従来はこの排
ガスを水洗したり酸洗浄やアルカリ洗浄、塩素処理、活
性炭処理尋を適宜組合せて脱臭処理していたが脱果処理
のための設備費中ランニングコストがかかり丁ぎてコス
トがアップする原因となっていた。Generally, when sludge is composted, exhaust gas containing malodorous components is generated in the fermenter, but this exhaust gas contains 5
00~110007) p ammonia 0.1~12P
Since it contains malodorous components such as 711-methyl mercaptan and 0.5-5-57F methyl sulfide, it cannot be released into the atmosphere as it is. Conventionally, this exhaust gas has been deodorized by washing with water, acid washing, alkaline washing, chlorine treatment, and activated carbon treatment, but this increases the running cost of the equipment cost for removing fruit. It was causing this.
本発明は、上記従来の欠点に鑑み提案されたもので、汚
泥をコンポスト化するときに、発酵槽内で発生する悪臭
成分を含んだ排ガス中には、酸素が10〜19%も含ま
れている点KN目し、この排ガスを隣接する曝気IK導
いて、活性汚泥処理用の曝気ガスとして利用するように
した点に%徴があり、脱臭処理のための特別な設備を%
に必要とせすに、排ガスの有効利用と効果的な脱臭を行
なうことができる、発酵槽の排ガス処理方法を提供しよ
うとするものである。The present invention was proposed in view of the above-mentioned conventional drawbacks, and when sludge is composted, the exhaust gas containing malodorous components generated in the fermenter contains 10 to 19% oxygen. The key point is that this exhaust gas is led to the adjacent aeration IK and used as aeration gas for activated sludge treatment, and special equipment for deodorization treatment is installed.
The purpose of the present invention is to provide a method for treating exhaust gas from a fermenter, which enables effective use of exhaust gas and effective deodorization.
以下、本発明の実施例を図面を参照して説明する。Embodiments of the present invention will be described below with reference to the drawings.
第1図は本発明に係る発酵槽の排ガス処理方法の1実施
例を示すプロセス説明図である。図中1は発酵槽で、そ
の内部は上部発酵室と上部発酵室とに区画され、各発酵
室にはコンポスト化される汚泥が収容されており、各発
酵室には発酵用の空気を供給するためのファン2及び配
管3が設けられている。4は一端が各発酵室に連通し、
他端が曝気槽5の底部に開口した抽出管で、その途中に
はブロワ6が設置され、抽出管4の先端は曝気槽5中に
開口されている。なお図中7は曝気槽5に供給される原
水、8は排出される処理水を示したものである。FIG. 1 is a process explanatory diagram showing one embodiment of the fermenter exhaust gas treatment method according to the present invention. In the figure, 1 is a fermentation tank, the inside of which is divided into an upper fermentation chamber and an upper fermentation chamber, each fermentation chamber contains sludge to be composted, and each fermentation chamber is supplied with air for fermentation. A fan 2 and piping 3 are provided for this purpose. 4 has one end communicating with each fermentation chamber,
The other end of the extraction pipe is an extraction pipe that opens at the bottom of the aeration tank 5 , a blower 6 is installed in the middle of the extraction pipe, and the tip of the extraction pipe 4 opens into the aeration tank 5 . In the figure, 7 indicates raw water supplied to the aeration tank 5, and 8 indicates treated water to be discharged.
上記プロセスよりなる本発明においては、ブロワ6を駆
動すると、発酵槽1の各発酵室内に発生した悪果成分を
含んだ排ガスは、抽出管4を介して抽出され、曝気槽5
に導かれることKなる。曝気槽5に導かれた排ガス中に
は、発酵室に供給された発酵用の空気が混合し、酸素が
10〜19%も含まれており、この排ガスを抽出管40
−口端より曝気槽5の底部に噴出させると、排ガス中の
残存酸素が原水7中の有機物を酸化処理するために必要
な酸素として有効に利用されると共に、曝気槽5の底部
K11Jt出された排ガスは、曝気槽5内の活性汚泥を
均一かつ適度な濃度に懸濁させ、好気性の状態が維持さ
れるよう曝気槽5内を攪拌することになって、活性汚泥
処理用の曝気ガスとして有効に利用されることになる。In the present invention comprising the above process, when the blower 6 is driven, the exhaust gas containing bad fruit components generated in each fermentation chamber of the fermenter 1 is extracted via the extraction pipe 4, and the aeration tank 5
It is important to be guided by. The exhaust gas led to the aeration tank 5 is mixed with the fermentation air supplied to the fermentation chamber and contains 10 to 19% oxygen, and this exhaust gas is passed through the extraction pipe 40.
- By blowing out from the mouth end to the bottom of the aeration tank 5, the residual oxygen in the exhaust gas is effectively used as oxygen necessary for oxidizing the organic matter in the raw water 7, and the oxygen is discharged from the bottom of the aeration tank 5. The waste gas is used to suspend the activated sludge in the aeration tank 5 to a uniform and appropriate concentration, and to stir the inside of the aeration tank 5 to maintain an aerobic state. It will be effectively used as
また、悪臭の主原因であった、排ガス中に多量に含まれ
るアンモニアは、曝気作用によって原水7中に攪拌混合
される間に吸収され、60−90%程度まで有効に除去
することができることKなる。In addition, the ammonia contained in large amounts in the exhaust gas, which was the main cause of bad odors, is absorbed while being stirred and mixed into the raw water 7 by aeration, and can be effectively removed to the extent of 60-90%. Become.
第2図は、曝気槽5への排ガス導入位置を変えた他の実
施例を示したものである。一般に曝気槽5の原水7供給
側は、BOI)負荷量が高く、多量の酸素を必要とする
ので、この個所には別途設けた空気供給管9がら空気を
供給して曝気し、発酵室1から抽気した排ガスはBOD
負荷量が低い処理水8の出口側に対し抽出管4を介して
噴出させて曝気するようにしたものである。FIG. 2 shows another embodiment in which the position at which exhaust gas is introduced into the aeration tank 5 is changed. Generally, the raw water 7 supply side of the aeration tank 5 has a high BOI load and requires a large amount of oxygen. The exhaust gas extracted from the BOD
Aeration is ejected through the extraction pipe 4 to the outlet side of the treated water 8 where the load is low.
第5図は、曝気槽へ導く排ガスの濃度制御を行なえるよ
うにした実施例を示したものである。一般に発酵室内の
排ガスは、コンポスト化する汚泥の性状や発酵状態に応
じて排ガスの発生量や発生した排ガス中の酸素濃度等が
変化するため、抽出管4を流れる排ガス中の酸素又は炭
酸ガスの濃度を濃度測定器10によって測定し、炭酸ガ
ス濃度が高く酸素濃度が低すき゛る場合には、空気供給
管9より空気を取入れて排ガスと混合し、酸素濃度を所
定値まで高めた上でブロワ6により曝気槽へ供給するの
である。なお、図中1112は各々流量を調節するため
の制御弁であって、濃度測定器10の測定値に応じて手
動又は自動的に開閉操作されるようになっている。FIG. 5 shows an embodiment in which the concentration of exhaust gas introduced into the aeration tank can be controlled. In general, the amount of exhaust gas generated in the exhaust gas in the fermentation chamber and the oxygen concentration in the generated exhaust gas change depending on the properties of the sludge to be composted and the fermentation state. The concentration is measured by the concentration measuring device 10, and if the carbon dioxide concentration is high and the oxygen concentration is low, air is taken in from the air supply pipe 9 and mixed with the exhaust gas to increase the oxygen concentration to a predetermined value, and then the blower 6 The water is supplied to the aeration tank. In the figure, reference numeral 1112 indicates a control valve for adjusting the flow rate, which is opened and closed manually or automatically according to the measured value of the concentration measuring device 10.
第4図は本発明の排ガス処理方法に脱臭処理を組込んだ
実施例を示したものである。コンポスト化する汚泥の性
状等によっては、発#室内で発生した排ガスをブロワ6
によって抽出管4の開口端から曝気槽5内に導入しただ
けでは、排ガス中の悪臭成分を十分に除去し得ないこと
もある。その場合には、曝気槽5の上面に蓋をして密閉
し、曝気槽5内のガスを配管16を介して酸洗浄工程1
4及び活性炭処理工程15等へ導き、悪臭成分を完全に
除去すればよい。このように別途脱臭処理工程を設ける
場合でも、排ガスを曝気槽5内に曝気させることは、脱
臭の前処理としてきわめて有効であることはいうまでも
ない2゜
第5図は本発明を深層曝気槽に適用した場合の実施例を
示したものである。図中16は深層曝気槽で、下降流室
17の上端より供給された原水7は、下降流室17を下
降して下端より上昇流室18を上昇し、処理水8として
排出されるが、上昇流室18の上部の処理水の一部は、
ポンプ19によって汲上けられ、返送管20を経て再び
下降流室17の上端に返送され、再循環されるようにな
っている。そして、発#呈内に発生した排ガスは、抽出
管4の開口端よりプロ76により下降流室17の上端の
原水中に曝気ガスとして噴出されるが、噴出された排ガ
スは原水と共に下降流室17及び上昇流室18中を乱流
効果により混合されながら長時間原水と接触したまf流
動することになる。このように深層曝気槽16において
は第1図に示すタイプの曝気槽5と比較して排ガスと原
水7との接触時間が長時間、例えば5〜10分間もとる
ことができるので、排ガス中の悪臭の主原因となってい
るアンモニアを70〜95チも除去することができ、き
わめて効果的である。なお、図示の実施例においては、
深層曝気僧16の曝気ガスとして発酵室内で発生する排
ガスのみを用いているが、第6図に示すように排ガス中
に空気を混入して酸素濃度を調節したものを曝気ガスと
して用いてもよい。FIG. 4 shows an embodiment in which deodorizing treatment is incorporated into the exhaust gas treatment method of the present invention. Depending on the properties of the sludge to be composted, the exhaust gas generated in the # generation chamber may be transferred to the blower 6.
Therefore, it may not be possible to sufficiently remove malodorous components in the exhaust gas simply by introducing the exhaust gas into the aeration tank 5 through the open end of the extraction pipe 4. In that case, the top surface of the aeration tank 5 is covered and sealed, and the gas in the aeration tank 5 is passed through the pipe 16 to the acid cleaning step 1.
4 and activated carbon treatment step 15, etc., to completely remove malodorous components. Even when a separate deodorization process is provided in this way, it goes without saying that aerating the exhaust gas into the aeration tank 5 is extremely effective as a pretreatment for deodorization. This shows an example in which the present invention is applied to a tank. In the figure, 16 is a deep aeration tank, and the raw water 7 supplied from the upper end of the downflow chamber 17 descends through the downflow chamber 17 and rises through the upflow chamber 18 from the lower end, and is discharged as treated water 8. A part of the treated water in the upper part of the upflow chamber 18 is
It is pumped up by the pump 19, returned to the upper end of the downflow chamber 17 via the return pipe 20, and recirculated. Then, the exhaust gas generated in the extraction tube 4 is ejected as aeration gas from the open end of the extraction pipe 4 into the raw water at the upper end of the downflow chamber 17 by the professional 76, but the ejected exhaust gas is discharged into the downflow chamber along with the raw water. 17 and the upward flow chamber 18 while being mixed by the turbulence effect and flowing while remaining in contact with the raw water for a long time. In this way, in the deep aeration tank 16, compared to the aeration tank 5 of the type shown in FIG. It is extremely effective as it can remove 70 to 95 tons of ammonia, which is the main cause of bad odors. In addition, in the illustrated embodiment,
Although only the exhaust gas generated in the fermentation chamber is used as the aeration gas in the deep aeration chamber 16, it is also possible to mix air into the exhaust gas to adjust the oxygen concentration and use it as the aeration gas, as shown in Figure 6. .
以上具体的に説明したように、本発明は汚泥をコンポス
ト化するときに発#槽内で発生する悪臭成分を含んだ排
ガスを抽気し、それを活性汚泥処理用の曝気ガスとして
曝気槽に導くようKしたので、酸素の残存する排ガスを
曝気ガスとして有効に利用することができると共に、排
ガス中の悪臭成分をも効果的に除去し得る利点がある。As specifically explained above, the present invention extracts the exhaust gas containing malodorous components generated in the generation tank when composting sludge, and guides it to the aeration tank as aeration gas for activated sludge treatment. This has the advantage that the exhaust gas in which oxygen remains can be effectively used as an aeration gas, and that malodorous components in the exhaust gas can also be effectively removed.
また、一般に汚泥をコンポスト化する発酵槽と活性汚泥
処理を行なう曝気槽とは則−汚泥処理施設の敷地内に隣
接して設置されることが多いから、発酵槽内の排ガスを
曝気槽に導くための配管等の施設はきわめて簡単である
と共に1排ガスの脱臭処理設備費を大幅に削減すること
ができる等多くの利点を有するものである。In addition, there is a general rule that there is a difference between a fermenter for composting sludge and an aeration tank for activated sludge treatment.Since they are often installed adjacent to the premises of a sludge treatment facility, the exhaust gas in the fermenter is guided to the aeration tank. The piping and other facilities for this process are extremely simple and have many advantages, such as the ability to significantly reduce the cost of deodorizing equipment for one exhaust gas.
第1図は本発明に係る発酵槽の排ガス処理方法の1実施
例を示すプロセス説明図、第2図は排ガスによる曝気位
置を変えた他の実施例を示すプロセス説明図、第3図は
曝気槽へ導く排ガスの濃度制御プロセス説明図、第4図
は本発明の排ガス処理方法に脱臭処理を組込んだ処理プ
ロセス説明図、第5図は本発明を深層曝気槽に適用した
場合のプロセス説明図である。
1・・・立型発酵槽、2・・・ファン、3・・・配管、
4・・・抽出管、5・・・曝気槽、6・・・プロワ、7
・・・原水、8・・・処理水、9・・・空気供給管、1
0・・・濃度測定器、11・・制御弁、12・・・制御
弁、13・・・配管、14・・・酸洗浄工程、15・・
・活性炭処理工程、16深層曝気槽、17・・・下降流
室、18・・・上昇流室、19・・・ポンプ、20・・
・返送管Fig. 1 is a process explanatory diagram showing one embodiment of the fermenter exhaust gas treatment method according to the present invention, Fig. 2 is a process explanatory diagram showing another embodiment in which the aeration position by flue gas is changed, and Fig. 3 is an aeration diagram. Fig. 4 is an explanatory diagram of the process for controlling the concentration of exhaust gas led to the tank, Fig. 4 is an explanatory diagram of the treatment process incorporating deodorization processing into the exhaust gas treatment method of the present invention, and Fig. 5 is an explanation of the process when the present invention is applied to a deep aeration tank. It is a diagram. 1... Vertical fermentation tank, 2... Fan, 3... Piping,
4...Extraction pipe, 5...Aeration tank, 6...Prower, 7
... Raw water, 8... Treated water, 9... Air supply pipe, 1
0... Concentration measuring device, 11... Control valve, 12... Control valve, 13... Piping, 14... Acid cleaning process, 15...
・Activated carbon treatment process, 16 Deep aeration tank, 17...Downflow chamber, 18...Upflow chamber, 19...Pump, 20...
・Return pipe
Claims (1)
成分を含んだ排ガスを抽気し、それを活性汚泥処理用の
曝気ガスとして曝気槽に導くようにしたことを特徴とす
る発酵槽の排ガス処理方法。Exhaust gas treatment for a fermenter, characterized in that exhaust gas containing malodorous components generated in the fermenter when composting sludge is extracted, and the gas is led to the aeration tank as aeration gas for activated sludge treatment. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56185163A JPS5888095A (en) | 1981-11-20 | 1981-11-20 | Treatment of exhaust gas from fermenting vat |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56185163A JPS5888095A (en) | 1981-11-20 | 1981-11-20 | Treatment of exhaust gas from fermenting vat |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5888095A true JPS5888095A (en) | 1983-05-26 |
Family
ID=16165926
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56185163A Pending JPS5888095A (en) | 1981-11-20 | 1981-11-20 | Treatment of exhaust gas from fermenting vat |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5888095A (en) |
-
1981
- 1981-11-20 JP JP56185163A patent/JPS5888095A/en active Pending
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