JPH07171592A - Automatic control device for inflow amount of raw water to anaerobic waste water treatment equipment - Google Patents
Automatic control device for inflow amount of raw water to anaerobic waste water treatment equipmentInfo
- Publication number
- JPH07171592A JPH07171592A JP14093991A JP14093991A JPH07171592A JP H07171592 A JPH07171592 A JP H07171592A JP 14093991 A JP14093991 A JP 14093991A JP 14093991 A JP14093991 A JP 14093991A JP H07171592 A JPH07171592 A JP H07171592A
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- Prior art keywords
- raw water
- anaerobic
- computer
- inflow
- concn
- 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.)
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- Y02W10/12—
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は嫌気性排水処理設備の流
入原水の有機物濃度の変動によっても常に安定な排水処
理を行うことのできる流入原水量自動制御装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an inflow raw water amount automatic control system capable of always performing stable wastewater treatment even if the organic matter concentration of the inflow raw water of an anaerobic wastewater treatment facility varies.
【０００２】[0002]
【従来の技術】工業用、家庭用等の有機物を含んだ排水
を処理する設備として、この排水を嫌気状態の発酵槽に
流入し、その槽で嫌気性菌による嫌気性発酵処理を行
い、有機物を分解して、主としてメタン、二酸化炭素等
のガスとして槽外に放出させる、そしてこの発酵処理が
完了した処理水は、次の空気、酸素曝気工程に導き、好
気性菌の作用により更に分解され、下水道放流水として
放出される。一方、嫌気性発酵槽で発生したメタンガス
は熱源又は有機化合物の合成原料等として使用される。
このような原水の処理法を所謂、嫌気性排水処理と云わ
れ、一般に行われている。この処理の場合、発酵槽の負
荷能力と流入原水の有機物の含有量との不整合、特に、
原水の有機物が槽の負荷能力を超える場合、原水の有機
物の嫌気性発酵が充分に行われず、安定した嫌気性発酵
処理ができなかった。2. Description of the Related Art As a facility for treating wastewater containing organic substances for industrial use, household use, etc., this wastewater is introduced into an anaerobic fermentation tank, and anaerobic fermentation treatment with anaerobic bacteria is carried out in the tank to remove organic matter. Is decomposed and released mainly as a gas such as methane and carbon dioxide to the outside of the tank, and the treated water after completion of this fermentation treatment is led to the next air and oxygen aeration step, and further decomposed by the action of aerobic bacteria. , Released as sewer discharge water. On the other hand, methane gas generated in the anaerobic fermentation tank is used as a heat source or a raw material for synthesizing organic compounds.
Such a raw water treatment method is called so-called anaerobic wastewater treatment and is generally performed. In the case of this treatment, there is a mismatch between the load capacity of the fermentor and the content of organic matter in the incoming raw water, especially,
When the organic matter in the raw water exceeds the load capacity of the tank, the anaerobic fermentation of the organic matter in the raw water was not sufficiently performed, and stable anaerobic fermentation treatment could not be performed.
【０００３】そこで、従来、この嫌気性処理設備におい
て、この処理を安定に行うため、その流入原水の有機物
濃度を手分析により行い、その結果をもとに嫌気性発酵
槽の負荷能力に適合した原水の流入量を人力により制御
していた。Therefore, conventionally, in order to perform this treatment stably in this anaerobic treatment facility, the organic matter concentration of the inflowing raw water was manually analyzed, and based on the result, it was adapted to the load capacity of the anaerobic fermentation tank. The inflow of raw water was controlled manually.
【０００４】[0004]
【発明が解決しようとする課題】上述の従来の嫌気性排
水処理設備への流入原水量の分析、流水量の制御等全て
が手動で行うため、その操作に時間と手間が掛るばかり
でなく、経時的な有機物濃度を的確に把握することが難
しくて、嫌気性排水処理槽の負荷と流入原水の有機物濃
度が常に適合した状態で嫌気性処理を行うことができな
かった。よって、この設備から流出する排出水の有機物
の含量が不安定になり、次の曝気処理が不安定となる欠
陥があった。The above-mentioned conventional analysis of the amount of raw water flowing into the anaerobic wastewater treatment facility, control of the amount of flowing water, etc. are all carried out manually, so not only the operation takes time and labor, but also Since it was difficult to accurately grasp the organic matter concentration over time, it was not possible to perform anaerobic treatment in a state where the load of the anaerobic wastewater treatment tank and the organic matter concentration of the inflowing raw water always matched. Therefore, the organic matter content of the discharged water flowing out from this equipment becomes unstable, and there is a defect that the next aeration process becomes unstable.
【０００５】[0005]
【課題を解決するための手段】本発明者は上記の欠陥を
解決するため鋭意研究の結果、嫌気性処理槽による発生
ガス量が原水の有機物濃度に深く関係し、この発生ガス
量から有機物濃度を算出し、嫌気性排水設備への負荷の
高低を分析して流入する原水量を自動的に調節すること
により前記課題を解決した。Means for Solving the Problems As a result of intensive research for solving the above-mentioned defects, the present inventor has found that the amount of gas generated by an anaerobic treatment tank is deeply related to the organic concentration of raw water. The above-mentioned problems were solved by calculating the above, analyzing the level of the load on the anaerobic drainage system, and automatically adjusting the amount of raw water flowing in.
【０００６】本発明は嫌気性排水処理設備において、原
水ＣＯＤｃｒ濃度測定値、メタンガス濃度測定値及び発
生ガス量測定値をコンピュータに入力して全データを分
析して原水量を自動制御する嫌気性排水処理設備への原
水自動制御装置である。The present invention relates to an anaerobic wastewater treatment facility in which raw water CODcr concentration measurement values, methane gas concentration measurement values and generated gas amount measurement values are input to a computer, all data are analyzed, and the raw water amount is automatically controlled. It is an automatic control device for raw water to the treatment equipment.
【０００７】本発明の嫌気性排水処理設備において、原
水は流量調節ポンプ、流量調節弁等の流量調節装置を設
けた導管により嫌気性発酵槽に送られる。この槽で嫌気
状態で嫌気性発酵が行われ、原水に含有されている有機
物が嫌気性菌により分解されガス体が生成する。この嫌
気性発酵により発生するガスはメタンガス及び二酸化炭
素を主体とするものである。このようにこの発酵処理が
完了した原水は、発酵槽から導管により取り出され、次
の曝気工程に移送される。一方、嫌気性発酵槽から発生
したメタン、二酸化炭素等のガス体は発酵槽の上部より
導管により取り出されガス溜に収集され、燃料又は合成
原料とされる。この導管中にメタンガス濃度計並びにガ
ス流量計が設けられている。In the anaerobic wastewater treatment facility of the present invention, raw water is sent to the anaerobic fermentation tank by a conduit provided with a flow rate control device such as a flow rate control pump and a flow rate control valve. Anaerobic fermentation is performed in this tank in an anaerobic state, and the organic matter contained in the raw water is decomposed by anaerobic bacteria to produce a gas body. The gas generated by this anaerobic fermentation is mainly methane gas and carbon dioxide. In this way, the raw water which has been subjected to this fermentation treatment is taken out of the fermenter by a conduit and transferred to the next aeration step. On the other hand, gas bodies such as methane and carbon dioxide generated from the anaerobic fermentation tank are taken out from the upper part of the fermentation tank by a conduit and collected in a gas reservoir to be used as fuel or synthetic raw material. A methane gas concentration meter and a gas flow meter are provided in this conduit.
【０００８】本発明の特徴は、前述の嫌気性排水処理設
備において、メタンガス濃度計により測定された値と、
ガス流量計により測定された値並びに原水ＣＯＤｃｒ濃
度測定値をコンピュータに入力し、次の計算式により原
水の発酵槽への量を調整する装置を自動的に作動して、
発酵槽の負荷に適合する原水量を発酵槽に供給するもの
である。発酵槽負荷に適合した原水流量の計算式は次の
通りである。従って、流入原水量は、〔式１〕で求めら
れる。The feature of the present invention is that, in the above-mentioned anaerobic wastewater treatment facility, a value measured by a methane gas concentration meter,
Input the value measured by the gas flow meter and the raw water CODcr concentration measurement value into the computer, and automatically operate the device that adjusts the amount of raw water to the fermenter according to the following formula:
The amount of raw water suitable for the load on the fermenter is supplied to the fermenter. The calculation formula of the raw water flow rate that is suitable for the fermenter load is as follows. Therefore, the inflow raw water amount is calculated by [Equation 1].
【式１】 なお、ガス化率は「用水と廃水」第30巻第12号、28頁19
88年に基づき、実績に応じて求めることができる。[Formula 1] The gasification rate is “Water and Wastewater” Vol. 30, No. 12, page 28 19
Based on 1988, it can be determined according to actual results.
【０００９】[0009]
【実施例】図１は本発明の嫌気性排水処理設備への流入
原水量自動制御装置の一実施例を示すブロック図であ
る。１は嫌気性発酵槽、２はガス溜、３は流入原水調整
槽、４は処理原水調整槽、５はガスボイラー、６は流水
量調節ポンプ、７は原水ＣＯＤｃｒ濃度入力コンピュー
タ、Ａ，Ｂ，Ｃ，Ｄ，Ｅ，Ｆはそれぞれ導管を示す。FIG. 1 is a block diagram showing an embodiment of an automatic control apparatus for the amount of raw water flowing into an anaerobic wastewater treatment facility according to the present invention. 1 is an anaerobic fermentation tank, 2 is a gas reservoir, 3 is an inflow raw water adjusting tank, 4 is a treated raw water adjusting tank, 5 is a gas boiler, 6 is a flow rate adjusting pump, 7 is a raw water CODcr concentration input computer, A, B, C, D, E, and F indicate conduits, respectively.
【００１０】本図において、流入原水を導管Ａを通し
て、流入原水調整槽３（1000ｍ3）に導入し、更にこの
調整槽３から導管Ｂを通して嫌気性発酵槽１（150ｍ3）
に導入する。この嫌気性発酵槽１で嫌気性発酵が行わ
れ、メタンと二酸化炭素が60：40の割合で発生する。こ
のガスを導管Ｃを通してガス溜２に導入し、このメタン
ガスは導管Ｄを通してメタンガスボイラー５，５に導入
し、燃料とする。一方、嫌気性発酵槽１で有機物を分解
された原水は導管Ｅを通して処理水調整槽４（2800
ｍ3）に導入し、後曝気工程に移す。この設備におい
て、導管Ｄに設けられているメタンガス濃度計並びに発
生ガス流量計により測定されたメタンガス濃度（％）及
びガス流量（Ｎｍ3/Ｄ）の値をそれぞれ予め算出された
ガス化率を入力しておいたコンピュータ９に入力し、一
方手分析で測定された原水ＣＯＤｃｒ濃度（ＣＯＤから
得られた有機物の濃度、mg/ｌ）が入力されているコン
ピュータ10からの値をコンピュータ９に入力して、前記
の演算により流入原水量（ｍ3/Ｄ）を算出し、これによ
り流水量調節ポンプ６を制御する。コンピュータ６への
入力、出力は点線で示した。[0010] In the figure, the inflow raw water through conduit A, was introduced into the inflow raw water regulating tank 3 (1000 m 3), further anaerobic fermentation tank 1 from the adjustment tank 3 through a conduit B (150 meters 3)
To introduce. Anaerobic fermentation is performed in this anaerobic fermentation tank 1, and methane and carbon dioxide are generated at a ratio of 60:40. This gas is introduced into the gas reservoir 2 through the conduit C, and this methane gas is introduced into the methane gas boilers 5 and 5 through the conduit D and used as fuel. On the other hand, the raw water from which the organic matter was decomposed in the anaerobic fermentation tank 1 is passed through the conduit E to the treated water adjusting tank 4 (2800
m 3 ) and transfer to the post-aeration step. In this equipment, input the gasification rate calculated in advance for the values of methane gas concentration (%) and gas flow rate (Nm 3 / D) measured by the methane gas concentration meter installed in the conduit D and the generated gas flow meter. The raw water CODcr concentration (concentration of organic matter obtained from COD, mg / l) measured by one-handed analysis is input to the computer 9, and the value from the computer 10 is input to the computer 9. Then, the inflow raw water amount (m 3 / D) is calculated by the above calculation, and the running water amount adjusting pump 6 is controlled by this. Input and output to the computer 6 are shown by dotted lines.
【００１１】以上のように、本願発明は発酵槽の負荷、
流入原水の有機物の濃度に適合して自動的に流入原水の
発酵槽に流入する水量を制御することが可能となり、常
に発酵槽の最大の負荷状態で嫌気性排水処理設備が稼働
される。As described above, according to the present invention, the load on the fermenter is
It becomes possible to automatically control the amount of water flowing into the fermenter of the inflow raw water according to the concentration of organic matter in the inflow raw water, and the anaerobic wastewater treatment facility is always operated under the maximum load condition of the fermenter.
【００１２】[0012]
【作用】本発明はガス溜から導出されるガスをメタンガ
ス濃度計でメタンガス濃度値及び発生ガス流量計で発生
ガス量値を測定し、これをコンピュータに入力し、又原
水ＣＯＤｃｒ濃度値を同コンピュータに入力して前述の
計算を行い、この結果を流入原水調整装置に指令してそ
の流量を計算値に適合するよう流入原水量を調整する。
このことによって、発酵槽の負荷に適合する有機物を含
有する原水の供給を自動的に管理する。According to the present invention, the methane gas concentration meter measures the methane gas concentration value of the gas discharged from the gas reservoir and the generated gas flow rate meter measures the generated gas amount value, and inputs this to a computer, and the raw water CODcr concentration value is also measured by the computer. To the inflow raw water adjusting device to adjust the flow rate to the calculated value.
This automatically controls the feed of raw water containing organic matter that is compatible with the fermenter load.
【００１３】[0013]
【発明の効果】以上述べたとおり、本発明は嫌気性排水
処理設備において、原水の流入量を原水中の有機物含量
が発酵槽の負荷に適合した量に自動的に制御することに
よって、常に安定した処理排水を次の工程に供給するこ
とができると同時に、常に発酵槽の最大負荷で発酵でき
効率がよい実用上極めて有用な発明である。As described above, according to the present invention, in an anaerobic wastewater treatment facility, the inflow rate of raw water is automatically controlled so that the content of organic matter in the raw water is suitable for the load of the fermenter, so that it is always stable. The treated wastewater can be supplied to the next step, and at the same time, it can be fermented at the maximum load of the fermenter at all times and is highly efficient and is a very useful invention.
【図１】本発明の一実施例を示すブロック図である。FIG. 1 is a block diagram showing an embodiment of the present invention.
１ 嫌気性発酵層 ２ ガス溜 ３ 流入原水調整槽 ４ 処理原水調整槽 ５ ガスボイラー ６ 流水量調整ポンプ ７ メタンガス濃度計 ８ 発生ガス流量計 ９ コンピュータ 10 原水ＣＯＤｃｒ濃度入力コンピュータ Ａ，Ｂ，Ｃ，Ｄ，Ｅ，Ｆ 導管 1 Anaerobic fermentation layer 2 Gas reservoir 3 Inflow raw water adjusting tank 4 Treatment raw water adjusting tank 5 Gas boiler 6 Flow rate adjusting pump 7 Methane gas concentration meter 8 Evolved gas flow meter 9 Computer 10 Raw water CODcr concentration input computer A, B, C, D , E, F conduit
Claims (1)
Ｄｃｒ濃度測定値、メタンガス濃度測定値及び発生ガス
量測定値をガス化率を予め入れておいたコンピュータに
入力して全データを分析して流入原水量を自動制御する
ことを特徴とする嫌気性排水処理設備への原水自動制御
装置。1. In an anaerobic wastewater treatment facility, raw water CO
Anaerobic characteristics characterized by inputting Dcr concentration measurement value, methane gas concentration measurement value and generated gas amount measurement value into a computer in which the gasification rate has been entered in advance and analyzing all data to automatically control the inflowing raw water amount. Automatic raw water control system for wastewater treatment facilities.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14093991A JP2557575B2 (en) | 1991-05-16 | 1991-05-16 | Automatic controller for raw water flow into anaerobic wastewater treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14093991A JP2557575B2 (en) | 1991-05-16 | 1991-05-16 | Automatic controller for raw water flow into anaerobic wastewater treatment facility |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07171592A true JPH07171592A (en) | 1995-07-11 |
| JP2557575B2 JP2557575B2 (en) | 1996-11-27 |
Family
ID=15280332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14093991A Expired - Lifetime JP2557575B2 (en) | 1991-05-16 | 1991-05-16 | Automatic controller for raw water flow into anaerobic wastewater treatment facility |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2557575B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997012840A1 (en) * | 1995-10-04 | 1997-04-10 | Institut National De La Recherche Agronomique | Method and device for controlling a device for purifying waste water |
| JPH10230289A (en) * | 1997-02-20 | 1998-09-02 | Kurita Water Ind Ltd | Anaerobic treatment |
| US6663777B2 (en) * | 2002-03-12 | 2003-12-16 | Keith A. Schimel | Apparatus, system, and process for anaerobic conversion of biomass slurry to energy |
| JP2006026461A (en) * | 2004-07-12 | 2006-02-02 | Toray Ind Inc | Method and apparatus for controlling anaerobic water treatment plant generating methane gas |
| JP2007090168A (en) * | 2005-09-27 | 2007-04-12 | Sumitomo Heavy Ind Ltd | Anaerobic treatment apparatus and anaerobic treatment method |
| JP2007229549A (en) * | 2006-02-27 | 2007-09-13 | Sumitomo Heavy Ind Ltd | Control system and control method for waste water treatment |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59225796A (en) * | 1983-05-23 | 1984-12-18 | ヘキスト・セラニーズ・コーポレーション | Control for anaerobic reactor |
-
1991
- 1991-05-16 JP JP14093991A patent/JP2557575B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59225796A (en) * | 1983-05-23 | 1984-12-18 | ヘキスト・セラニーズ・コーポレーション | Control for anaerobic reactor |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1997012840A1 (en) * | 1995-10-04 | 1997-04-10 | Institut National De La Recherche Agronomique | Method and device for controlling a device for purifying waste water |
| FR2739615A1 (en) * | 1995-10-04 | 1997-04-11 | Agronomique Inst Nat Rech | METHOD FOR CONTROLLING A WASTEWATER CLEANING DEVICE AND CORRESPONDING DEVICE |
| JPH10230289A (en) * | 1997-02-20 | 1998-09-02 | Kurita Water Ind Ltd | Anaerobic treatment |
| US6663777B2 (en) * | 2002-03-12 | 2003-12-16 | Keith A. Schimel | Apparatus, system, and process for anaerobic conversion of biomass slurry to energy |
| JP2006026461A (en) * | 2004-07-12 | 2006-02-02 | Toray Ind Inc | Method and apparatus for controlling anaerobic water treatment plant generating methane gas |
| JP2007090168A (en) * | 2005-09-27 | 2007-04-12 | Sumitomo Heavy Ind Ltd | Anaerobic treatment apparatus and anaerobic treatment method |
| JP2007229549A (en) * | 2006-02-27 | 2007-09-13 | Sumitomo Heavy Ind Ltd | Control system and control method for waste water treatment |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2557575B2 (en) | 1996-11-27 |
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Legal Events
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| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19960723 |