JPH0713497U - Wastewater treatment equipment - Google Patents

Wastewater treatment equipment

Info

Publication number
JPH0713497U
JPH0713497U JP4441193U JP4441193U JPH0713497U JP H0713497 U JPH0713497 U JP H0713497U JP 4441193 U JP4441193 U JP 4441193U JP 4441193 U JP4441193 U JP 4441193U JP H0713497 U JPH0713497 U JP H0713497U
Authority
JP
Japan
Prior art keywords
tank
biological treatment
wastewater
treatment tank
adjusting tank
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.)
Granted
Application number
JP4441193U
Other languages
Japanese (ja)
Other versions
JP2600023Y2 (en
Inventor
清之 北野
肇 田辺
規夫 前田
正己 山本
勇次 鈴木
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.)
Komatsu Ltd
Original Assignee
Komatsu Ltd
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 Komatsu Ltd filed Critical Komatsu Ltd
Priority to JP4441193U priority Critical patent/JP2600023Y2/en
Publication of JPH0713497U publication Critical patent/JPH0713497U/en
Application granted granted Critical
Publication of JP2600023Y2 publication Critical patent/JP2600023Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Biological Wastes In General (AREA)
  • Activated Sludge Processes (AREA)

Abstract

(57)【要約】 【目的】 アルカリ性有機排水を設置面積が比較的小さ
くしてすみ、またアルカリ性の中和を簡単な構成で、し
かも日常のメンテナンスが不要となって維持管理が容易
であり、さらにアルカリ性の中和を高い安全性でもって
行なうことができるようにする。 【構成】 槽本体1内にPH調整槽2あるいは流量調整
槽9等の前段処理槽と生物処理槽4とを前段処理槽を上
流側にして設け、この前段処理槽内に気散装置8aを設
置し、この気散装置8aを、ブロワ7aを介して生物処
理装置3の上部空間3aに接続した構成となっている。
(57) [Summary] [Purpose] Alkaline organic wastewater can be installed in a relatively small installation area, and alkaline neutralization can be done easily, and maintenance is easy because daily maintenance is unnecessary. Furthermore, the neutralization of alkalinity can be performed with high safety. [Structure] A pretreatment tank such as a pH adjusting tank 2 or a flow rate adjusting tank 9 and a biological treatment tank 4 are provided in the tank main body 1 with the pretreatment tank upstream, and an air diffuser 8a is provided in the pretreatment tank. The air diffuser 8a is installed and connected to the upper space 3a of the biological treatment apparatus 3 via a blower 7a.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、搾乳ライン洗浄水、飲料水製造ライン、食品洗瓶ライン等から排出 されるアルカリ性有機排水を浄化するための排水処理装置に関するものである。 The present invention relates to a wastewater treatment device for purifying alkaline organic wastewater discharged from milking line washing water, drinking water production line, food washing bottle line and the like.

【0002】[0002]

【従来の技術】[Prior art]

アルカリ性有機排水を活性汚泥法、接触酸化法等の生物処理法を用いて浄化す るためには、そのアルカリ性により処理微生物の活性が低下することを防止する ため、生物処理の前段でPH調整を行う必要がある。従来からの一般的な方法に は、PH調整槽、PHセンサー、PH調整器、薬品タンク、薬注ポンプを設け、 硫酸あるいは塩酸等の酸性性薬品を所定PHになるまで添加する方法がある。 また、炭酸ガスボンベを設置し、炭酸ガスをPH調整槽に導き、炭酸ガスでP Hを調整する方法もある。 In order to purify alkaline organic wastewater by using biological treatment methods such as activated sludge method and catalytic oxidation method, pH adjustment must be performed before biological treatment in order to prevent the activity of treated microorganisms from decreasing due to its alkalinity. There is a need to do. As a conventional general method, there is a method in which a pH adjusting tank, a PH sensor, a PH adjuster, a chemical tank, and a chemical injection pump are provided, and an acidic chemical such as sulfuric acid or hydrochloric acid is added until a predetermined pH is reached. There is also a method of installing a carbon dioxide gas cylinder, introducing the carbon dioxide gas into a pH adjusting tank, and adjusting the PH with the carbon dioxide gas.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

酸性薬品を使う方法では、PH調整のために前項で例示したごとく種々の装置 、機器が必要になり、PHセンサーの校正、薬品の補充等のメインテナンスを必 要とする。さらに、一般に使用する酸性薬品が劇物等であることから、使用・保 管中の危険が予測される。 炭酸ガスボンベを用いる方法でも、高圧ガスとしての安全管理と定期的なガス の補充が必要になる。 The method using an acidic chemical requires various devices and equipment for pH adjustment, as exemplified in the previous section, and requires maintenance such as calibration of the PH sensor and replenishment of chemicals. Furthermore, since the acidic chemicals that are commonly used are deleterious substances, etc., dangers during use and storage are predicted. Even with the method using a carbon dioxide gas cylinder, safety management as high-pressure gas and regular gas replenishment are required.

【0004】 本考案は上記のことにかんがみなされたもので、アルカリ性有機排水の浄化を 設置面積が比較的小さくてすみ、またアルカリ性の中和を簡単な構成で、しかも 日常のメインテナンスが不要となって維持管理が容易であり、さらにアルカリ性 中和を高い安全性で行なうことができるようにした排水浄化装置を提供すること を目的とするものである。The present invention has been made in view of the above, and requires only a relatively small installation area for the purification of alkaline organic wastewater, has a simple configuration for neutralizing alkaline, and does not require daily maintenance. It is an object of the present invention to provide a wastewater purification device that is easy to maintain and manage, and that can perform alkaline neutralization with high safety.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

上記目的を達成するために、本考案に係る排水浄化装置は、槽本体1内に、P H調整槽2あるいは流量調整槽9等の前段処理槽と生物処理槽3とを前段処理槽 を上流側にして設け、この前段処理槽内に気散装置8aを設置し、この気散装置 8aを、ブロワ7aを介して生物処理装置3の上部空間3aに接続した構成とな っている。 In order to achieve the above-mentioned object, the wastewater purifying apparatus according to the present invention includes a pretreatment tank such as a pH adjusting tank 2 or a flow rate adjusting tank 9 and a biological treatment tank 3 in the tank main body 1 upstream of the pretreatment tank. The air diffuser 8a is installed inside the pretreatment tank, and the air diffuser 8a is connected to the upper space 3a of the biological treatment apparatus 3 via a blower 7a.

【0006】[0006]

【作 用】[Work]

生物処理槽3で発生した二酸化炭素を含む処理ガスが前段処理槽内の処理水中 で気散され、これにより、この処理水中のアルカリ性が中和される。 The treatment gas containing carbon dioxide generated in the biological treatment tank 3 is diffused in the treated water in the pretreatment tank, whereby the alkalinity in the treated water is neutralized.

【0007】[0007]

【実 施 例】【Example】

本考案の実施例を図面に基づいて説明する。 図1は本考案の第1実施例を示すもので、槽本体1内にPH調整槽2と生物処 理槽3とが、PH調整槽2を上流側にして設けてあり、PH調整槽2側に流入口 4が、また生物処理槽3側に流出口5が設けてあり、かつ両槽2,3は溢水壁6 にて仕切られている。 An embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a first embodiment of the present invention, in which a PH adjusting tank 2 and a biological treatment tank 3 are provided in a tank body 1 with the PH adjusting tank 2 on the upstream side. An inflow port 4 is provided on the side and an outflow port 5 is provided on the biological treatment tank 3 side, and both tanks 2 and 3 are partitioned by an overflow wall 6.

【0008】 上記両槽2,3の底部にはそれぞれブロワ7a,7bに接続した気散装置8a ,8bが設置してある。そして生物処理槽3側の気散装置8bに接続したブロワ 7bの入口側は大気に開放されているが、PH調整槽2側の気散装置8aに接続 したブロワ7aの入口側は生物処理槽3の上部空間3aに接続されている。At the bottom of both tanks 2 and 3, diffusers 8a and 8b connected to blowers 7a and 7b are installed. The inlet side of the blower 7b connected to the air diffuser 8b on the biological treatment tank 3 side is open to the atmosphere, but the inlet side of the blower 7a connected to the air diffuser 8a on the PH adjusting tank 2 side is the biological treatment tank. 3 is connected to the upper space 3a.

【0009】 上記構成において、被処理排水はPH調整槽2に流入してから溢水壁6を越え て生物処理槽3に流入し、ここで生物処理をされて流出口5より排出される。 このとき、生物処理槽3では気散装置8bよりの気泡にて曝気されると共に、 微生物による有機物の酸化、また細胞物質の合成及び酸化により、これの上部空 間3aに二酸化炭素を含む処理ガスが発生する。そしてこの処理ガスがPH調整 槽2側のブロワ7aにてPH調整槽2側の気散装置8aより気散され、このPH 調整槽2内に流入した被処理排水に接触される。In the above-mentioned configuration, the wastewater to be treated flows into the pH adjusting tank 2, then flows into the biological treatment tank 3 over the overflow wall 6, where it is biologically treated and discharged from the outlet 5. At this time, in the biological treatment tank 3, the treatment gas containing carbon dioxide in the upper space 3a of the biological treatment tank 3 is aerated by air bubbles from the aeration device 8b, and is oxidized by microorganisms to oxidize organic substances and also to synthesize and oxidize cellular substances. Occurs. Then, the treated gas is diffused by the blower 7a on the PH adjusting tank 2 side by the diffuser 8a on the PH adjusting tank 2 side, and is brought into contact with the waste water to be treated flowing into the PH adjusting tank 2.

【0010】 上記生物処理槽3で発生した処理ガスは二酸化炭素を含有していることにより 、アルカリ性の排水に溶解しやすく、この排水に溶解することにより、これのP Hを酸性側に変化して中和される。なおこのときの処理ガスの二酸化炭素の濃度 は、生物処理槽3に流入する有機物量、槽内の微生物濃度、曝気強度等から概略 予測できる。Since the treated gas generated in the biological treatment tank 3 contains carbon dioxide, it easily dissolves in alkaline wastewater, and by dissolving it in this wastewater, the pH of this is changed to the acidic side. Be neutralized. The concentration of carbon dioxide in the treated gas at this time can be roughly estimated from the amount of organic substances flowing into the biological treatment tank 3, the concentration of microorganisms in the tank, the aeration intensity, and the like.

【0011】 このとき、上記処理ガスの酸性成分が、主に弱酸である二酸化炭素であること 及びその濃度が低いことにより、長時間大量の発生ガスを中和に用いても、アル カリ性排水のPHが中性を越えて強い酸性になることはない。従って、従来技術 で必要であったPHの調整機構、すなわちPHセンサー、PH調整器が無くても PHが下がりすぎ後段の生物処理に悪影響を与えることは無い。At this time, since the acidic component of the treated gas is mainly carbon dioxide, which is a weak acid, and its concentration is low, even if a large amount of generated gas is used for neutralization for a long time, the alkaline wastewater PH does not exceed neutral and becomes strongly acidic. Therefore, even without the PH adjustment mechanism required in the prior art, that is, without the PH sensor and the PH adjuster, the PH does not drop too much and does not adversely affect the biological treatment in the subsequent stage.

【0012】 図2は本考案の第2実施例を示すもので、この実施例の第1の実施例との相違 点は生物処理槽3の上流側にPH調整槽2の代りに流量調整槽9を設けたもので ある。そして流量調整槽9には、この中の排水を生物処理槽3へ送るポンプ10 と、上記PH調整槽2と同様の気散装置8aが設置してある。 この実施例では流量調整槽9にてPH調整がなされる。FIG. 2 shows a second embodiment of the present invention. The difference between this embodiment and the first embodiment is that the flow rate adjusting tank is provided upstream of the biological treatment tank 3 instead of the PH adjusting tank 2. 9 is provided. The flow rate adjusting tank 9 is provided with a pump 10 for sending the wastewater therein to the biological treatment tank 3 and an air diffuser 8a similar to the PH adjusting tank 2 described above. In this embodiment, PH adjustment is performed in the flow rate adjusting tank 9.

【0013】 図3、図4は図1に示した第1の実施例の変形例を示すもので、図3に示すも のは、図1で示した槽本体1の下流側に補助槽11を介して多段生物処理槽12 を接続し、この多段生物処理槽12の上部空間12aがPH調整槽2側のブロワ 7aに接続されている。 この構成では途中の補助槽11に他の有機性排水が合流可能であり、この補助 槽11からより高濃度の有機性排水を流入することにより、多段生物処理槽12 での発生ガス中の二酸化炭素等の酸性ガスの濃度を高めることができ、PH調整 槽2内の中和作用をより効果的に行なうことができる 一方図4に示すものは多段生物処理槽12′が槽本体1側の生物処理槽3と直 接一体状に接続した構成となっている。FIGS. 3 and 4 show a modification of the first embodiment shown in FIG. 1. What is shown in FIG. 3 is an auxiliary tank 11 on the downstream side of the tank body 1 shown in FIG. The multi-stage biological treatment tank 12 is connected via the above, and the upper space 12a of this multi-stage biological treatment tank 12 is connected to the blower 7a on the PH adjusting tank 2 side. With this configuration, other organic wastewater can join the auxiliary tank 11 on the way, and the organic wastewater with a higher concentration can flow into the auxiliary tank 11 to cause the dioxide in the gas generated in the multi-stage biological treatment tank 12 to flow. The concentration of acidic gas such as carbon can be increased, and the neutralizing action in the pH adjusting tank 2 can be more effectively performed. On the other hand, in the one shown in FIG. It is directly connected to the biological treatment tank 3 in an integrated manner.

【0014】 図5、図6は図2に示した第2の実施例の変形例を示したもので、図5に示す ものは、図2で示した槽本体1の下流側に補助槽11を介して多段生物処理槽1 2′を接続し、この多段生物処理槽12′の上部空間12b′がPH調整槽2側 のブロワ7aに接続されている。 一方図6に示すものは多段生物処理槽12′が槽本体1側の生物処理槽3と直 接一体状に接続した構成となっている。FIGS. 5 and 6 show a modification of the second embodiment shown in FIG. 2, in which the auxiliary tank 11 is provided downstream of the tank body 1 shown in FIG. The multi-stage biological treatment tank 12 'is connected via the above, and the upper space 12b' of this multi-stage biological treatment tank 12 'is connected to the blower 7a on the PH adjusting tank 2 side. On the other hand, the structure shown in FIG. 6 has a structure in which a multi-stage biological treatment tank 12 'is directly connected to the biological treatment tank 3 on the side of the tank main body 1 in an integrated manner.

【0015】 図7、図8は図5、図6で示す装置の各部分の配置を変えたものの構成を示す ものである。 上記各実施例の装置で、搾乳ラインの洗浄排水を処理した結果、排水PHを約 10から7〜8に中和でき、その結果生物処理が順調に進行し、最終排水のBO D(生物化学的酸素要求量)は10−15ppmと良好であった。FIGS. 7 and 8 show the configuration of the apparatus shown in FIGS. 5 and 6 in which the arrangement of each part is changed. As a result of treating the washing wastewater of the milking line with the apparatus of each of the above-mentioned examples, the wastewater PH can be neutralized from about 10 to 7 to 8, and as a result, the biological treatment proceeds smoothly, and the final wastewater BOD (biochemical Oxygen demand) was as good as 10-15 ppm.

【0016】[0016]

【考案の効果】[Effect of device]

本考案によれば、アルカリ性有機排水を設置面積が比較的小さくてすみ、また アルカリ性の中和を簡単な構成で、しかも日常のメンテナンスが不要となって維 持管理が容易であり、さらにアルカリ性の中和を高い安全性で行なうことができ る。 According to the present invention, the installation area of the alkaline organic waste water is relatively small, the alkaline neutralization is simple, and the daily maintenance is not required, and the maintenance is easy. Neutralization can be performed with high safety.

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

【図1】本考案の第1の実施例を示す構成説明図であ
る。
FIG. 1 is a structural explanatory view showing a first embodiment of the present invention.

【図2】本考案の第2の実施例を示す構成説明図であ
る。
FIG. 2 is a structural explanatory view showing a second embodiment of the present invention.

【図3】本考案の第1の実施例の変形例を示す構成説明
図である。
FIG. 3 is a structural explanatory view showing a modified example of the first embodiment of the present invention.

【図4】本考案の第1の実施例の他の変形例を示す構成
説明図である。
FIG. 4 is a structural explanatory view showing another modification of the first embodiment of the present invention.

【図5】本考案の第2の実施例の変形例を示す構成説明
図である。
FIG. 5 is a structural explanatory view showing a modified example of the second embodiment of the present invention.

【図6】本考案の第2の実施例の他の変形例を示す構成
説明図である。
FIG. 6 is a structural explanatory view showing another modification of the second embodiment of the present invention.

【図7】図5で示す装置の各部分の配置を変えたものの
構成を示す平面図である。
FIG. 7 is a plan view showing a configuration of the apparatus shown in FIG. 5 in which the arrangement of each part is changed.

【図8】図6で示す装置の各部分の配置を変えたものの
構成を示す平面図である。
FIG. 8 is a plan view showing a configuration of the apparatus shown in FIG. 6 in which the arrangement of each part is changed.

【符号の説明】[Explanation of symbols]

1…槽本体、2…PH調整槽、3…生物処理槽、3a,
12a,12a′…上部空間、4…流入口、5…流出
口、6…溢水壁、7a,7b…ブロワ、8a,8b…気
散装置、9…流量調整槽、10…ポンプ、11…補助
槽、12…多段生物処理槽。
1 ... Tank main body, 2 ... PH adjusting tank, 3 ... Biological treatment tank, 3a,
12a, 12a '... Upper space, 4 ... Inlet, 5 ... Outlet, 6 ... Overflow wall, 7a, 7b ... Blower, 8a, 8b ... Vaporizer, 9 ... Flow rate adjusting tank, 10 ... Pump, 11 ... Auxiliary Tank, 12 ... Multi-stage biological treatment tank.

───────────────────────────────────────────────────── フロントページの続き (72)考案者 田辺 肇 北海道札幌市中央区北3条西1丁目2番地 大同ほくさん株式会社内 (72)考案者 前田 規夫 北海道旭川市南6条通21丁目1978番地 大 同ほくさん株式会社内 (72)考案者 山本 正己 東京都目黒区大橋1丁目6番3号 小松化 成株式会社内 (72)考案者 鈴木 勇次 千葉県市原市潤井戸2082番地 小松化成株 式会社千葉工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Hajime Tanabe Hajime Tanabe 1-chome, Kita 3-jo Nishi 1-chome, Chuo-ku, Sapporo, Hokkaido Within Daido Hokusan Co., Ltd. Daido Hokusan Co., Ltd. (72) Inventor Masami Yamamoto 1-6-3 Ohashi, Meguro-ku, Tokyo Komatsu Kasei Co., Ltd. (72) Inventor Yuji Suzuki 2082 Junwell, Ichihara-shi, Chiba Komatsu Kasei Co., Ltd. Chiba factory

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 槽本体1内に、PH調整槽2あるいは流
量調整槽9等の前段処理槽と生物処理槽3とを前段処理
槽を上流側にして設け、この前段処理槽内に気散装置8
aを設置し、この気散装置8aを、ブロワ7aを介して
生物処理装置3の上部空間3aに接続したことを特徴と
する排水処理装置。
1. A pretreatment stage such as a pH adjustment bath 2 or a flow rate adjustment bath 9 and a biological treatment bath 3 are provided in the bath main body 1 with the pretreatment stage upstream, and air is diffused in the pretreatment stage. Device 8
A wastewater treatment equipment is characterized in that a is installed and the air diffuser 8a is connected to the upper space 3a of the biological treatment equipment 3 via a blower 7a.
JP4441193U 1993-08-13 1993-08-13 Wastewater treatment equipment Expired - Fee Related JP2600023Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4441193U JP2600023Y2 (en) 1993-08-13 1993-08-13 Wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4441193U JP2600023Y2 (en) 1993-08-13 1993-08-13 Wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JPH0713497U true JPH0713497U (en) 1995-03-07
JP2600023Y2 JP2600023Y2 (en) 1999-09-27

Family

ID=12690772

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4441193U Expired - Fee Related JP2600023Y2 (en) 1993-08-13 1993-08-13 Wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JP2600023Y2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009099207A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Method and apparatus for treating nitrate waste liquid
WO2009099208A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Method and apparatus for treating radioactive nitrate waste liquid
WO2009099209A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Apparatus and method for treatment of radioactive nitrate salt liquid waste
JP2019126772A (en) * 2018-01-24 2019-08-01 オルガノ株式会社 Biological treatment apparatus, biological treatment method and regulating device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009099207A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Method and apparatus for treating nitrate waste liquid
WO2009099208A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Method and apparatus for treating radioactive nitrate waste liquid
WO2009099209A1 (en) * 2008-02-08 2009-08-13 Mitsubishi Heavy Industries, Ltd. Apparatus and method for treatment of radioactive nitrate salt liquid waste
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