JP2000218283A - Treatment of acidic organic waste water and treating device - Google Patents

Treatment of acidic organic waste water and treating device

Info

Publication number
JP2000218283A
JP2000218283A JP11020744A JP2074499A JP2000218283A JP 2000218283 A JP2000218283 A JP 2000218283A JP 11020744 A JP11020744 A JP 11020744A JP 2074499 A JP2074499 A JP 2074499A JP 2000218283 A JP2000218283 A JP 2000218283A
Authority
JP
Japan
Prior art keywords
organic wastewater
acidic organic
tank
acidic
biological treatment
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
Application number
JP11020744A
Other languages
Japanese (ja)
Inventor
Masatake Ozawa
真健 小澤
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.)
NEC Ameniplantex Ltd
Original Assignee
NEC Ameniplantex 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 NEC Ameniplantex Ltd filed Critical NEC Ameniplantex Ltd
Priority to JP11020744A priority Critical patent/JP2000218283A/en
Publication of JP2000218283A publication Critical patent/JP2000218283A/en
Pending 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)
  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a convenient treating method of acidic org. waste water which does not use a strongly basic chemical high in danger and instruments bringing about complicated administration and also to provide a treating device of the acidic org. waste water which is appropriately used at the time of treating the acidic org. waste water by this treating method. SOLUTION: In the treating method of the acidic org. waste water, the org. matter is decomposed by an organism after adjusting the pH of the acidic org. waste water by subjecting the acidic org. waste water and calcium carbonate 2 to neutralization reaction. The treating device of the acidic org. waste water is provided with a pH adjusting tank 3 for executing the pH adjustment of the acidic org. waste water and a biological treating tank 1, and the pH adjusting tank 3 has a constitution in which granular calcium carbonate 2 is stored and the supplied acidic org. waste water is allowed to overflow, and the biological treating tank 1 is a device for treating the acidic org. waste water, that the acidic org. waste water allowed to overflow from the pH adjusting tank 3 is introduced thereinto and the org. matter in acidic org. waste water is decomposed by the organism.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生ごみや生物汚泥
の乾燥凝縮水などの酸性有機廃水の処理方法および処理
装置に関し、特に、微生物などの生物が有機物を分解す
る能力を利用する酸性有機廃水の処理方法および処理装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for treating acidic organic wastewater such as garbage and dried sludge of biological sludge, and more particularly to an acidic organic wastewater utilizing the ability of organisms such as microorganisms to decompose organic substances. The present invention relates to a method and an apparatus for treating wastewater.

【0002】[0002]

【従来の技術】従来から、生ごみや生物汚泥の乾燥凝縮
水などの酸性有機廃水を処理する方法として、活性汚泥
法などの生物処理法が知られている。前記生物処理法で
は、微生物などの生物が有機物を分解する能力を利用す
るため、温度、pH、液中酸素濃度などの条件を生物が
十分に活動しうる範囲に調整する必要がある。特に、p
Hに関して言えば、多くの生物は、中性付近を至適範囲
としている。このため、生物を利用して酸性有機廃水を
処理する場合には、あらかじめpHを中性付近に調整し
ておく必要がある。
2. Description of the Related Art Hitherto, a biological treatment method such as an activated sludge method is known as a method for treating acidic organic wastewater such as garbage and dried condensed water of biological sludge. In the biological treatment method, in order to utilize the ability of an organism such as a microorganism to decompose an organic substance, it is necessary to adjust conditions such as temperature, pH, and oxygen concentration in a liquid to a range where the organism can sufficiently operate. In particular, p
As for H, most organisms have an optimal range near neutrality. For this reason, when treating acidic organic wastewater using living organisms, it is necessary to adjust the pH to near neutrality in advance.

【0003】酸性有機廃水のpHを調整するには、一般
に、水酸化ナトリウムや水酸化カルシウムなどの強塩基
性薬剤が用いられている。前記強塩基性薬剤を用いて酸
性有機廃水のpHを調整するには、有機物を微生物に分
解させる生物処理槽内、または、前記生物処理槽に供給
する酸性有機廃水のpHを調整するためのpH調整槽内
に、pH制御装置と連動するポンプを用いて強塩基性薬
剤の水溶液を供給するとともに、撹拌機などで撹拌する
方法によって行われる。
In order to adjust the pH of acidic organic wastewater, a strong basic agent such as sodium hydroxide or calcium hydroxide is generally used. To adjust the pH of the acidic organic wastewater using the strong basic agent, a biological treatment tank for decomposing organic substances into microorganisms, or a pH for adjusting the pH of the acidic organic wastewater supplied to the biological treatment tank The method is carried out by supplying an aqueous solution of the strongly basic drug into the adjustment tank using a pump linked to a pH controller and stirring the solution with a stirrer or the like.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、この方
法では、危険性の高い強塩基性薬剤を使用しているた
め、pHを調整する際に前記強塩基性薬剤の取扱いが面
倒であった。また、強塩基性薬剤を使用してpHを調整
するには、薬液タンク、薬液供給用ポンプ、pH計、p
H制御装置、撹拌機などの機器類を用いてpHを制御す
る必要があった。しかも、正確にpHの制御を行うに
は、pH計の電極の校正を定期的に行わなければならな
いなど、前記機器類の管理が必要であり、煩雑であっ
た。本発明は、前記事情に鑑みてなされたもので、上記
の問題を解決し、危険性の高い強塩基性薬剤や、煩雑な
管理を伴う機器類を使用しない簡便な酸性有機廃水の処
理方法を提供することを課題としている。また、前記処
理方法によって酸性有機廃水を処理する際に好適に使用
される酸性有機廃水の処理装置を提供することを課題と
している。
However, in this method, since a highly dangerous strong basic drug is used, handling of the strong basic drug when adjusting the pH is troublesome. To adjust the pH using a strongly basic drug, a chemical tank, a chemical supply pump, a pH meter,
It was necessary to control the pH using equipment such as an H controller and a stirrer. In addition, in order to accurately control the pH, the electrodes of the pH meter must be periodically calibrated, and the devices must be managed, which is complicated. The present invention has been made in view of the above circumstances, solves the above problems, a highly dangerous strong basic drug, and a simple method for treating acidic organic wastewater without using equipment with complicated management. The task is to provide. It is another object of the present invention to provide an acidic organic wastewater treatment apparatus suitably used when treating acidic organic wastewater by the treatment method.

【0005】[0005]

【課題を解決するための手段】前記課題は、酸性有機廃
水と炭酸カルシウムとを中和反応させることにより、前
記酸性有機廃水のpHを調整したのち、生物により有機
物を分解させることを特徴とする酸性有機廃水の処理方
法によって解決できる。また、酸性有機廃水と炭酸カル
シウムとを中和反応させることにより、前記酸性有機廃
水のpHを調整しながら、生物により有機物を分解させ
ることを特徴とする酸性有機廃水の処理方法によって解
決できる。
The object of the present invention is to adjust the pH of the acidic organic wastewater by neutralizing the acidic organic wastewater with calcium carbonate, and then decompose organic substances by living organisms. It can be solved by the treatment method of acidic organic wastewater. Further, the problem can be solved by a method for treating acidic organic wastewater, wherein organic matter is decomposed by living organisms while the pH of the acidic organic wastewater is adjusted by neutralizing the acidic organic wastewater with calcium carbonate.

【0006】さらに、前記課題は、酸性有機廃水のpH
調整を行うpH調整槽と生物処理槽とを有する酸性有機
廃水の処理装置であり、前記pH調整槽は、粒状の炭酸
カルシウムを収容し得るとともに、供給された前記酸性
有機廃水が前記pH調整槽にて中和された後オーバーフ
ローする構成となっており、前記生物処理槽は、前記p
H調整槽からオーバーフローした有機廃水が導入され、
前記酸性有機廃水中の有機物を生物により分解させるも
のであることを特徴とする酸性有機廃水の処理装置によ
って解決できる。
[0006] Further, the above-mentioned problem is a problem of pH of acidic organic wastewater.
An acidic organic wastewater treatment device having a pH adjustment tank for performing adjustment and a biological treatment tank, wherein the pH adjustment tank can contain granular calcium carbonate, and the supplied acidic organic wastewater is supplied to the pH adjustment tank. Is overflowed after neutralization in the biological treatment tank.
Organic wastewater overflowing from the H adjustment tank is introduced,
The problem can be solved by a treatment apparatus for acidic organic wastewater, wherein organic matter in the acidic organic wastewater is decomposed by living organisms.

【0007】また、酸性有機廃水のpH調整を行うpH
調整槽と生物処理槽とを有する酸性有機廃水の処理装置
であり、前記pH調整槽は、粒状の炭酸カルシウムを収
容し得るとともに、前記炭酸カルシウムの粒径よりも小
さい孔を有するものであり、前記生物処理槽は、前記孔
から流出した中和処理後の有機廃水が導入され、前記酸
性有機廃水中の有機物を生物により分解させるものであ
ることを特徴とする酸性有機廃水の処理装置としてもよ
い。本発明において、「炭酸カルシウムの粒径よりも小
さい孔」とは、pH調整槽に投入時の粒状の炭酸カルシ
ウムの粒径よりも小さい孔のことをいう。
Further, the pH for adjusting the pH of acidic organic wastewater is adjusted.
An acidic organic wastewater treatment device having an adjustment tank and a biological treatment tank, wherein the pH adjustment tank can accommodate granular calcium carbonate and has pores smaller than the particle size of the calcium carbonate, In the biological treatment tank, the organic wastewater after the neutralization treatment flowing out of the holes is introduced, and the organic wastewater in the acidic organic wastewater is decomposed by living organisms. Good. In the present invention, “pores smaller than the particle size of calcium carbonate” refers to holes smaller than the particle size of granular calcium carbonate when charged into a pH adjusting tank.

【0008】さらにまた、酸性有機廃水のpH調整を行
うpH調整槽と、前記酸性有機廃水の有機物を生物によ
り分解させる生物処理槽とを有する酸性有機廃水の処理
装置であり、前記pH調整槽は、前記生物処理槽内に設
けられ、粒状の炭酸カルシウムを収容し得るとともに、
前記炭酸カルシウムの粒径よりも小さい孔を有するもの
であり、前記pH調整槽内の酸性有機廃水と前記生物処
理槽内の酸性有機廃水とが、前記孔を介して互いに流通
可能とされていることを特徴とする酸性有機廃水の処理
装置としてもよい。
Further, the present invention is an acidic organic wastewater treatment apparatus comprising a pH adjusting tank for adjusting the pH of acidic organic wastewater and a biological treatment tank for decomposing organic substances of the acidic organic wastewater by living organisms. , Provided in the biological treatment tank, can accommodate granular calcium carbonate,
It has pores smaller than the particle size of the calcium carbonate, and the acidic organic wastewater in the pH adjusting tank and the acidic organic wastewater in the biological treatment tank can be mutually circulated through the holes. It is good also as an acidic organic wastewater treatment apparatus characterized by the above.

【0009】[0009]

【発明の実施の形態】図1は、本発明の酸性有機廃水の
処理装置の一例を示した図である。図1において、符号
3は、酸性有機廃水のpH調整を行うpH調整槽を示
し、符号1は、酸性有機廃水の有機物を生物により分解
させる生物処理槽を示している。前記pH調整槽3は、
生物処理槽1の内壁に設けられ、粒状の炭酸カルシウム
2を収容している。
FIG. 1 is a diagram showing an example of an apparatus for treating acidic organic wastewater of the present invention. In FIG. 1, reference numeral 3 denotes a pH adjusting tank for adjusting the pH of acidic organic wastewater, and reference numeral 1 denotes a biological treatment tank for decomposing organic substances of acidic organic wastewater by living organisms. The pH adjustment tank 3 comprises:
It is provided on the inner wall of the biological treatment tank 1 and contains granular calcium carbonate 2.

【0010】この装置を用いて酸性有機廃水を処理する
には、まず、酸性有機廃水を、図1の矢印7で示すよう
に、pH調整槽3に連続して供給し、炭酸カルシウムと
の中和反応により前記酸性有機廃水のpHを調整したの
ち、前記pH調整槽3の開口3aから図1の矢印8で示
すようにオーバーフローさせる。ついで、pH調整槽3
からオーバーフローされた有機廃水を、前記生物処理槽
1に供給する。このとき、生物処理槽1内の液面6は、
pH調整槽3の開口3aよりも低い位置となるように設
定される。そして、生物処理槽1に供給された有機廃水
中の有機物(BOD成分)を生物により分解し、生物処
理槽1のpH調整槽3と対向する壁面上部に設けられた
排出口5から、図1の矢印9で示すように排出すること
により、処理水が得られる。
In order to treat acidic organic wastewater using this apparatus, first, acidic organic wastewater is continuously supplied to the pH adjusting tank 3 as shown by an arrow 7 in FIG. After the pH of the acidic organic wastewater is adjusted by the summation reaction, the wastewater is allowed to overflow from the opening 3a of the pH adjusting tank 3 as shown by an arrow 8 in FIG. Then, pH adjustment tank 3
The organic wastewater overflowed from is supplied to the biological treatment tank 1. At this time, the liquid level 6 in the biological treatment tank 1
It is set to be at a position lower than the opening 3a of the pH adjusting tank 3. Then, the organic matter (BOD component) in the organic wastewater supplied to the biological treatment tank 1 is decomposed by living organisms, and the organic matter (BOD component) in the biological treatment tank 1 is discharged from an outlet 5 provided at the upper part of the wall facing the pH adjusting tank 3 in FIG. By discharging as shown by the arrow 9, treated water is obtained.

【0011】前記pH調整槽3内では、前記酸性有機廃
水と炭酸カルシウム2との中和反応が行われる。この中
和反応により、酸性有機廃水のpHは、ほぼ中性に調整
される。前記酸性有機廃水の中和反応は、下記反応式
(I)に示すように、pH調整槽3内に投入された炭酸
カルシウム2が酸性有機廃水と接触することにより溶解
して炭酸イオンとカルシウムイオンとに解離し、前記炭
酸イオンと酸性有機廃水の酸性を呈している水素イオン
とが反応することにより行われる。
In the pH adjusting tank 3, a neutralization reaction between the acidic organic wastewater and the calcium carbonate 2 is performed. By this neutralization reaction, the pH of the acidic organic wastewater is adjusted to almost neutral. In the neutralization reaction of the acidic organic wastewater, as shown in the following reaction formula (I), the calcium carbonate 2 put in the pH adjusting tank 3 is dissolved by contact with the acidic organic wastewater to dissolve the carbonate ion and the calcium ion. The reaction is carried out by reacting the carbonate ion with the hydrogen ion exhibiting the acidity of the acidic organic wastewater.

【0012】[0012]

【化1】 Embedded image

【0013】前記炭酸カルシウム2は、少なくとも酸性
有機廃水のオーバーフローによって、流出しない程度の
大きさを有する粒状のものが投入される。投入された炭
酸カルシウム2は、pH調整槽3内に保持された状態
で、酸性有機廃水と中和反応することによって消費され
る。この消費によって粒径が小さくなった炭酸カルシウ
ムは、最終的に酸性有機廃水とともにオーバーフローに
よって生物処理槽1内に流出する。このようにして消費
される粒状の炭酸カルシウム2は、消費量に合わせてp
H調整槽3内に定期的に補充される。
The calcium carbonate 2 is supplied in the form of granules having a size that does not flow out at least by overflow of the acidic organic wastewater. The introduced calcium carbonate 2 is consumed by performing a neutralization reaction with acidic organic wastewater while being held in the pH adjustment tank 3. The calcium carbonate whose particle size has been reduced by this consumption finally flows out into the biological treatment tank 1 by overflow together with the acidic organic wastewater. The granular calcium carbonate 2 consumed in this way is p
It is periodically refilled in the H adjustment tank 3.

【0014】また、前記pH調整槽3からオーバーフロ
ーされた有機廃水中の有機物(BOD成分)は、生物に
より分解される。ここでの生物としては、スポンジ状や
粒状などの抗体に付着させた微生物、活性汚泥、生物膜
などを用いることができ、とくに、前記抗体に付着させ
た微生物が好ましく使用される。前記生物は、生物処理
槽1内にあらかじめ保持されていることが好ましい。生
物による有機物の分解は、生物処理槽1内の攪拌と、液
中酸素濃度の調整のために、散気管4から送り出される
空気によって生物処理槽1内を曝気しながら行うことが
好ましい。さらに、生物処理槽1内の温度、有機物(B
OD成分)の濃度、生物の量などの条件を、生物が効果
的に有機物を分解しうる範囲に調整することが望まし
い。
The organic matter (BOD component) in the organic wastewater overflowed from the pH adjusting tank 3 is decomposed by living organisms. Microorganisms, activated sludge, biofilm, and the like attached to the antibody, such as sponge and granules, can be used as the organism here. In particular, microorganisms attached to the antibody are preferably used. It is preferable that the living thing is held in the biological treatment tank 1 in advance. The decomposition of organic matter by living organisms is preferably performed while the inside of the biological treatment tank 1 is aerated with air sent out from the air diffuser 4 in order to stir the inside of the biological treatment tank 1 and adjust the oxygen concentration in the liquid. Furthermore, the temperature in the biological treatment tank 1 and the organic matter (B
It is desirable to adjust the conditions such as the concentration of the OD component) and the amount of the organism to a range where the organism can effectively decompose organic substances.

【0015】このような酸性有機廃水の処理方法は、酸
性有機廃水と炭酸カルシウム2とを中和反応させて前記
酸性有機廃水のpH調整を行うので、強塩基性薬剤を使
用することなく、酸性有機廃水のpHが調整できる。そ
の中和反応は、炭酸カルシウムとの接触による溶解反応
に基づいているため、その炭酸カルシウムの溶解度によ
り、pHは、一定に維持される。したがって、pHを制
御するために、煩雑な管理を伴う機器類を用いる必要は
ない。また、炭酸カルシウム2は、安全性が高いため、
危険性の高い強塩基性薬剤と比較して取扱いが容易であ
り、安全に酸性有機廃水を処理することができる。さら
に、炭酸カルシウム2は、溶解度が非常に小さいため、
短時間で消費することはなく、補充の頻度が少なくてす
み、手間がかからない。
According to such a method for treating acidic organic wastewater, the pH of the acidic organic wastewater is adjusted by neutralizing the acidic organic wastewater with calcium carbonate 2. Therefore, the acidic organic wastewater can be used without using a strong basic agent. The pH of the organic wastewater can be adjusted. Since the neutralization reaction is based on a dissolution reaction by contact with calcium carbonate, the pH is kept constant by the solubility of the calcium carbonate. Therefore, it is not necessary to use devices with complicated management to control the pH. In addition, since calcium carbonate 2 is highly safe,
It is easier to handle as compared with highly dangerous highly basic drugs, and can safely treat acidic organic wastewater. Furthermore, since calcium carbonate 2 has a very low solubility,
It is not consumed in a short time, the frequency of replenishment is low, and no labor is required.

【0016】また、上記の酸性有機廃水の処理装置で
は、前記pH調整槽は、少なくとも酸性有機廃水のオー
バーフローによって流出しない程度の大きさを有する粒
状の炭酸カルシウム2を収容し、供給された前記酸性有
機廃水が中和処理後にオーバーフローするようになって
いるので、pH調整槽3内で、前記炭酸カルシウム2と
酸性有機廃水とを中和反応させることができ、pH調整
槽3内でほぼ中性に調整された酸性有機廃水を生物処理
槽1に供給することが可能である。さらに、粒状の炭酸
カルシウム2をpH調整槽3内に投入することにより、
酸性有機廃水と中和反応させる炭酸カルシウム2を容易
に供給することができる。
In the above-mentioned apparatus for treating acidic organic wastewater, the pH adjusting tank contains at least granular calcium carbonate 2 having a size not to flow out due to overflow of the acidic organic wastewater. Since the organic wastewater overflows after the neutralization treatment, the calcium carbonate 2 and the acidic organic wastewater can be neutralized in the pH adjustment tank 3 and almost neutralized in the pH adjustment tank 3. The adjusted acidic organic wastewater can be supplied to the biological treatment tank 1. Further, by introducing granular calcium carbonate 2 into the pH adjusting tank 3,
Calcium carbonate 2 to be neutralized with acidic organic wastewater can be easily supplied.

【0017】本発明の酸性有機廃水の処理装置は、上述
したように、オーバーフローすることによりpH調整槽
3から生物処理槽1に供給するものとすることができる
が、図2に示すように、前記pH調整槽3の底面3bに
粒状の炭酸カルシウム2よりも小さい孔3cを設け、生
物処理槽1内の液面6を、pH調整槽3の底面3bより
も低い位置になるようにし、この孔3cを介してpH調
整槽3から生物処理槽1に有機廃水を供給するものとし
てもよい。この場合、孔3cは、図2に示すように複数
個であってもよいし、1個であってもよい。また、孔3
cは、pH調整槽3に投入時の粒状の炭酸カルシウム2
よりも小さく形成されていればよい。
As described above, the acidic organic wastewater treatment apparatus of the present invention can be supplied from the pH adjustment tank 3 to the biological treatment tank 1 by overflowing, as shown in FIG. A hole 3c smaller than the granular calcium carbonate 2 is provided in the bottom surface 3b of the pH adjustment tank 3 so that the liquid level 6 in the biological treatment tank 1 is lower than the bottom surface 3b of the pH adjustment tank 3. Organic wastewater may be supplied from the pH adjustment tank 3 to the biological treatment tank 1 through the hole 3c. In this case, the number of holes 3c may be plural as shown in FIG. 2, or may be one. Hole 3
c is the granular calcium carbonate 2 when charged into the pH adjusting tank 3.
What is necessary is just to be formed smaller.

【0018】また、図2に示す酸性有機廃水の処理装置
においては、生物処理槽1内の液面6を、pH調整槽3
の底面3bよりも高い位置となるようにし、廃水が前記
孔を介してpH調整槽3と生物処理槽1内とを互いに流
通可能にしてもよい。この場合、未処理の酸性有機廃水
は、pH調整槽3と生物処理槽1のどちらか一方または
両方に供給することが可能である。また、pH調整槽3
内と生物処理槽1内との廃水の流通は、散気管4から送
り出される空気によって生物処理槽1内を曝気すること
で促進される。
In the apparatus for treating acidic organic wastewater shown in FIG. 2, the liquid level 6 in the biological treatment tank 1 is
May be set at a position higher than the bottom surface 3b, and the wastewater may be allowed to flow between the pH adjustment tank 3 and the biological treatment tank 1 through the hole. In this case, the untreated acidic organic wastewater can be supplied to one or both of the pH adjustment tank 3 and the biological treatment tank 1. In addition, pH adjustment tank 3
The circulation of wastewater between the inside and the biological treatment tank 1 is promoted by aerating the inside of the biological treatment tank 1 with air sent out from the air diffuser 4.

【0019】[0019]

【実施例】以下、実施例と比較例を示して更に詳細に説
明する。
The present invention will be described below in more detail with reference to examples and comparative examples.

【実施例1】図1に示す生物処理装置を用いて酸性有機
廃水の処理を行った。すなわち、表1に示す性状の酸性
有機廃水を、5mm程度以上の粒径を有する粒状の炭酸
カルシウム1.0gが投入されている容積0.05lの
pH調整槽3内に流速0.2l/hrで連続して供給
し、前記酸性有機廃水のpHを調整したのち、前記pH
調整槽3の開口3aからオーバーフローさせた。つい
で、pH調整槽3からオーバーフローされた有機廃水
を、液面6がpH調整槽3の開口3aよりも低い位置と
なるように、0.64lの微生物付着担体が投入されて
いる有効容積3.2lの生物処理槽1に供給し、エアー
流量100l/hrで曝気しながら有機物(BOD成
分)を分解して、処理水を得た。
Example 1 The treatment of acidic organic wastewater was carried out using the biological treatment apparatus shown in FIG. That is, acidic organic wastewater having the properties shown in Table 1 was introduced into a pH adjusting tank 3 having a volume of 0.05 l and charged with 1.0 g of granular calcium carbonate having a particle diameter of about 5 mm or more at a flow rate of 0.2 l / hr. After continuously adjusting the pH of the acidic organic wastewater, the pH is adjusted.
It overflowed from the opening 3a of the adjustment tank 3. Then, the effective volume of the organic wastewater overflowed from the pH adjusting tank 3 into which 0.64 l of the microorganism-adhering carrier is introduced is set so that the liquid level 6 is lower than the opening 3 a of the pH adjusting tank 3. The organic matter (BOD component) was decomposed while being supplied to a 2 l biological treatment tank 1 and aerated at an air flow rate of 100 l / hr to obtain treated water.

【0020】[0020]

【表1】 [Table 1]

【0021】[0021]

【実施例2】実施例1で用いた生物処理装置1のpH調
整槽3の底面3bに、図2に示すように、直径3mmの
3c孔を5つ設け、生物処理装置1内の液面6をpH調
整槽3内の底面3bよりも高い位置とすることで、前記
孔3cを介して廃水がpH調整槽3内と生物処理槽1内
とを互いに流通可能とした生物処理装置を用いて酸性有
機廃水の処理を行った。すなわち、実施例1と同様の酸
性有機廃水を実施例1と同様の流速で生物処理槽1に連
続して供給し、液面6がpH調整槽3の底面3bよりも
わずかに高い位置となるようにするとともに、調整槽3
内で実施例1と同様にして前記酸性有機廃水のpHを調
整しながら、生物処理槽1内で実施例1と同様にして有
機物(BOD成分)を分解し、処理水を得た。
Embodiment 2 As shown in FIG. 2, five 3c holes having a diameter of 3 mm are provided on the bottom surface 3b of the pH adjusting tank 3 of the biological treatment apparatus 1 used in Example 1, and the liquid level in the biological treatment apparatus 1 is increased. 6 is a position higher than the bottom surface 3b in the pH adjustment tank 3, a biological treatment apparatus that allows wastewater to flow between the pH adjustment tank 3 and the biological treatment tank 1 through the hole 3c. To treat acidic organic wastewater. That is, the same acidic organic wastewater as in Example 1 is continuously supplied to the biological treatment tank 1 at the same flow rate as in Example 1, and the liquid level 6 is at a position slightly higher than the bottom surface 3b of the pH adjustment tank 3. And adjusting tank 3
While adjusting the pH of the acidic organic wastewater in the same manner as in Example 1, the organic matter (BOD component) was decomposed in the biological treatment tank 1 in the same manner as in Example 1 to obtain treated water.

【0022】[0022]

【比較例】実施例1で用いた生物処理装置と同様の生物
処理槽1を用いて酸性有機廃水の処理を行った。すなわ
ち、実施例1と同様の酸性有機廃水を実施例1と同様の
流速で生物処理槽1に連続して供給し、炭酸カルシウム
によるp調整を行わずに、実施例1と同様にして有機物
(BOD成分)を分解して、処理水を得た。
Comparative Example The treatment of acidic organic wastewater was performed using the biological treatment tank 1 similar to the biological treatment apparatus used in Example 1. That is, the same acidic organic wastewater as in Example 1 is continuously supplied to the biological treatment tank 1 at the same flow rate as in Example 1, and the organic matter ( BOD component) was decomposed to obtain treated water.

【0023】[0023]

【従来例】実施例1と同様の酸性有機廃水を、あらかじ
め0.1NーNaOHでpH6.8に中和したのち、比
較例と同様にして、処理水を得た。結果を表2に示す。
Prior Art The same acidic organic waste water as in Example 1 was neutralized to pH 6.8 with 0.1N NaOH in advance, and treated water was obtained in the same manner as in Comparative Example. Table 2 shows the results.

【0024】[0024]

【表2】 [Table 2]

【0025】表2より、実施例1で得られた処理水は、
pH6.8、BOD450mg/lであり、実施例2で
得られた処理水は、pH7.3、BOD450mg/l
であり、pH調整を行わなかった比較例で得られた処理
水と比べて、BODが低いことが確認できた。また、あ
らかじめ0.1NーNaOHで酸性有機廃水を中和処理
した従来例と、同等のpHおよびBODの処理水が得ら
れることがあきらかとなった。さらに、実施例1および
実施例2で得られた処理水のBODは、下水道への放流
基準値(600mg/l)以下であり、pHは、下水道
放流基準値(5〜9)内であった。
From Table 2, the treated water obtained in Example 1 was
pH 6.8, BOD 450 mg / l, treated water obtained in Example 2 was pH 7.3, BOD 450 mg / l
It was confirmed that the BOD was lower than that of the treated water obtained in the comparative example in which the pH was not adjusted. Further, it became clear that treated water having the same pH and BOD as that of the conventional example in which acidic organic wastewater was neutralized with 0.1N NaOH in advance was obtained. Furthermore, the BOD of the treated water obtained in Example 1 and Example 2 was equal to or lower than the reference value (600 mg / l) for discharging to the sewer, and the pH was within the reference value for discharging the sewer (5 to 9). .

【0026】[0026]

【発明の効果】以上説明したように、本発明の酸性有機
廃水の処理方法では、酸性有機廃水と炭酸カルシウムと
を中和反応させて前記酸性有機廃水のpH調整を行うの
で、強塩基性薬剤を使用することなく、酸性有機廃水の
pHが調整できる。したがって、pHを制御するため
に、煩雑な管理を伴う機器類を用いる必要はない。その
結果、従来よりも簡便な装置で酸性有機廃水を処理する
ことができる。また、炭酸カルシウムは、安全性が高い
ため、危険性の高い強塩基性薬剤と比較して取扱いが容
易であり、安全に酸性有機廃水を処理することができ
る。さらに、炭酸カルシウムは、溶解度が非常に小さい
ため、短時間で消費することはなく、補充の頻度が少な
くてすみ、手間がかからない。
As described above, in the method for treating acidic organic wastewater of the present invention, the pH of the acidic organic wastewater is adjusted by neutralizing the acidic organic wastewater with calcium carbonate. The pH of the acidic organic wastewater can be adjusted without using any. Therefore, it is not necessary to use devices with complicated management to control the pH. As a result, acidic organic wastewater can be treated with a simpler device than before. In addition, calcium carbonate is highly safe, so it is easier to handle as compared with highly dangerous strong basic drugs, and can treat acidic organic wastewater safely. Further, since calcium carbonate has a very low solubility, it is not consumed in a short time, the frequency of replenishment is low, and no labor is required.

【0027】また、上記の酸性有機廃水の処理装置で
は、前記pH調整槽は、粒状の炭酸カルシウムを収容し
ているので、pH調整槽内で、前記炭酸カルシウムと酸
性有機廃水とを中和反応させることができる。さらに、
粒状の炭酸カルシウムをpH調整槽内に投入することに
より、酸性有機廃水と中和反応させる炭酸カルシウムを
容易に供給することができる。
In the above-mentioned apparatus for treating acidic organic wastewater, since the pH adjusting tank contains granular calcium carbonate, the calcium carbonate and the acidic organic wastewater are neutralized in the pH adjusting tank. Can be done. further,
By feeding granular calcium carbonate into the pH adjusting tank, calcium carbonate to be neutralized with acidic organic wastewater can be easily supplied.

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

【図1】 本発明の酸性有機廃水の処理装置の一例を示
した図である。
FIG. 1 is a diagram showing an example of an apparatus for treating acidic organic wastewater of the present invention.

【図2】 本発明の酸性有機廃水の処理装置の他の例を
示した図である。
FIG. 2 is a view showing another example of the acidic organic wastewater treatment apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1 生物処理槽 2 炭酸カルシウム 3 pH調整槽 3a 開口 3b 底面 3c 孔 4 散気管 5 排出口 6 液面 DESCRIPTION OF SYMBOLS 1 Biological treatment tank 2 Calcium carbonate 3 pH adjustment tank 3a Opening 3b Bottom surface 3c Hole 4 Air diffuser 5 Outlet 6 Liquid level

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 3/12 C02F 3/12 N ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 3/12 C02F 3/12 N

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 酸性有機廃水と炭酸カルシウムとを中和
反応させることにより、前記酸性有機廃水のpHを調整
したのち、生物により有機物を分解させることを特徴と
する酸性有機廃水の処理方法。
1. A method for treating acidic organic wastewater, comprising the steps of: adjusting the pH of the acidic organic wastewater by neutralizing the acidic organic wastewater with calcium carbonate; and then decomposing organic substances by living organisms.
【請求項2】 酸性有機廃水と炭酸カルシウムとを中和
反応させることにより、前記酸性有機廃水のpHを調整
しながら、生物により有機物を分解させることを特徴と
する酸性有機廃水の処理方法。
2. A method for treating acidic organic wastewater, wherein organic matter is decomposed by living organisms while the pH of the acidic organic wastewater is adjusted by neutralizing the acidic organic wastewater with calcium carbonate.
【請求項3】 酸性有機廃水のpH調整を行うpH調整
槽と生物処理槽とを有する酸性有機廃水の処理装置であ
り、 前記pH調整槽は、粒状の炭酸カルシウムを収容し得る
とともに、供給された前記酸性有機廃水が中和反応後オ
ーバーフローする構成となっており、 前記生物処理槽は、前記pH調整槽からオーバーフロー
した有機廃水が導入され、前記酸性有機廃水中の有機物
を生物により分解させるものであることを特徴とする酸
性有機廃水の処理装置。
3. An acidic organic wastewater treatment apparatus having a pH adjusting tank for adjusting the pH of an acidic organic wastewater and a biological treatment tank, wherein the pH adjusting tank is capable of containing granular calcium carbonate and being supplied. The acidic organic wastewater is configured to overflow after the neutralization reaction, and the biological treatment tank is configured to receive the organic wastewater overflowed from the pH adjustment tank and decompose organic substances in the acidic organic wastewater by living organisms. An acidic organic wastewater treatment apparatus, characterized in that:
【請求項4】 酸性有機廃水のpH調整を行うpH調整
槽と生物処理槽とを有する酸性有機廃水の処理装置であ
り、 前記pH調整槽は、粒状の炭酸カルシウムを収容し得る
とともに、前記炭酸カルシウムの粒径よりも小さい孔を
有するものであり、 前記生物処理槽は、前記孔から中和され流出した有機廃
水が導入され、前記酸性有機廃水中の有機物を生物によ
り分解させるものであることを特徴とする酸性有機廃水
の処理装置。
4. A treatment apparatus for an acidic organic wastewater having a pH adjusting tank for adjusting the pH of an acidic organic wastewater and a biological treatment tank, wherein the pH adjusting tank can contain granular calcium carbonate, and The biological treatment tank has pores smaller than the particle diameter of calcium, and the biological treatment tank is configured to receive the organic wastewater neutralized and flowing out of the pores and decompose organic substances in the acidic organic wastewater by living organisms. A device for treating acidic organic wastewater.
【請求項5】 酸性有機廃水のpH調整を行うpH調整
槽と、前記酸性有機廃水の有機物を生物により分解させ
る生物処理槽とを有する酸性有機廃水の処理装置であ
り、 前記pH調整槽は、前記生物処理槽内に設けられ、粒状
の炭酸カルシウムを収容し得るとともに、前記炭酸カル
シウムの粒径よりも小さい孔を有するものであり、 供給された前記酸性有機廃水が前記pH調整槽内と前記
生物処理槽内とを前記孔を介して互いに流通可能とされ
ていることにより、中和処理と生物処理を同時に行うこ
とを特徴とする酸性有機廃水の処理装置。
5. An acidic organic wastewater treatment device comprising: a pH adjusting tank for adjusting the pH of acidic organic wastewater; and a biological treatment tank for decomposing organic substances of the acidic organic wastewater by living organisms. It is provided in the biological treatment tank, and can accommodate granular calcium carbonate, and has pores smaller than the particle size of the calcium carbonate, and the supplied acidic organic wastewater is contained in the pH adjustment tank and the An acidic organic wastewater treatment apparatus, wherein a neutralization treatment and a biological treatment are performed at the same time by being able to flow through the inside of the biological treatment tank through the holes.
JP11020744A 1999-01-28 1999-01-28 Treatment of acidic organic waste water and treating device Pending JP2000218283A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11020744A JP2000218283A (en) 1999-01-28 1999-01-28 Treatment of acidic organic waste water and treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11020744A JP2000218283A (en) 1999-01-28 1999-01-28 Treatment of acidic organic waste water and treating device

Publications (1)

Publication Number Publication Date
JP2000218283A true JP2000218283A (en) 2000-08-08

Family

ID=12035712

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2000218283A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010184211A (en) * 2009-02-13 2010-08-26 Sumitomo Chemical Co Ltd Wastewater treatment method
CN113666388A (en) * 2021-08-25 2021-11-19 浙江闰土股份有限公司 Treatment method of dye wastewater

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54144037A (en) * 1978-04-28 1979-11-09 Gunze Kk Method of denitrifying waste water
JPS614800U (en) * 1984-06-15 1986-01-13 保 森 Car wash wastewater regeneration device
JPH10480A (en) * 1996-06-14 1998-01-06 Hoshizaki Electric Co Ltd Neutralization tank for acidic water
JPH10249365A (en) * 1997-03-10 1998-09-22 Kubota Corp Sewage treating device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54144037A (en) * 1978-04-28 1979-11-09 Gunze Kk Method of denitrifying waste water
JPS614800U (en) * 1984-06-15 1986-01-13 保 森 Car wash wastewater regeneration device
JPH10480A (en) * 1996-06-14 1998-01-06 Hoshizaki Electric Co Ltd Neutralization tank for acidic water
JPH10249365A (en) * 1997-03-10 1998-09-22 Kubota Corp Sewage treating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010184211A (en) * 2009-02-13 2010-08-26 Sumitomo Chemical Co Ltd Wastewater treatment method
CN113666388A (en) * 2021-08-25 2021-11-19 浙江闰土股份有限公司 Treatment method of dye wastewater

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