JPH07112194A - Treatment with activated sludge of industrial waste water - Google Patents

Treatment with activated sludge of industrial waste water

Info

Publication number
JPH07112194A
JPH07112194A JP5262237A JP26223793A JPH07112194A JP H07112194 A JPH07112194 A JP H07112194A JP 5262237 A JP5262237 A JP 5262237A JP 26223793 A JP26223793 A JP 26223793A JP H07112194 A JPH07112194 A JP H07112194A
Authority
JP
Japan
Prior art keywords
activated sludge
industrial wastewater
treatment
sludge treatment
beer
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
JP5262237A
Other languages
Japanese (ja)
Inventor
Masahiro Fujii
正博 藤井
Shigeharu Matsubara
茂晴 松原
Masaya Ishio
真弥 石尾
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.)
KYUSHU KANKYO KANRI KYOKAI
Original Assignee
KYUSHU KANKYO KANRI KYOKAI
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 KYUSHU KANKYO KANRI KYOKAI filed Critical KYUSHU KANKYO KANRI KYOKAI
Priority to JP5262237A priority Critical patent/JPH07112194A/en
Publication of JPH07112194A publication Critical patent/JPH07112194A/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

Abstract

PURPOSE:To smoothly perform an activated sludge treatment of industrial waste water incorporating harmful components hindering the function of activated sludge such as sulfides and cyan compounds. CONSTITUTION:A mixture of strained lees from beer and/or strained less from bean curd or the both plus a water soluble iron salt is added to an aeration tank for activated sludge treatment of the industrial waste water containing the harmful components hindering the function of the activated sludge such as sulfides and cyan compounds. As a result, a lowered activity of the activated sludge for treating industrial waste water containing the harmful components which hinder the function of the activated sludge such as sulfides and cyan compounds is recovered in a short time and also occurrence of the undesirable treatment condition is previously suppressed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、活性汚泥に対して有害
なシアン化合物及び又は硫化物を含む産業廃水の活性汚
泥処理を円滑に行わせる方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for smoothly performing activated sludge treatment of industrial wastewater containing a cyanide and / or sulfide harmful to activated sludge.

【0002】[0002]

【従来の技術】製鉄所、化学工場、ガス工場などのコー
クス炉から発生する安水、石油精製工場、化学薬品、染
料などの化学工場などから排出される産業廃水は、BO
D、CODによって表示される汚濁物を活性汚泥処理方
法により処理を行っている。しかし、これらの産業廃水
は製造プロセス、原料の種類、生産量などの変動により
廃水の発生量、汚濁物濃度などが大幅に変動し、このた
め、活性汚泥処理は処理不調、即ち、汚濁物成分の分解
不良、活性汚泥のバルキングが発生し易く、処理水質の
悪化を招き易い。
[0002] Industrial water discharged from coke ovens such as steel mills, chemical plants and gas plants, industrial wastewater discharged from petroleum refining plants, chemical plants such as chemicals and dyes, etc.
The pollutants indicated by D and COD are treated by the activated sludge treatment method. However, in these industrial wastewater, the amount of wastewater generated, the concentration of pollutants, etc. fluctuate significantly due to changes in the manufacturing process, types of raw materials, production volume, etc. Is not easily decomposed, bulking of activated sludge is likely to occur, and the quality of treated water is likely to deteriorate.

【0003】特に、コークス炉から排出される安水、石
油精製工場の廃水は、活性汚泥の機能を阻害する硫化物
及び又はシアン化合物を含有しているので、汚濁物負荷
量の変動と相俟って、処理不調が発生し易い。
In particular, the low water discharged from the coke oven and the wastewater of the oil refinery contain sulfide and / or cyanide compounds which hinder the function of activated sludge, and therefore, they are associated with the fluctuation of the pollutant load. As a result, processing failure is likely to occur.

【0004】[0004]

【発明が解決しようとする課題】このような、産業廃水
の活性汚泥処理、例えば、製鉄所、化学工場、都市ガス
工場などにおいて石炭からコークス、都市ガスなどを製
造する際にコークス炉から排出される安水(ガス廃
液)、石油精製工場の廃水は、COD、BOD、フェノ
ール系化合物、ロダン化合物などによって表示される汚
濁成分を活性汚泥処理方法によって処理を行っている。
これらの産業廃水の活性汚泥処理は、フェノール系化合
物、ロダン化合物などのCOD成分の大部分を分解除去
する重要なプロセスであるにもかかわらず、都市下水な
どの活性汚泥処理の設備、管理、操業条件などを、その
まま模倣している。しかし、これらの産業廃水は、都市
下水などに比べて組成的に複雑であり、又シアン化合
物、硫化物など活性汚泥の機能を阻害する毒性成分を含
有しているので、都市下水などの活性汚泥処理の設備仕
様、管理、操業技術などをそのまま適用するには限界が
ある。このため、従来のこれらの産業廃水の活性汚泥処
理は、原因不明の処理不調が発生しやすく、又処理不調
が発生すると、その回復方法は、試行錯誤的であり、回
復に2〜6ケ月の長期間を要することがある。
The above-mentioned activated sludge treatment of industrial wastewater, for example, when producing coke, city gas, etc. from coal in a steel mill, chemical factory, city gas factory, etc., is discharged from the coke oven. The polluted components represented by COD, BOD, phenolic compounds, rhodan compounds, etc. are treated by the activated sludge treatment method for the safe water (gas waste liquid) and the wastewater of the oil refinery.
Although the activated sludge treatment of these industrial wastewaters is an important process that decomposes and removes most of the COD components such as phenolic compounds and rhodan compounds, it is necessary to install, manage and operate the activated sludge treatment of municipal sewage. The conditions are imitated as they are. However, since these industrial wastewaters are more complex in composition than city sewage and contain toxic components that inhibit the function of activated sludge such as cyanide compounds and sulfides, activated sludge such as city sewage is There is a limit to applying processing equipment specifications, management, operation technology, etc. as they are. For this reason, in the conventional activated sludge treatment of these industrial wastewater, a treatment failure of unknown cause is likely to occur, and when the treatment failure occurs, the recovery method is trial-and-error, and it takes 2 to 6 months for the recovery. It may take a long time.

【0005】さらに、処理不調が発生した場合の重要な
問題点は、処理不調の多くのケースにおいて、汚泥のバ
ルキングがおこること及びロダン化合物の分解性が低下
し処理水質が悪化することである。この処理水中のロダ
ン化合物は、鉄凝集沈澱法、活性炭吸着法などの物理化
学的処理によっても除去困難であり、現在の所、活性汚
泥処理以外の方法では経済的にしかも効率的に除去する
技術が確立されていない。従って、このような場合、活
性汚泥処理の後に鉄凝集沈澱法、活性炭吸着法などの追
加処理設備を設置してもロダン化合物は、この処理設備
を素通りして除去することができない。
Further, an important problem when the treatment failure occurs is that, in many cases of the treatment failure, the sludge bulking occurs and the decomposability of the rhodane compound is lowered to deteriorate the treated water quality. Rhodan compounds in this treated water are difficult to remove even by physicochemical treatment such as iron coagulation precipitation method, activated carbon adsorption method, etc. Currently, technology other than activated sludge treatment is economically and efficiently removed. Is not established. Therefore, in such a case, even if an additional treatment equipment such as an iron coagulation sedimentation method or an activated carbon adsorption method is installed after the activated sludge treatment, the rhodane compound cannot be removed by passing through this treatment equipment.

【0006】このロダン化合物を分解する菌(ロダン分
解菌)は、フェノールなどを分解する菌に比べて増殖性
が著しく遅く、発明者の研究によると毒性物質、pHな
どのショックによりロダン分解菌の機能が低下した場
合、これらのショックを取り除いた後、機能がショック
以前の状態に回復するのに20〜60日も要し、この期
間は、処理水のCOD、ロダン濃度が高い状態が続くこ
とが明らかになっている。
[0006] The fungus that decomposes this rhodane compound (rodan-decomposing bacterium) has a remarkably slower proliferative property than the fungus that decomposes phenol and the like. If the function deteriorates, it takes 20 to 60 days for the function to recover to the state before the shock after removing these shocks, and during this period, the COD and the rhodan concentration of the treated water remain high. Has been revealed.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決するた
め本発明は 産業廃水の活性汚泥処理において、曝気槽にビールのし
ぼりかす及び又は豆腐のしぼりかす(おから)を添加し
て、活性汚泥処理を行わせることを特徴とする産業廃水
の活性汚泥処理方法 ビールのしぼりかす及び又は豆腐のしぼりかすと水溶性
鉄塩を添加する上記発明記載の産業廃水の活性汚泥処理
方法 産業廃水が活性汚泥の機能を阻害する有害成分を含む上
記第1又は第2発明記載の産業廃水の活性汚泥処理方法 上記有害成分がシアン化合物及び又は硫化物などの還元
性硫黄化合物を含む廃水である上記第3発明記載の産業
廃水の活性汚泥処理方法 産業廃水がコークス炉から発生する安水(ガス廃液)で
ある上記第1〜第4発明にそれぞれ記載の産業廃水の活
性汚泥処理方法 処理不調が発生した安水の活性汚泥処理を行いかつ回復
させる上記第5発明記載の産業廃水の活性汚泥処理方法 ビールのしぼりかす及び又は豆腐のしぼりかすと第2鉄
塩単独、或いは第2鉄塩と第1鉄塩とを組み合わせた水
溶性鉄塩を添加する上記第6発明記載の産業廃水の活性
汚泥処理方法 によって構成される。
Means for Solving the Problems In order to solve the above-mentioned problems, the present invention provides activated sludge treatment of industrial wastewater by adding beer squeezer and / or tofu squeezer (okara) to an aeration tank for activation. Activated sludge treatment method of industrial wastewater characterized by performing sludge treatment Activated sludge treatment method of industrial wastewater according to the above invention wherein squeezed beer and / or tofu squeeze and water-soluble iron salt are added Method for treating activated sludge of industrial wastewater according to the first or second invention, which contains harmful components that inhibit sludge function The above-mentioned third, wherein the harmful components are wastewater containing a reducing sulfur compound such as a cyanide compound and / or a sulfide. Activated sludge treatment method for industrial wastewater according to the invention The activated sludge treatment process for industrial wastewater according to each of the first to fourth inventions, wherein the industrial wastewater is an ammonium hydroxide (gas waste liquid) generated from a coke oven. Method: Activated sludge treatment method of industrial wastewater according to the fifth aspect of the present invention, which comprises performing and recovering activated sludge treatment of cheap water in which treatment failure has occurred Squeezing beer and / or tofu squeezing powder and ferric iron alone or second It is constituted by the method for treating activated sludge of industrial wastewater according to the sixth invention, wherein a water-soluble iron salt obtained by combining an iron salt and a ferrous salt is added.

【0008】[0008]

【作用】発明者らは、既に、活性汚泥の機能を阻害する
有害成分がシアン化合物及び又は硫化物などの還元性硫
黄化合物を含む産業廃水、例えば、安水の処理に適した
処理技術を確立しているが、処理不調に対してある程度
は対処することができた。
The inventors have already established a treatment technique suitable for treating industrial wastewater, for example, ammonium hydroxide, in which harmful components that inhibit the function of activated sludge include cyanide compounds and / or reducing sulfur compounds such as sulfides. However, I was able to deal with the poor processing to some extent.

【0009】今回の本発明は、従来の方法を更に改善し
て、活性汚泥の機能を阻害する有害成分がシアン化合物
及び又は硫化物などの還元性硫黄化合物を含む産業廃水
の活性汚泥処理が不調になったときに従来の方法よりも
著しく短期間に回復させる技術を完成するに至ったもの
である。
In the present invention, the conventional method is further improved so that the activated sludge treatment of industrial wastewater containing harmful compounds that inhibit the function of the activated sludge containing a reducing sulfur compound such as a cyanide compound and / or a sulfide is unsuccessful. Then, we have completed the technology to recover in a significantly shorter time than the conventional method.

【0010】即ち、コーク炉から排出される安水、石油
精製工場の廃水によって代表される活性汚泥の機能を阻
害する有害成分がシアン化合物及び又は硫化物などの還
元性硫黄化合物を含む産業廃水の活性汚泥処理は、活性
汚泥の機能を阻害する成分によるショック、あるいは異
常pHによるショックによる処理不調が発生し易い。こ
れは、これらのショックにより活性汚泥を構成している
バクテリアの数がかなり減少していると共に活性度の低
下に起因している。従って、処理不調が正常な処理状態
に回復するためには、まず、ショックによって減少した
バクテリアを増殖させて正常な処理を行っていたときの
状態に回復させなければならない。
That is, industrial wastewater containing harmful compounds that inhibit the function of activated sludge, such as cheap water discharged from a coke oven and wastewater of an oil refinery, contains cyanide compounds and / or reducing sulfur compounds such as sulfides. In the activated sludge treatment, a treatment disorder is likely to occur due to a shock due to a component that inhibits the function of the activated sludge or a shock due to an abnormal pH. This is because these shocks significantly reduce the number of bacteria that make up the activated sludge and also decrease the activity. Therefore, in order to recover the processing disorder to the normal processing state, first, the bacteria reduced by shock must be grown to recover the state when the normal processing was performed.

【0011】処理不調の活性汚泥を正常な状態に回復さ
せる方法は、処理不調になった原因を取り除いて活性汚
泥のpH、温度、DOなどを適正な条件に管理する方法
が最も普遍的である。
The most general method for recovering the untreated activated sludge to a normal state is to remove the cause of the untreated treatment and manage the pH, temperature and DO of the activated sludge under appropriate conditions. .

【0012】しかし、活性汚泥は各種バクテリアの集合
体であり、各バクテリアの性状がかなり異なっているこ
とが考えられる。例えば、先に説明したようにロダン分
解菌の増殖速度は非常に遅く、フェノール系化合物を分
解するバクテリアの約1/40である。従って、例え
ば、安水の活性汚泥処理の不調を短期間に回復させるた
めには、ロダン分解菌のように増殖速度の遅いバクテリ
アの増殖速度を促進する必要がある。
However, activated sludge is an aggregate of various bacteria, and it is conceivable that the properties of each bacterium are quite different. For example, as described above, the growth rate of the rhodanic acid-degrading bacterium is very slow, which is about 1/40 of that of bacteria degrading phenolic compounds. Therefore, for example, in order to recover the disorder of the activated sludge treatment of the ammonium hydroxide in a short period of time, it is necessary to promote the growth rate of a slow-growing bacterium such as a rhodane-degrading bacterium.

【0013】従来の不調回復方法は、活性汚泥処理の条
件即ち、温度、pH、溶存酸素(DO)などを管理しバ
クテリアの自然増殖を期待するに過ぎず、このような方
法では処理不調の回復は、先に説明したように長期間を
要する。
The conventional disorder recovery method merely controls the conditions of activated sludge treatment, that is, temperature, pH, dissolved oxygen (DO), etc. and expects natural growth of bacteria. Takes a long time as explained above.

【0014】発明者らは、安水、石油精製工場などの廃
水に代表される活性汚泥の機能を阻害する有害成分がシ
アン化合物及び又は硫化物などの還元性硫黄化合物を含
む産業廃水の活性汚泥処理の不調を短期間に回復させる
ためにバクテリア、特に、ロダン分解菌の増殖を促進さ
せて処理不調を短期間に回復させる方法について研究を
行った。
The inventors of the present invention have activated sludge of industrial wastewater containing harmful compounds that inhibit the function of activated sludge typified by wastewater such as cheap water and oil refineries containing cyanide compounds and / or reducing sulfur compounds such as sulfides. In order to recover the treatment disorder in a short period of time, a study was conducted on a method of promoting the growth of bacteria, in particular, a rhodane-degrading bacterium to restore the treatment disorder in a short period of time.

【0015】一般に、バクテリアは、微量のビタミン、
酵素、フチン酸などが存在すると増殖速度が促進される
ことが知られている。発明者らは、ビタミン、酵素、フ
チン酸などを安水活性汚泥処理の曝気槽に添加しバクテ
リアの増殖速度を測定した結果、ロダン分解菌を例にと
ると無添加の場合に比べて増殖速度が約2〜5倍も促進
されることが判明した。この結果から、活性汚泥処理の
不調が発生した場合、ビタミン、酵素、フチン酸などを
添加すると不調が短期間に回復することが考えられる。
In general, bacteria are trace amounts of vitamins,
It is known that the growth rate is promoted in the presence of enzymes, phytic acid and the like. The inventors measured the growth rate of bacteria by adding vitamins, enzymes, phytic acid, etc. to the aeration tank of the activated water sludge treatment, and as a result, in the case of Rhodan-degrading bacteria as an example, the growth rate was higher than that without addition. Was promoted about 2 to 5 times. From these results, it is conceivable that if a problem occurs in the activated sludge treatment, the addition of vitamins, enzymes, phytic acid, etc. will recover the problem in a short period of time.

【0016】そこで、実際に不調が発生した活性汚泥処
理に、これらを添加した結果、ロダン化合物の分解不良
の回復は、従来の方法が20〜60日間も要していたの
に対してビタミン、酵素、フチン酸などを添加すること
により7〜10日間で回復した。
Therefore, as a result of adding these to the activated sludge treatment in which a malfunction actually occurred, recovery of poor decomposition of the rhodane compound took 20 to 60 days in comparison with the conventional method, but vitamins, It was recovered in 7 to 10 days by adding enzymes, phytic acid and the like.

【0017】しかし、実設備の処理不調にこの方法を適
用すると大量のビタミン、酵素、フチン酸などを必要と
し、コスト的に問題があり実用化は、かなり困難であ
る。そこで発明者らはビタミン、酵素、フチン酸を含む
物質で安価で、かつ大量に入手できるものとしてビール
しぼりかす、豆腐のしぼりかす(おから)に着目し、こ
れを安水、石油精製工場の廃水に代表される活性汚泥の
機能を阻害する有害成分がシアン化合物及び又は硫化物
などの還元性硫黄化合物を含む産業廃水の活性汚泥処理
の曝気槽に散布したところビタミン、酵素、フチン酸を
添加したときと同程度の効果が得られることが判った。
[0017] However, if this method is applied to the treatment failure of the actual equipment, a large amount of vitamins, enzymes, phytic acid, etc. are required, and there is a problem in terms of cost, and practical application is quite difficult. Therefore, the inventors focused on beer squeeze cake and tofu squeeze cake (okara) as a substance containing vitamins, enzymes, and phytic acid, which is inexpensive and available in large quantities, and uses this for the refined water and refinery plants. Vitamin, enzyme, phytic acid were added when sprayed to the aeration tank of the activated sludge treatment of industrial wastewater containing harmful compounds that inhibit the function of activated sludge represented by wastewater containing cyanide compounds and / or reducing sulfur compounds such as sulfides. It was found that the same effect as when it was done can be obtained.

【0018】又、安水、石油精製工場などの廃水に代表
される活性汚泥の機能を阻害する有害成分がシアン化合
物及び又は硫化物などの還元性硫黄化合物を含む産業廃
水の活性汚泥処理は、処理不調になると活性汚泥のバル
キング(膨潤化)が起こり、汚泥沈澱槽において汚泥の
浮上、流出が起こり、活性汚泥が処理水に流出して、処
理水質の悪化を招く。又、このバルキングは、回復に適
切な方法が無く、このため回復に長期間要していた。し
かし、本発明において、このようなバルキングを起こし
た活性汚泥にビールしぼりかす及び又は豆腐のしぼりか
すと水溶性鉄塩、例えば、第2鉄塩単独、或いは第2鉄
塩と第1鉄塩とを組み合わせた鉄塩の水溶液を添加する
と早期に回復することが明らかになった。
The activated sludge treatment of industrial wastewater containing harmful compounds that inhibit the function of activated sludge typified by wastewater such as cheap water and oil refineries contains cyanide compounds and / or reducing sulfur compounds such as sulfides. When the treatment becomes unsuccessful, activated sludge bulking (swelling) occurs, sludge floats and flows out in the sludge settling tank, and the activated sludge flows out into the treated water, causing deterioration of the treated water quality. In addition, this bulking had no proper method for recovery, and thus it took a long time to recover. However, in the present invention, beer squeeze cake and / or tofu squeeze cake and water-soluble iron salt, for example, ferric iron salt alone, or ferric iron salt and ferrous iron salt are added to activated bulk sludge that has caused such bulking. It was clarified that the recovery was made early by adding the aqueous solution of the iron salt which was combined with.

【0019】このバルキングの回復機構について、次の
ように考えられる。ビールのしぼりかす及び又は豆腐の
しぼりかすは、米、麦、大豆などの原料の穀物の表皮が
かなり残っており、バルキングなどの処理不調の活性汚
泥処理にビールのしぼりかす及び又は豆腐のしぼりかす
を添加すると、この表皮に活性汚泥が付着し、更に、水
溶性鉄塩が共存すると、鉄塩、特に、第2鉄塩の凝集作
用により活性汚泥が付着した表皮が凝集して沈降性が良
好なフロックを形成してバルキングが短期間で回復する
ものと思われる。従って、水溶性鉄塩の代わりに活性汚
泥に悪影響しない凝集剤、例えば、ポリ塩化アルミ、高
分子凝集剤なども使用することができる。
The bulking recovery mechanism is considered as follows. Beer squeeze cake and / or tofu squeeze cake has a large amount of the skin of grain, which is a raw material of rice, wheat, soybean, etc. When activated sludge adheres to the skin, and when a water-soluble iron salt coexists, the skin on which the activated sludge adheres due to the aggregating action of iron salt, especially ferric iron, has good sedimentability. It seems that bulking will be recovered in a short period of time by forming various flock. Therefore, instead of the water-soluble iron salt, a coagulant that does not adversely affect the activated sludge, such as polyaluminum chloride or a polymer coagulant, can be used.

【0020】[0020]

【実施例】次に本発明の実施例について説明する。 (実施例1)安水のロダン化合物が分解不良となった活
性汚泥処理の曝気槽にビールのしぼりかすを、曝気槽1
3 当たり、1日に約30〜60g常時添加した。その
結果、ビールのしぼりかす添加後、約5〜7日目後から
分解性が回復し、7〜10日後には分解性がほぼ完全に
回復した。なお、ビールのしぼりかすを添加しない場
合、ロダン化合物の分解性の回復は、約20〜60日間
以上も要した。このことから、ビールのしぼりかすは、
ロダン化合物の分解性の回復を促進する作用があること
が明らかになった。
EXAMPLES Next, examples of the present invention will be described. (Example 1) Beer squeezing residue was aerated in the aeration tank for the activated sludge treatment in which the rhodan compound of the ammonium hydroxide became poorly decomposed.
About 30 to 60 g per m 3 was constantly added per day. As a result, the decomposability was recovered from about 5 to 7 days after the addition of squeezed beer, and the decomposability was recovered almost completely after 7 to 10 days. In addition, when the squeeze residue of beer was not added, recovery of the decomposability of the rhodane compound required about 20 to 60 days or more. From this, the squeeze of beer is
It was revealed that the rhodane compound has an action of promoting recovery of degradability.

【0021】(実施例2)ロダン分解菌を培養するため
の回分式活性汚泥処理の曝気槽にビールのしぼりかす
を、曝気槽1m3 当たり、500〜600g添加した結
果、ロダン化合物濃度300mg/l(as SCN)
の水溶液を24時間以内に分解した。なお、ビールのし
ぼりかすを添加しない場合、同濃度の水溶液を完全に分
解するには96時間以上も要した。このことから、ビー
ルのしぼりかすは、ロダン分解菌を活性化させる作用が
あることが明らかになった。
(Example 2) As a result of adding 500 to 600 g of beer squeeze per 1 m 3 of the aeration tank to the aeration tank of the batch activated sludge treatment for culturing the rhodanic acid-decomposing bacteria, the concentration of the rhodane compound was 300 mg / l. (As SCN)
The aqueous solution of was decomposed within 24 hours. It should be noted that, without adding squeezed beer, it took 96 hours or more to completely decompose the aqueous solution having the same concentration. From this, it was clarified that the squeeze cake of beer had an action of activating the rhodane-decomposing bacteria.

【0022】(実施例3)安水成分(硫化物、シアン)
及び安水活性汚泥処理の過曝気によって生じる亜硫酸イ
オン(NO2-)のロダン分解菌の機能阻害は、ビールの
しぼりかすを添加することによって改善された。
(Example 3) Ammonia component (sulfide, cyanide)
The inhibition of the function of sulfite ion (NO 2 − ) caused by rhodane-decomposing bacteria caused by over-aeration of the activated sludge treatment with amniotic water was improved by the addition of squeezed beer.

【0023】即ち、ロダン分解菌にロダン化合物溶液1
00mg/l(as SCN)を加え、ビールのしぼり
かすを500〜600mg/l添加して振とう培養を行
った結果、硫化物を15mg/l(as S2-)、又
は、シアンイオンを10mg/l、又は、亜硫酸イオン
を20mg/l(as NO2-)添加してもロダン化合
物は、24時間以内に完全に分解した。なお、ビールの
しぼりかすを添加しない場合、S2-を10mg/l、又
は、CN- を10mg/l、又は、NO2-を15mg/
lの添加したときのロダン分解率は、それぞれ38%、
35%と53%である。このことから、S2-、CN-
びNO2-によるロダン分解菌の機能阻害がビールしぼり
かすの添加により改善された。
That is, the rhodane-decomposing bacterium is added to the rhodane compound solution 1
00 mg / l (as SCN) was added, and 500 to 600 mg / l of beer squeezed residue was added and shake culture was performed. As a result, sulfide was 15 mg / l (as S 2- ) or cyanide ion was 10 mg. / l, or a sulfite ion 20mg / l (as NO 2-) thiocyanate compound that may be added are completely degraded within 24 hours. When no beer squeeze is added, S 2- is 10 mg / l, CN - is 10 mg / l, or NO 2- is 15 mg / l.
The rate of decomposition of rhodan when adding 1 is 38%,
35% and 53%. From this, the functional inhibition of the rhodane-degrading bacterium by S 2− , CN and NO 2 was improved by the addition of beer squeezing residue.

【0024】(実施例4)バルキング状態になり、又、
ロダン化合物の分解性などが低下し、処理不調状態にな
った安水の活性汚泥処理の曝気槽に、曝気槽1m3 当た
り、ビールのしぼりかすを、1日に30〜60g、水溶
性鉄塩として塩化第2鉄の水溶液を常時添加した。その
結果、通常はバルキングを回復させるのに約30日から
半年以上を要したが、ビールのしぼりかすと塩化鉄を添
加後、7〜10日目頃から沈降性が良好になり添加後、
15〜20日でバルキング状態が完全に回復した。又、
ロダン化合物の分解性は、添加後5〜10日で向上し、
10〜20日後には完全に回復した。
(Embodiment 4) In the bulking state,
30 to 60 g of beer squeezing powder per day in an aeration tank for activated sludge treatment of annoying water that has been in poor condition due to degradation of the rhodane compound, etc., water-soluble iron salt As a solution, an aqueous solution of ferric chloride was constantly added. As a result, it usually took about 30 days to more than half a year to recover bulking, but after adding beer squeezing powder and iron chloride, the sedimentation property became good from about 7 to 10 days, and after addition,
The bulking condition was completely recovered in 15 to 20 days. or,
The degradability of the rhodan compound improves 5-10 days after addition,
It was completely recovered after 10 to 20 days.

【0025】(実施例5)硫化物を約50mg/l(a
s S2-)含む石油精製工場の廃水を、工場の廃水発生
量の時間的変化に合わせて供給しながら活性汚泥処理を
行った結果、活性汚泥がバルキング状態になり、処理水
のCOD、SS濃度が著しく高くなった。なお、この活
性汚泥処理は、豆腐のしぼりかす(おから)と水溶性鉄
塩を添加しなかった。
Example 5 About 50 mg / l (a of sulfide)
s S 2 ‐ ) wastewater from an oil refinery including s S 2 − ) is treated while supplying it according to the temporal change in the amount of wastewater generated in the factory, resulting in activated sludge in a bulking state, resulting in COD and SS of treated water. The concentration became significantly higher. In this activated sludge treatment, squeezed tofu (okara) and water-soluble iron salt were not added.

【0026】そこで、この活性汚泥処理の曝気槽に豆腐
のしぼりかすを、曝気槽1m3 当たり、1日に約50g
と水溶性鉄塩として塩化第2鉄と硫酸第1鉄の水溶液を
1日に30〜50g(鉄イオンとして)を約30日間毎
日添加した。活性汚泥の沈降性は、豆腐のしぼりかすと
水溶性鉄塩を添加後、約10日目頃から改善され、添加
後15〜20日でバルキング状態が完全に回復した。
Therefore, about 50 g of tofu squeeze debris was added to this activated sludge aeration tank per 1 m 3 of the aeration tank per day.
An aqueous solution of ferric chloride and ferrous sulfate as a water-soluble iron salt was added daily at 30 to 50 g (as iron ions) for about 30 days every day. The sedimentation property of the activated sludge was improved from about 10 days after the addition of the squeeze cake of tofu and the water-soluble iron salt, and the bulking state was completely recovered 15 to 20 days after the addition.

【0027】その後、豆腐のしぼりかすと水溶性鉄塩の
添加を約1ケ月毎に2日に1回、5日に1回、10日に
1回と逐次減らし、最終的には10日に1回の割合で豆
腐のしぼりかすと水溶性鉄塩を添加した結果、バルキン
グが発生せず、良好な処理水質がえられた。
Thereafter, the addition of the squeeze cake of tofu and the water-soluble iron salt is reduced once every two months, once every two days, once every five days, once every ten days, and finally every ten days. As a result of adding tofu squeeze cake and water-soluble iron salt once, bulking did not occur and good treated water quality was obtained.

【0028】このように、バルキングが発生し易い活性
汚泥処理に豆腐のしぼりかすと水溶性鉄塩を一定の間隔
で添加すると、バルキングの発生を抑制し、安定した良
好な活性汚泥処理が可能になった。
As described above, when the tofu squeeze cake and the water-soluble iron salt are added to the activated sludge treatment which tends to cause bulking at regular intervals, the occurrence of bulking is suppressed and a stable and good activated sludge treatment becomes possible. became.

【0029】[0029]

【発明の効果】以上説明したように本発明は、硫化物、
シアン化合物などの活性汚泥の機能を阻害する有害成分
を含む産業廃水を活性汚泥処理法により処理するに当た
り、活性汚泥処理の曝気槽にビールのしぼりかす及び又
は豆腐のしぼりかす、又は、ビールのしぼりかす及び又
は豆腐のしぼりかすと水溶性鉄塩とを添加することによ
り活性汚泥のバルキングの発生、廃水の汚濁成分の分解
不良などの処理不調を短期間に回復させると共に、常時
添加することによりこれらの処理不調を未然に抑制する
ことが可能になった。
As described above, the present invention provides a sulfide,
When processing industrial wastewater containing harmful components that inhibit the function of activated sludge such as cyanide compounds by the activated sludge treatment method, squeeze of beer and / or squeeze of tofu in the aeration tank of activated sludge treatment, or squeeze of beer By adding the dregs and / or tofu squeezed residue and the water-soluble iron salt, it is possible to recover the processing troubles such as the occurrence of bulking of activated sludge and the poor decomposition of polluted components of wastewater in a short period of time, and to add these at all times. It has become possible to suppress the processing failure of.

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 産業廃水の活性汚泥処理において、曝気
槽にビールのしぼりかす及び又は豆腐のしぼりかす(お
から)を添加して、活性汚泥処理を行わせることを特徴
とする産業廃水の活性汚泥処理方法。
1. An activated sludge treatment of industrial wastewater, which comprises adding beer squeeze cake and / or tofu squeeze cake (okara) to an aeration tank to perform activated sludge treatment. Sludge treatment method.
【請求項2】 ビールのしぼりかす及び又は豆腐のしぼ
りかすと水溶性鉄塩を添加する請求項(1) 記載の産業廃
水の活性汚泥処理方法。
2. The method for treating activated sludge of industrial wastewater according to claim 1, wherein the squeezed dregs of beer and / or the squeezed dregs of tofu and a water-soluble iron salt are added.
【請求項3】 産業廃水が活性汚泥の機能を阻害する有
害成分を含む請求項(1) 又は(2) 記載の産業廃水の活性
汚泥処理方法。
3. The method for treating activated sludge of industrial wastewater according to claim 1, wherein the industrial wastewater contains harmful components that inhibit the function of activated sludge.
【請求項4】 上記有害成分がシアン化合物及び又は硫
化物などの還元性硫黄化合物を含む廃水である請求項
(3) 記載の産業廃水の活性汚泥処理方法。
4. The waste water containing the harmful compound as a reducing component such as a cyanide compound and / or a reducing sulfur compound such as a sulfide.
(3) The method for treating activated sludge as described in the industrial wastewater.
【請求項5】 産業廃水がコークス炉から発生する安水
(ガス廃液)である請求項(1) 〜(4) にそれぞれ記載の
産業廃水の活性汚泥処理方法。
5. The method for treating activated sludge of industrial wastewater according to any one of claims 1 to 4, wherein the industrial wastewater is an ammonium hydroxide (gas waste liquid) generated from a coke oven.
【請求項6】 処理不調が発生した安水の活性汚泥処理
を行いかつ回復させる請求項(5) 記載の産業廃水の活性
汚泥処理方法。
6. The method for treating activated sludge of industrial wastewater according to claim 5, wherein the activated sludge treatment of the poor water in which the treatment failure occurs is performed and recovered.
【請求項7】 ビールのしぼりかす及び又は豆腐のしぼ
りかすと第2鉄塩単独、或いは第2鉄塩と第1鉄塩とを
組み合わせた水溶性鉄塩を添加する請求項(6) 記載の産
業廃水の活性汚泥処理方法。
7. A squeeze cake of beer and / or a tofu squeeze cake and a ferric salt alone, or a water-soluble iron salt obtained by combining a ferric salt and a ferrous salt is added. Activated sludge treatment method for industrial wastewater.
JP5262237A 1993-10-20 1993-10-20 Treatment with activated sludge of industrial waste water Pending JPH07112194A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5262237A JPH07112194A (en) 1993-10-20 1993-10-20 Treatment with activated sludge of industrial waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5262237A JPH07112194A (en) 1993-10-20 1993-10-20 Treatment with activated sludge of industrial waste water

Publications (1)

Publication Number Publication Date
JPH07112194A true JPH07112194A (en) 1995-05-02

Family

ID=17372987

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5262237A Pending JPH07112194A (en) 1993-10-20 1993-10-20 Treatment with activated sludge of industrial waste water

Country Status (1)

Country Link
JP (1) JPH07112194A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
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JP2012101201A (en) * 2010-11-12 2012-05-31 Taisei Corp Purification promoting material and purification promoting method
JP2014510632A (en) * 2011-04-11 2014-05-01 ティッセンクルップ・ウーデ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Method and apparatus for biological purification of coke plant wastewater
CN114620831A (en) * 2022-01-26 2022-06-14 四川轻化工大学 Biological promoter and preparation method and application thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007326067A (en) * 2006-06-09 2007-12-20 Kurita Water Ind Ltd Biological treatment accelerator of wastewater and biological treatment method of wastewater using it
JP2011519717A (en) * 2008-04-18 2011-07-14 エコマリネ アーベー How to handle offshore objects
JP2012101201A (en) * 2010-11-12 2012-05-31 Taisei Corp Purification promoting material and purification promoting method
JP2014510632A (en) * 2011-04-11 2014-05-01 ティッセンクルップ・ウーデ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Method and apparatus for biological purification of coke plant wastewater
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