JPH06126288A - Method of removing biologically hardly degradable material - Google Patents

Method of removing biologically hardly degradable material

Info

Publication number
JPH06126288A
JPH06126288A JP27607292A JP27607292A JPH06126288A JP H06126288 A JPH06126288 A JP H06126288A JP 27607292 A JP27607292 A JP 27607292A JP 27607292 A JP27607292 A JP 27607292A JP H06126288 A JPH06126288 A JP H06126288A
Authority
JP
Japan
Prior art keywords
substance
ozone
biologically
group
water
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
JP27607292A
Other languages
Japanese (ja)
Inventor
勝利 ▲猜▼山
Katsutoshi Abeyama
Tamotsu Tanaka
保 田中
Hidenori Harauchi
秀教 原内
Kazutaka Akai
一隆 赤井
Hideki Jimi
秀樹 自見
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.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
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 Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP27607292A priority Critical patent/JPH06126288A/en
Publication of JPH06126288A publication Critical patent/JPH06126288A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently remove by treating with ozone for an aqueous liquid containing a hardly degradable material having a specific physical and chemical property, in treatment of waste water, etc., at production of a coke. CONSTITUTION:The aqueous liquid incorporating a phenolic hydroxy group, a carboxylic group, a sulfo group, a nitro group and an ester group in the molecule whose weight average molecular weight is about 1000-1500 and being water-soluble and forming an acid and hygroscopic precipitate in acidic condition and also containing the biologically hardly degradable material, is treated with ozone. In this case, the ozone concentration, aeration speed and treatment time, etc., are selected such that the ozone quantity for one l treating water is about >=100mg.

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、水溶液中に含まれる生
物学的に難分解性の物質を分解・除去する方法に関する
ものである。詳しくは、コークスの製造工程で排出され
る廃水中に含まれる生物学的難分解性物質の分解・除去
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 decomposing / removing a biologically persistent substance contained in an aqueous solution. More specifically, it relates to the decomposition and removal of biologically difficult-to-decompose substances contained in the wastewater discharged in the coke manufacturing process.

【0002】[0002]

【従来の技術】コークスを製造する工程において、原料
炭の乾留の際に留出するコークス炉ガス(COG)やタ
ール等は水で冷却されそれぞれの用途に供せられる。そ
のときにアンモニア含量の多い液が排出される。この排
出液は安水とよばれ、通常、6,000ppm程度のア
ンモニアを含有している。
2. Description of the Related Art In the process of producing coke, coke oven gas (COG), tar, and the like that are distilled off during dry distillation of raw coal are cooled with water and used for their respective purposes. At that time, a liquid having a high ammonia content is discharged. This effluent is called ammonium hydroxide and usually contains about 6,000 ppm of ammonia.

【0003】かかる安水には、アンモニアのほか多量の
フェノールやクレゾール等のフェノール類、シアン化
物、硫化物等々種々の物質が含有されている。通常、安
水は、工業用水や海水等で約4〜5倍程度に希釈し、活
性汚泥(分裂菌類、鞭毛虫類、繊毛虫類等)による生物
的処理に付され、安水中のフェノール類などの含有物質
が分解除去されている。
In addition to ammonia, the ammonium hydroxide contains a large amount of various substances such as phenol, cresol and other phenols, cyanide, sulfide and the like. Usually, anhydrous water is diluted about 4 to 5 times with industrial water or seawater, and is subjected to biological treatment with activated sludge (fission bacteria, flagellates, ciliates, etc.) The contained substances such as are decomposed and removed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、コーク
ス製造工程から排出される安水中に含まれる物質は、原
料炭の乾留条件等で異なり一定ではないため、活性汚泥
の負荷変動となり、活性汚泥の活性に大きく影響してい
る。また、活性汚泥による安水中の含有物質の分解除去
率には限界があり、安水の廃水処理における問題となっ
ている。
However, since the substances contained in the ammonium hydroxide discharged from the coke manufacturing process are not constant because they differ depending on the conditions such as the carbonization conditions of the raw coal, the load of the activated sludge changes and the activity of the activated sludge is changed. Have a great influence on. In addition, there is a limit to the decomposition and removal rate of the substances contained in the ammonium hydroxide by activated sludge, which is a problem in the wastewater treatment of ammonium hydroxide.

【0005】[0005]

【課題を解決するための手段】本発明者らは、活性汚泥
により分解除去できない生物学的難分解性物質を安水か
ら分解・除去する方法を提供すべく種々検討し、先ず活
性汚泥により分解除去できない成分の特定化を行った。
その結果、その中で多くを占める物質についての理化学
的性質を明らかにした。すなわち該生物学的難分解性物
質の除去方法について検討した結果、該物質含有水溶液
を特定の条件下にオゾン処理することによって該生物学
的難分解性物質を効率的に分解・除去することができる
こと、更に該難分解性物質とは異なる原因による、該水
溶液の着色物質を効率よく脱色除去できることを見出し
本発明を完成するに到った。
[Means for Solving the Problems] The inventors of the present invention have made various studies to provide a method for decomposing / removing biologically difficult-to-decompose substances that cannot be decomposed and removed by activated sludge from aminated water. The components that cannot be removed were specified.
As a result, the physicochemical properties of the substances that occupy most of them were clarified. That is, as a result of examining a method for removing the biologically difficult-to-decompose substance, it is possible to efficiently decompose and remove the biologically difficult-to-decompose substance by subjecting the aqueous solution containing the substance to ozone treatment under specific conditions. The present inventors have completed the present invention by finding that they can be performed, and that the coloring substance in the aqueous solution can be efficiently decolorized and removed due to a cause different from that of the hardly decomposable substance.

【0006】即ち、本発明の要旨は、少なくとも、下記
(a)〜(e)の理化学的性質 (a)重量平均分子量が、約1,000〜1,500 (b)分子中にフェノール性水酸基、カルボキシル基、
スルホン酸基またはニトロ基を有する (c)分子中にエステル結合を有する (d)水に可溶で、酸性条件で沈澱物を生成する (e)上記沈澱物は酸性で、吸湿性を示す を有し、生物学的に難分解性の物質を含有する水溶液か
ら、該物質を除去する方法であって、該生物学的難分解
性物質を含有する水溶液をオゾンで処理することによっ
て、該物質を分解・除去することを特徴とする生物学的
難分解性物質の除去方法に存する。
That is, the gist of the present invention is at least the following physicochemical properties (a) to (e) (a) a weight average molecular weight of about 1,000 to 1,500 (b) a phenolic hydroxyl group in the molecule. , Carboxyl group,
Having a sulfonic acid group or a nitro group (c) Having an ester bond in the molecule (d) Soluble in water to form a precipitate under acidic conditions (e) The precipitate is acidic and exhibits hygroscopicity A method for removing a biologically difficult-to-decompose substance-containing aqueous solution containing the biologically difficult-to-decompose substance by treating the aqueous solution containing the biologically-hardly-decomposable substance with ozone. And a method for removing a biologically difficult-to-decompose substance, which is characterized by decomposing / removing.

【0007】以下本発明を説明するに、本発明で処理す
る水溶液には少なくとも上記(a)〜(e)の理化学的
性質を有する生物学的難分解性物質を含有する。本発明
における生物学的難分解性物質は、過酸化水素や酸素な
どの酸化剤による酸化や200℃での加熱によって分解
されず、水蒸気によるストリッピング処理で釜残に濃縮
される。
The present invention will be described below. The aqueous solution treated in the present invention contains at least the biologically difficult-to-decompose substance having the physicochemical properties (a) to (e). The biologically difficult-to-decompose substance in the present invention is not decomposed by oxidation with an oxidizing agent such as hydrogen peroxide or oxygen or heating at 200 ° C., and is concentrated in the bottom of the pot by stripping treatment with steam.

【0008】本発明における生物学的難分解性物質の化
学構造は不明であるが、たとえば、元素分析値の結果
(C=21.6%,H=4.9%,N=9.8%,灰分
=2.7%,その他=61%)、X線マイクロアナライ
ザーの結果(硫黄を検出)、IRスペクトル(KBr錠
剤成型法)の結果(図1)、更には、 1H−NMRおよ
13C−NMR〔溶媒:ジメチルスルホキシド(DMS
O)の結果(図2および図3)〕から、下記に示す様な
官能基を有するベンゼン環の縮合物と推定される。
Although the chemical structure of the biologically difficult-to-decompose substance in the present invention is unknown, for example, the result of elemental analysis (C = 21.6%, H = 4.9%, N = 9.8%). , Ash content = 2.7%, others = 61%), X-ray microanalyzer result (sulfur is detected), IR spectrum (KBr tableting method) result (FIG. 1), 1 H-NMR and 13 C-NMR [solvent: dimethyl sulfoxide (DMS
From the results of O) (FIGS. 2 and 3)], it is presumed that the condensation product is a benzene ring having a functional group as shown below.

【0009】[0009]

【化1】 −OH −COOH −NO2 及び/又は −SO3 H −NOH また、GPS(カラム「Asahipak GS-310H」、カラム温
度40℃、溶離液;アセトニトリル/水=40/60、
検量線;ポリエチレングリコール)での分析による重量
平均分子量は約1,000〜1,500である。
Embedded image --OH --COOH --NO 2 and / or --SO 3 H --NOH Also, GPS (column “Asahipak GS-310H”, column temperature 40 ° C., eluent; acetonitrile / water = 40/60,
The calibration curve; polyethylene glycol) has a weight average molecular weight of about 1,000 to 1,500.

【0010】具体的には、コークスの製造工程において
排出されるCOGやタール等の冷却処理水である安水等
が挙げられる。安水には、通常、6,000〜6,50
0ppmのアンモニア、COD換算で約4,000〜
5,000ppmのフェノールやクレゾール等のフェノ
ール類が主成分として含まれ、そのほか、COD換算で
約500〜700ppmのシアン化合物、約300〜4
00ppmの本発明における生物学的難分解性物質およ
び約700〜1,000ppmの構造未知の生物学的易
分解性物質等がマイナー成分として含まれている。
[0010] Specifically, there is an example of cold water such as COG or tar discharged in the coke manufacturing process, which is cold water. For cheap water, it is usually 6,000 to 6,50
0ppm ammonia, COD conversion approximately 4,000-
Phenols such as 5,000 ppm and cresol are contained as main components, and in addition, about 500 to 700 ppm of cyanide compound in COD conversion, about 300 to 4
The biologically degradable substance of the present invention of 00 ppm and the biologically easily degradable substance of unknown structure of about 700 to 1,000 ppm are contained as minor components.

【0011】安水を処理する場合、予め常法に従って活
性汚泥処理によってフェノールやクレゾール等の主成分
を分解除去しておいてもよい。その際の活性汚泥として
は、フェノールやクレゾール等を分解する前述のような
菌を使用し、通常、工業用水や海水等で約4〜5倍程度
に希釈し、30〜40℃の温度で反応させ、次いで、沈
降分離して上澄液を得る。
In the case of treating ammonium hydroxide, the main components such as phenol and cresol may be decomposed and removed in advance by an activated sludge treatment according to a conventional method. As the activated sludge at this time, the above-mentioned bacteria that decompose phenol, cresol and the like are used, and usually diluted with industrial water or seawater to about 4 to 5 times and reacted at a temperature of 30 to 40 ° C. Then, sedimentation separation is performed to obtain a supernatant.

【0012】かかる水溶液の本発明におけるオゾン処理
は、処理水1リットル当りオゾン量が100mg以上、
好ましくは、200mg以上、特に好ましくは、400
〜1000mgとなるように、適宜オゾン濃度、通気速
度、処理時間等を選択して行う。処理水の温度は、通
常、25〜40℃程度で行えばよい。上記のようなオゾ
ン処理によって通常40〜60%の該物質を、分離除去
することができる。更に本発明においては後述の実施例
(図4)に示すように、処理水溶液の着色物質をも80
〜98%程度脱色除去することができる。
In the ozone treatment of the present invention for such an aqueous solution, the amount of ozone per liter of treated water is 100 mg or more,
Preferably 200 mg or more, particularly preferably 400
The ozone concentration, the aeration rate, the treatment time, etc. are appropriately selected so that the amount becomes about 1000 mg. The temperature of the treated water is usually about 25 to 40 ° C. By the ozone treatment as described above, usually 40 to 60% of the substance can be separated and removed. Further, in the present invention, as shown in the below-mentioned Example (FIG. 4), the coloring substance in the treatment aqueous solution is also added to 80%.
Approximately 98% can be decolorized and removed.

【0013】[0013]

【実施例】以下に実施例を挙げて更に本発明を具体的に
説明する。 実施例1.コークス製造工程から排出された安水を海水
で4倍に希釈して、30〜35℃にて約16時間攪拌下
に活性汚泥処理し、沈降分離して上澄液(pH8.3)
を得た。得られた上澄液を高速液体クロマトグラフィー
(HPLC:カラム「Nucleosil 100 」、カラム温度4
0℃、溶離液;アセトニトリル/水=40/60)で分
析した結果、処理前の安水中に含まれていたフェノー
ル、クレゾール、キシレノール類のピークは消失してい
た。
EXAMPLES The present invention will be described in more detail with reference to the following examples. Example 1. The ammonium hydroxide discharged from the coke production process is diluted 4 times with seawater, treated with activated sludge under stirring at 30 to 35 ° C. for about 16 hours, sedimented and separated to obtain a supernatant (pH 8.3).
Got The obtained supernatant was subjected to high performance liquid chromatography (HPLC: column "Nucleosil 100", column temperature 4
As a result of analysis at 0 ° C., eluent: acetonitrile / water = 40/60), the peaks of phenol, cresol, and xylenol contained in the untreated water before treatment disappeared.

【0014】かかる上澄液にオゾンを上澄液1リットル
当り0mg〜1500mgとなるように通気した。次い
で、オゾン処理液の吸光度(460nm)および生物学
的難分解性物質の割合の変化(CODMn値)を測定し
た。その結果を図4に示した。図4から明らかなよう
に、オゾン処理することにより従来除去することができ
なかった生物学的に難分解性の物質を分解除去できるこ
とがわかる。また、淡黄色に着色している上澄液の脱色
も同時にできることがわかる。
Ozone was aerated through the supernatant so that the amount of ozone was 0 to 1500 mg per liter of the supernatant. Then, the absorbance (460 nm) of the ozone-treated solution and the change in the proportion of the biologically difficult-to-decompose substance (COD Mn value) were measured. The results are shown in Fig. 4. As is clear from FIG. 4, it can be seen that the biologically difficult-to-decompose substance that could not be removed by the ozone treatment can be decomposed and removed by the ozone treatment. Further, it can be seen that decolorization of the supernatant liquid colored in pale yellow can be performed at the same time.

【0015】[0015]

【発明の効果】本発明の方法によれば、活性汚泥処理等
の生物学的方法により分解除去できなかった成分の内の
大部分を占める上記理化学的性質を有する生物学的難分
解性物質を除去し、その含有量を低減することができ
る。
EFFECTS OF THE INVENTION According to the method of the present invention, a biologically difficult-to-decompose substance having the above-mentioned physicochemical properties, which accounts for most of the components that cannot be decomposed and removed by a biological method such as activated sludge treatment, is obtained. It can be removed and its content can be reduced.

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

【図1】本発明における生物学的難分解性物質のIRス
ペクトル
FIG. 1 is an IR spectrum of a biologically persistent substance according to the present invention.

【図2】同物質の 1H−NMR分析結果を示す。FIG. 2 shows the 1 H-NMR analysis result of the same substance.

【図3】同物質の13C−NMR分析結果を示す。FIG. 3 shows the 13 C-NMR analysis result of the same substance.

【図4】安水の活性汚泥処理液のオゾン処理における吸
光度(460nm)および生物学的難分解性物質の残存
量の変化を示す。
FIG. 4 shows changes in absorbance (460 nm) and residual amount of biologically difficult-to-decompose substance in ozone treatment of an activated sludge treatment liquid of ammonium hydroxide.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 赤井 一隆 香川県坂出市番の州町1番地 三菱化成株 式会社坂出工場内 (72)発明者 自見 秀樹 香川県坂出市番の州町1番地 三菱化成株 式会社坂出工場内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazutaka Akai No. 1 Kyushu Town, Sakaide City, Kagawa Prefecture Mitsubishi Chemical Co., Ltd. Sakaide Factory (72) Inventor Hideki Hidemi No. 1, No. 1 Town Town, Sakaide City, Kagawa Prefecture Mitsubishi Kasei Corporation Ceremony company Sakaide factory

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 少なくとも、下記(a)〜(e)の理化
学的性質 (a)重量平均分子量が、約1,000〜1,500 (b)分子中にフェノール性水酸基、カルボキシル基、
スルホン酸基またはニトロ基を有する (c)分子中にエステル結合を有する (d)水に可溶で、酸性条件で沈澱物を生成する (e)上記沈澱物は酸性で、吸湿性を示す を有し、生物学的に難分解性の物質を含有する水溶液か
ら、該物質を除去する方法であって、該生物学的難分解
性物質を含有する水溶液をオゾンで処理することによっ
て、該物質を分解・除去することを特徴とする生物学的
難分解性物質の除去方法。
1. At least the following physicochemical properties (a) to (e): (a) a weight average molecular weight of about 1,000 to 1,500 (b) a phenolic hydroxyl group or a carboxyl group in the molecule;
Having a sulfonic acid group or a nitro group (c) Having an ester bond in the molecule (d) Soluble in water to form a precipitate under acidic conditions (e) The precipitate is acidic and exhibits hygroscopicity A method for removing a biologically difficult-to-decompose substance-containing aqueous solution containing the biologically difficult-to-decompose substance by treating the aqueous solution containing the biologically-hardly-decomposable substance with ozone. A method for removing a biologically difficult-to-decompose substance, which comprises decomposing / removing.
【請求項2】 生物学的難分解性物質含有水溶液が、コ
ークス製造工程から排出される安水である請求項1記載
の除去方法。
2. The removal method according to claim 1, wherein the aqueous solution containing a biologically difficult-to-decompose substance is ammonium hydroxide discharged from the coke manufacturing process.
JP27607292A 1992-10-14 1992-10-14 Method of removing biologically hardly degradable material Pending JPH06126288A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27607292A JPH06126288A (en) 1992-10-14 1992-10-14 Method of removing biologically hardly degradable material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27607292A JPH06126288A (en) 1992-10-14 1992-10-14 Method of removing biologically hardly degradable material

Publications (1)

Publication Number Publication Date
JPH06126288A true JPH06126288A (en) 1994-05-10

Family

ID=17564414

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27607292A Pending JPH06126288A (en) 1992-10-14 1992-10-14 Method of removing biologically hardly degradable material

Country Status (1)

Country Link
JP (1) JPH06126288A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6589432B2 (en) 1999-11-10 2003-07-08 Nec Electronics Corporation Method and apparatus for processing biologically hardly degradable waste water capable of reducing ozone
JP2008504111A (en) * 2004-06-28 2008-02-14 レクティセル Purification method of contaminated water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6589432B2 (en) 1999-11-10 2003-07-08 Nec Electronics Corporation Method and apparatus for processing biologically hardly degradable waste water capable of reducing ozone
JP2008504111A (en) * 2004-06-28 2008-02-14 レクティセル Purification method of contaminated water

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