JPH06170378A - Treatment of waste containing phenols and aldehydes - Google Patents

Treatment of waste containing phenols and aldehydes

Info

Publication number
JPH06170378A
JPH06170378A JP34527592A JP34527592A JPH06170378A JP H06170378 A JPH06170378 A JP H06170378A JP 34527592 A JP34527592 A JP 34527592A JP 34527592 A JP34527592 A JP 34527592A JP H06170378 A JPH06170378 A JP H06170378A
Authority
JP
Japan
Prior art keywords
aldehydes
phenol
phenols
treatment
sulfuric acid
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
JP34527592A
Other languages
Japanese (ja)
Inventor
Shingo Sasaki
新吾 佐佐木
Rikunori Yamao
陸矩 山尾
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.)
Unitika Ltd
Original Assignee
Unitika 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 Unitika Ltd filed Critical Unitika Ltd
Priority to JP34527592A priority Critical patent/JPH06170378A/en
Publication of JPH06170378A publication Critical patent/JPH06170378A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To purify waste water containing phenols and aldehydes in high concn. to reduce the concn. of phenols and aldehydes to specific low concn. CONSTITUTION:0.1-5wt.% of sulfuric acid and 0.1-5wt.% of gum arabic are added to waste water containing phenol and formaldehyde in high concn. and this waste water is heated at 70-100 deg.C under stirring to reduce the concn. of phenol and formaldehyde to below 1,000ppm.

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、フェノール・アルデヒ
ド類含有廃水の処理法に関し、詳しくは主としてフェノ
ール樹脂製造工程で発生するフェノール・アルデヒド類
含有廃水を効率的に廃水処理するための前処理方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating wastewater containing phenol / aldehydes, and more particularly to a pretreatment method for efficiently treating wastewater containing phenol / aldehydes mainly generated in a phenol resin production process. Regarding

【0002】[0002]

【従来の技術】フェノール類及びアルデヒド類を含有す
る廃水(以下、フェノール・アルデヒド類含有廃水と称
する)を廃水処理する方法として、従来、特公昭60−
15397号公報に記載のようなバクテリア処理法(活
性汚泥法)が一般的に用いられている。
2. Description of the Related Art As a method for treating wastewater containing phenols and aldehydes (hereinafter referred to as phenol / aldehyde-containing wastewater), there is a conventional method as disclosed in JP-B-60-
The bacterial treatment method (activated sludge method) as described in Japanese Patent No. 15397 is generally used.

【0003】ところが活性汚泥法によるフェノール・ア
ルデヒド類含有廃水の廃水処理は、特にフェノール類が
高濃度で存在する場合、バクテリアが死滅する懸念が大
きため、フェノール類等を含有しない多量の水で希釈す
る等の処置が必要となり、処理効率が極めて悪くなり,
処理コストが高価となる。
However, in the wastewater treatment of wastewater containing phenol / aldehydes by the activated sludge method, there is a great concern that bacteria will be killed, especially when phenols are present at a high concentration. It becomes necessary to take measures such as
The processing cost is high.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記のよう
な状況に鑑み、主として、水系でフェノール樹脂を製造
する際、発生するフェノール類及びアルデヒド類を高濃
度で含有する廃水を廃水量を増やすことなく、残査等の
処理も容易な効率的前処理法を提供することを目的とす
るものである。
SUMMARY OF THE INVENTION In view of the above situation, the present invention mainly aims at reducing the amount of waste water containing a high concentration of phenols and aldehydes generated when a phenol resin is produced in an aqueous system. It is an object of the present invention to provide an efficient pretreatment method in which it is possible to easily treat residual substances without increasing the amount.

【0005】[0005]

【課題を解決するための手段】本発明は、このような課
題を解決するために鋭意研究の結果、到達したものであ
る。すなわち、本発明は、フェノール類及びアルデヒド
類を1,000ppm以上の高濃度で含有する廃水に、廃水重量
に対し、0.1 〜5重量%の硫酸及び0.1 〜5重量%のア
ラビアゴムを加え、70〜100 ℃で加熱、攪拌することを
特徴とするフェノール・アルデヒド類含有廃水の処理法
を要旨とするものである。
The present invention has been achieved as a result of earnest research for solving such problems. That is, according to the present invention, 0.1 to 5% by weight of sulfuric acid and 0.1 to 5% by weight of gum arabic are added to a wastewater containing phenols and aldehydes at a high concentration of 1,000 ppm or more, to 70 to 70% by weight. The gist is a method for treating wastewater containing phenol / aldehydes, which is characterized by heating and stirring at 100 ° C.

【0006】以下、本発明を詳細に説明する。本発明の
方法にて処理の対象とするフェノール・アルデヒド類含
有廃水はフエノール樹脂製造工程にて排出されるフェノ
ール類及びアルデヒド類を1,000ppm以上の高濃度で含有
する廃水であって, フェノール類としてはフェノールあ
るいはフェノール誘導体であり、このフェノール誘導体
としては、例えば、m−クレゾール、p−ter−ブチ
ルフェノール、o−プロピルフェノール、レゾルシノー
ル、ビスフェノールA等が挙げられ、これらの1種また
は2種以上の混合物が含まれる。また、アルデヒド類と
しては、例えば、ホルムアルデヒド、パラホルムアルデ
ヒド、アセトアルデヒド、フルフラール等が挙げられ、
これらの1種または2種以上の混合物が含まれる。な
お、これら主原料以外にアンモニア水、ヘキサメチレン
テトラミン、ジメチルアミン、塩酸、硫酸等の触媒、ポ
リビニールアルコール等のエマルジョン安定剤等の副原
料及び添加剤、並びにフェノール類とアルデヒド類との
反応によって生成した水媒体に可溶性のレゾール、ノボ
ラック等の低分子量フェノール・アルデヒド縮合物(フ
ェノール樹脂中間体、副生物)も含まれる。
The present invention will be described in detail below. The phenol / aldehyde-containing wastewater to be treated by the method of the present invention is a wastewater containing phenols and aldehydes discharged in the phenol resin manufacturing process at a high concentration of 1,000 ppm or more. Is phenol or a phenol derivative, and examples of this phenol derivative include m-cresol, p-ter-butylphenol, o-propylphenol, resorcinol, bisphenol A, and the like, or a mixture of one or more of these. Is included. Examples of aldehydes include formaldehyde, paraformaldehyde, acetaldehyde, furfural, and the like.
A mixture of one or more of these is included. In addition to these main raw materials, catalysts such as ammonia water, hexamethylenetetramine, dimethylamine, hydrochloric acid and sulfuric acid, auxiliary raw materials and additives such as emulsion stabilizers such as polyvinyl alcohol, and reaction between phenols and aldehydes It also contains low molecular weight phenol-aldehyde condensates (phenolic resin intermediates, by-products) such as resole and novolac, which are soluble in the produced aqueous medium.

【0007】本発明の方法にて添加する硫酸は稀硫酸、
濃硫酸、発煙硫酸のいづれでもよく、その添加量は、発
煙硫酸に換算して廃水重量に対し0.1 〜5重量%が好ま
しい。硫酸の添加量が、0.1 重量%未満では、重合速度
が小さく、短時間でフェノール含有量を1.000ppm未満ま
で低減させることができない。また5重量%を越えても
重合速度がさらに大きくなることはなく、他方、中和に
要するアルカリ消費量が増え、環境汚染の面でも、処理
コストの面でも好ましくない。
The sulfuric acid added in the method of the present invention is diluted sulfuric acid,
Either concentrated sulfuric acid or fuming sulfuric acid may be used, and the addition amount thereof is preferably 0.1 to 5% by weight in terms of fuming sulfuric acid, based on the weight of waste water. If the addition amount of sulfuric acid is less than 0.1% by weight, the polymerization rate is low and the phenol content cannot be reduced to less than 1.000 ppm in a short time. Further, even if it exceeds 5% by weight, the polymerization rate does not further increase, and on the other hand, the alkali consumption required for neutralization increases, which is not preferable in terms of environmental pollution and treatment cost.

【0008】他方、本発明の方法にて添加するアラビア
ゴムは豆科植物Acacia senegal Willd等の樹液由来の
天然アラビアゴム, これらを加工処理した半合成アラビ
アゴム, あるいは合成ゴムラッテックス由来の合成アラ
ビアゴムであって、その添加量は、フェノール含有量に
対して0.1 〜5重量%の量が好ましい。この添加量が、
0.1 重量%未満では、加熱、攪拌によって生成するフェ
ノール樹脂が独立した粒子を維持できなくなり、粘調な
塊となり攪拌翼等に付着して後処理が困難となる。ま
た、5重量%越えてアラビアゴムを加えても形成される
フェノール樹脂粒子の安定性に差はなく、他方、活性汚
泥法等の最終処理工程での負荷が高くなり好ましくな
い。
On the other hand, the gum arabic added by the method of the present invention is natural gum arabic derived from sap of legume Acacia senegal Willd, semi-synthetic gum arabic obtained by processing these, or synthetic gum arabic derived from synthetic rubber latex. The rubber is preferably added in an amount of 0.1 to 5% by weight based on the phenol content. This added amount is
If it is less than 0.1% by weight, the phenol resin produced by heating and stirring cannot maintain independent particles, and it becomes a viscous mass and adheres to the stirring blades and the like, which makes post-treatment difficult. Further, even if the amount of gum arabic exceeds 5% by weight, there is no difference in stability of the phenol resin particles formed, and on the other hand, the load in the final treatment step such as the activated sludge method becomes high, which is not preferable.

【0009】上記硫酸及びアラビアゴムの添加は、通常
室温にて攪拌しつつ、廃水に対して一度にまとめて行う
方法、徐々に注入する方法あるいは段階的に行う方法の
いずれかの方法にて行う。この水を70〜100 ℃で0.5 〜
5時間加熱、攪拌し、室温まで冷却する。
The above-mentioned addition of sulfuric acid and gum arabic is usually carried out at a room temperature while stirring, and is carried out by any one of a method in which the waste water is added all at once, a method in which it is gradually injected or a method in which it is carried out stepwise. . Add this water at 70-100 ° C for 0.5-
Heat and stir for 5 hours, then cool to room temperature.

【0010】本発明の方法により1,000ppm以上の高濃度
で溶存していたフェノール類及びアルデヒド類は大部分
が急速に重合するとともに水媒体より析出・凝集し、固
液分離の容易な微粒子状のフェノール樹脂となって水媒
体中に沈澱あるいは分散する。かくして、この微粒子状
フェノール樹脂を濾過、遠心分離等の分離手段にて分離
することによりフェノール類及びアルデヒド類の濃度が
1,000ppm以下の廃水となる。なお、処理前の廃水中のフ
ェノール類とアルデヒド類とがそれらの当量に対してい
ずれかが著しく偏っている場合は、不足している成分を
ほぼ当量に達するまで追加して後、本発明の方法を適用
するのが好ましい。
According to the method of the present invention, most of the phenols and aldehydes dissolved at a high concentration of 1,000 ppm or more polymerize rapidly and precipitate / aggregate from an aqueous medium to form fine particles that are easy to solid-liquid separate. It becomes a phenol resin and precipitates or disperses in an aqueous medium. Thus, the concentration of phenols and aldehydes can be reduced by separating this particulate phenol resin with a separating means such as filtration or centrifugation.
Waste water of 1,000ppm or less. If any of the phenols and aldehydes in the wastewater before treatment is significantly biased with respect to their equivalents, the deficient components are added until they almost reach the equivalents, and then the Preference is given to applying the method.

【0011】このように前処理した1.000ppm未満のフェ
ノールを含有する廃水は、活性汚泥法、活性炭吸着法、
化学酸化法等の従来公知の最終水処理法を効率的に適用
することにより高度に純化された無害の処理水となって
河川・海等の天然水系に還元することができる。
Wastewater containing less than 1.000 ppm of phenol pretreated in this way is treated by an activated sludge method, an activated carbon adsorption method,
By efficiently applying a conventionally known final water treatment method such as a chemical oxidation method, highly purified harmless treated water can be reduced to a natural water system such as a river or sea.

【0012】[0012]

【実施例】次に、本発明を実施例によって具体的に説明
する。なお、以下各例にて廃水中あるいは処理水中のフ
ェノール及びホルムアルデヒド含有量は、以下の方法で
測定した。 フェノール:JIS−K0102−86−28−1・2
に基づいて4−アミノアンチピリン吸光光度法により測
定。 ホルムアルデヒド:JIS−K0102−86−29−
1に基づいてアセチルアセトン吸光光度法により測定。
EXAMPLES Next, the present invention will be specifically described with reference to examples. In addition, the content of phenol and formaldehyde in waste water or treated water in each of the following examples was measured by the following method. Phenol: JIS-K0102-86-28-1.2
Based on 4-aminoantipyrine absorptiometry. Formaldehyde: JIS-K0102-86-29-
Measured by acetylacetone absorptiometry based on 1.

【0013】実施例1〜4 フェノールとホルマリンより塩基性触媒下に水系エマル
ジョン重合にてフェノール樹脂を調製した反応液を、遠
心分離にかけ微粒子状の樹脂分を固液分離して、残った
フェノール・ホルムアルデヒド含有廃水(特性を表1に
示す。)をグラスライニング反応缶に採り、表1に示す
量の硫酸及びアラビアゴムを加えて3時間95℃で加
熱、攪拌した。反応終了後、PH6〜7に中和し、凝集
沈澱したフェノール樹脂粒子を濾別後濾液中のフェノー
ル及びホルムアルデヒド濃度を定量分析して表1に示す
結果を得た。
Examples 1 to 4 A reaction solution prepared by phenol-formalin formalin by a water-based emulsion polymerization in the presence of a basic catalyst was subjected to centrifugation to solid-liquid separate fine-particle resin components, and the remaining phenol Formaldehyde-containing wastewater (characteristics are shown in Table 1) was placed in a glass-lined reaction can, sulfuric acid and gum arabic in the amounts shown in Table 1 were added, and the mixture was heated and stirred at 95 ° C. for 3 hours. After completion of the reaction, the phenol resin particles were neutralized to pH 6 to 7, and the phenol resin particles coagulated and precipitated were separated by filtration and the phenol and formaldehyde concentrations in the filtrate were quantitatively analyzed to obtain the results shown in Table 1.

【0014】比較例1、2 実施例1と同様に、ただし硫酸及びアラビアゴムを表1
に示す量に変えて、フェノール及びホルムアルデヒド含
有廃水の処理を行い表1に示す結果を得た。
Comparative Examples 1 and 2 As in Example 1, except that sulfuric acid and gum arabic were used.
The amount shown in Table 1 was changed and the wastewater containing phenol and formaldehyde was treated to obtain the results shown in Table 1.

【0015】[0015]

【表1】 [Table 1]

【0016】表1から明らかなように、本発明の方法
(実施例1・2)は、高濃度にフェノール及びホルムア
ルデヒドを含有する廃水を容易に1.000ppm未満に低減せ
しめる極めて効率的な前処理方法であることが明らかで
ある。
As is clear from Table 1, the method of the present invention (Examples 1 and 2) is an extremely efficient pretreatment method for easily reducing the waste water containing phenol and formaldehyde at a high concentration to less than 1.000 ppm. It is clear that

【0017】[0017]

【発明の効果】本発明は、高濃度にフェノール及びホル
ムアルデヒドを含有する廃水を安価、かつ効率的に処理
して両成分が顕著に除去された処理水とすることができ
る優れた廃水処理法であり、この処理水を通常の活性汚
泥法等の二次処理を行うことにより、完全に浄化された
水に還元することができる。
INDUSTRIAL APPLICABILITY The present invention provides an excellent wastewater treatment method capable of treating wastewater containing a high concentration of phenol and formaldehyde at low cost and efficiently to obtain treated water from which both components have been significantly removed. Yes, this treated water can be reduced to completely purified water by performing a secondary treatment such as an ordinary activated sludge method.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 フェノール類及びアルデヒド類を1,000p
pm以上の濃度で含む廃水を処理するにあたり、廃水重量
に対し0.1 〜5重量%の硫酸及び0.1 〜5重量%のアラ
ビアゴムを添加し70〜100 ℃で加熱、攪拌することを特
徴とするフェノール・アルデヒド類含有廃水の処理法。
1. The amount of phenols and aldehydes is 1,000 p
Phenol characterized by adding 0.1 to 5% by weight of sulfuric acid and 0.1 to 5% by weight of gum arabic and agitating at 70 to 100 ° C. and treating the wastewater containing at a concentration of pm or more with respect to the weight of the wastewater -Treatment method for wastewater containing aldehydes.
JP34527592A 1992-11-30 1992-11-30 Treatment of waste containing phenols and aldehydes Pending JPH06170378A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34527592A JPH06170378A (en) 1992-11-30 1992-11-30 Treatment of waste containing phenols and aldehydes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34527592A JPH06170378A (en) 1992-11-30 1992-11-30 Treatment of waste containing phenols and aldehydes

Publications (1)

Publication Number Publication Date
JPH06170378A true JPH06170378A (en) 1994-06-21

Family

ID=18375494

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34527592A Pending JPH06170378A (en) 1992-11-30 1992-11-30 Treatment of waste containing phenols and aldehydes

Country Status (1)

Country Link
JP (1) JPH06170378A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101899137A (en) * 2010-04-15 2010-12-01 河南许绝电工绝缘材料有限公司 Method for producing phenolic insulating resin
CN109306043A (en) * 2018-09-20 2019-02-05 吉林大学 A kind of method that biomass power generation Sewage treatment containing phenolic tar utilizes
CN113816563A (en) * 2021-09-30 2021-12-21 天津正达科技有限责任公司 Treatment method of phenol-containing wastewater in coal chemical industry

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101899137A (en) * 2010-04-15 2010-12-01 河南许绝电工绝缘材料有限公司 Method for producing phenolic insulating resin
CN109306043A (en) * 2018-09-20 2019-02-05 吉林大学 A kind of method that biomass power generation Sewage treatment containing phenolic tar utilizes
CN113816563A (en) * 2021-09-30 2021-12-21 天津正达科技有限责任公司 Treatment method of phenol-containing wastewater in coal chemical industry

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