JPS631114B2 - - Google Patents

Info

Publication number
JPS631114B2
JPS631114B2 JP55027345A JP2734580A JPS631114B2 JP S631114 B2 JPS631114 B2 JP S631114B2 JP 55027345 A JP55027345 A JP 55027345A JP 2734580 A JP2734580 A JP 2734580A JP S631114 B2 JPS631114 B2 JP S631114B2
Authority
JP
Japan
Prior art keywords
wastewater
dyeing
isocyanuric acid
dyeing process
dyes
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.)
Expired
Application number
JP55027345A
Other languages
Japanese (ja)
Other versions
JPS56124490A (en
Inventor
Tokuyuki Taniguchi
Masanori Oota
Shoichi Sato
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.)
Nissan Chemical Corp
Original Assignee
Nissan Chemical 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 Nissan Chemical Corp filed Critical Nissan Chemical Corp
Priority to JP2734580A priority Critical patent/JPS56124490A/en
Publication of JPS56124490A publication Critical patent/JPS56124490A/en
Publication of JPS631114B2 publication Critical patent/JPS631114B2/ja
Granted legal-status Critical Current

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  • Removal Of Specific Substances (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、染色工場等において染色終了後に廃
棄される着色水及び染色された染色物の水洗工程
終了後に廃棄される着色水等染色工程における着
色廃水の脱色・浄化方法に係わる。 染色工場では、直接染料、酸性染料、分散染
料、反応性染料等各種の染料及び染色助剤が用い
られ、被染物を染色した後廃棄される染色廃水及
び染色物を水洗した後廃棄される洗浄廃水等を無
処理のまゝ河川等に放流すると河川が著るしく汚
染されるため、上記染色工程廃水の無公害化対策
が望まれていた。かゝる対策の提案としては、従
来より幾つか知られているが、未だいずれも充分
でない。例えば、活性汚泥により処理する方法、
凝集沈降剤により処理する方法、活性炭により吸
着処理する方法等があるが、これらの方法では、
脱色浄化効率が低く、また、COD(化学的酸素要
求量)及びBOD(生物学的酸素要求量)の増加を
充分に防ぐことができない。更にこれらの方法を
実施するには、そのための設備、運転等に多大の
費用を要し、工業的実施が困難である。 本発明者らは、上記問題点の解決のために種々
の実験的研究を行なつたところ、三塩素化イソシ
アヌール酸を主成分とする錠剤を前記染色工程廃
水の流水中に浸漬させた際、単に廃水の脱色が生
起するのみならず、COD及びBODの増加を防ぎ
得ることを見出し、本発明を完成した。本発明の
目的は、染色工程着色廃水を効率よく脱色・浄化
する方法を提供することにあり、更に他の目的
は、染色工程廃水の脱色・浄化を簡易かつ低コス
トに実施し得る方法を提供することにある。本発
明の染色工程廃水を、塩素化イソシアヌール酸を
含む錠剤に接触させることを特徴とする。 本発明の対象とする染色工程廃水は、染色工場
において例えば、直接染料、酸性染料、分散染
料、反応性染料等通常の染料を用いた染色液によ
り被色物を染色処理した後廃棄される着色廃水、
上記染色液により染色処理された染色物の水洗処
理に用いられた廃棄される着色廃水又はこれらの
混合廃水等であり、通常0.2%以下の染料を尚溶
存し、着色度の高いものである。この着色廃水
は、水により10〜100倍位に希釈しても尚着色度
が高く、河川に放流できない。 本発明に用いられる塩素化イソシアヌール酸と
しては、三塩素化イソシアヌール酸、二塩素化イ
ソシアヌール酸のナトリウム塩若しくはカリウム
塩等が挙げられ、また、本発明に用いられる塩素
化イソシアヌール酸を含む錠剤は、上記塩素化イ
ソシアヌール酸に助剤、充填剤等を配合し錠剤化
したものである。好ましい錠剤は、三塩素化イソ
シアヌール酸に数%以内の硼酸を配合し加圧打錠
することにより得られる。また、三塩素化イソシ
アヌール酸を主成分とし、これに二塩素化イソシ
アヌール酸のナトリウム塩若しくはカリウム塩と
数%以内の硼酸とを配合した後加圧打錠すること
によつても得られる。三塩素化イソシアヌール酸
は、水に対する溶解速度が小さく、二塩素化イソ
シアヌール酸のナトリウム塩及びカリウム塩は対
する溶解速度が大きいので、錠剤を前記着色廃水
に接触させる際廃水の流速が小さいとき又は錠剤
の比表面積が充分大きいときは、錠剤中の三塩素
化イソシアヌール酸の割合を高くするのが好まし
い。通常、用いられる錠剤としては、打錠成形を
容易ならしめるために直径1〜数cm程度の円柱状
又は円板状のものが好まれる。粒度が小さくなる
と、例えば、粉状品を用いて前記染色工程廃水の
流水に接触させると、流水下部に沈降し易く、効
率よく前記廃水の浄化を達成できない。 本発明による染色工程廃水の浄化は、上記塩素
化イソシアヌール酸を含む錠剤に、前記染色工程
廃水を接触させることにより達成される。接触に
よつて、錠剤中から塩素化イソシアヌール酸が廃
水中に溶出し、廃水中の溶存染料を分解し、脱色
が生起すると共に、廃水のCOD及びBODの増加
が避けられる。 好ましい接触は、前記錠剤を通水性容器、例え
ば、網、かご等に内容させ、これを流廃水中に浸
漬することにより達成される。 廃水の脱色・浄化を効率よく達成するには、廃
水の流速及び錠剤の接触表面積を適当に選定する
ことによつて容易に行ない得る。かくして、本発
明によれば、染色工程廃水をきわめて簡易にかつ
効率よく浄化し得る。 以下、実施例及び比較例を挙げて更に詳しく説
明するが、本発明の技術的範囲はこれに限定され
るものではない。 実施例 1 染色機40台を備え、繊維製品を染色する工場の
染色工程廃水量は、廃棄される染色液が1日当り
約100m3であり、染色物の洗浄に用いられた後の
廃棄される洗浄廃水が1日当り約200m3である。
両者は混合された後約300m3/日の着色廃水とし
て工場から排出される。この廃水中には、直接染
料、分散染料、反応性染料、界面活性剤、無機塩
類等を約5%含み、赤褐色であつた。 トリクロロイソシアヌール酸粉末とこれに対し
2%の硼酸との配合物を加圧打錠することにより
得られた円板状錠剤(直径35mm、高さ19mm、重さ
30g)を縦、横、高さがそれぞれ40cm×50cm×30
cmのポリエチレン製のざるに5Kg投入し、これを
上記廃水の流れの中に浸漬した。廃水の流速は、
30cm3/時であつたが、上記錠剤に接触した後の廃
水は、肉眼では微赤色程度まで脱色された。更に
波長540mμ光の吸光度、懸濁物質、COD及び
BODを測定したところ第1表所載の結果が得ら
れた。 比較例 1 実施例1に記載のものと同じ廃水1cm3に対し凝
集沈澱剤としてポリ塩化アルミニウム15g、炭酸
ナトリウム8g、ポリアクリルアミド2gを加
え、凝集沈澱法廃水処理設備により処理したが、
廃水はなお強い赤褐色を呈し、吸光度、固形分、
COD及びBODを実施例1と同様にして測定した
ところ第1表所載の結果が得られた。 実施例 2 実施例1における錠剤の代りに、三塩素化イソ
シアヌール酸88%、二塩化イソシアヌール酸のナ
トリウム塩2%及び硼酸10%からなる錠剤(直径
35mm、高さ19mm、重さ30g)を5Kg用い、廃水の
流速が30m3/時である他は、実施例1と同様にし
て本発明の浄化方法を実施したところ第1表所載
の結果を得た。 表1表には、無処理の廃水について測定した結
果も示したが、本発明の方法が極めて効果的であ
ることが認められる。
The present invention relates to a method for decolorizing and purifying colored wastewater in a dyeing process, such as colored water discarded after completion of dyeing in a dyeing factory or the like, and colored water discarded after the washing process of dyed dyed products. In dyeing factories, various dyes and dyeing aids such as direct dyes, acid dyes, disperse dyes, and reactive dyes are used.Dyeing wastewater is discarded after dyeing the dyed object, and washing water is discarded after washing the dyed object with water. If wastewater and the like are discharged into rivers and the like without treatment, the rivers will be significantly polluted, so there has been a desire for measures to make the dyeing process wastewater pollution-free. Although several proposals for such countermeasures have been known in the past, none of them are yet sufficient. For example, a method of treatment with activated sludge,
There are methods such as treatment with coagulation-sedimentation agents and adsorption treatment with activated carbon, but with these methods,
The decolorization and purification efficiency is low, and increases in COD (chemical oxygen demand) and BOD (biological oxygen demand) cannot be sufficiently prevented. Furthermore, implementing these methods requires a large amount of equipment, operation, etc., and is difficult to implement industrially. The present inventors conducted various experimental studies to solve the above problems, and found that when tablets containing trichlorinated isocyanuric acid as a main component were immersed in flowing dyeing process wastewater, They discovered that not only decolorization of wastewater occurs, but also an increase in COD and BOD can be prevented, and the present invention was completed. An object of the present invention is to provide a method for efficiently decolorizing and purifying colored wastewater from a dyeing process, and a further object is to provide a method for decolorizing and purifying dyeing process wastewater easily and at low cost. It's about doing. The dyeing process wastewater of the present invention is characterized in that it is brought into contact with tablets containing chlorinated isocyanuric acid. Dyeing process wastewater that is the object of the present invention is, for example, colored waste water that is discarded after dyeing objects with a dyeing solution using ordinary dyes such as direct dyes, acid dyes, disperse dyes, and reactive dyes in dyeing factories. waste water,
This is colored wastewater or mixed wastewater used for washing dyed products dyed with the above-mentioned dyeing solution, and usually contains less than 0.2% dye and has a high degree of coloring. Even if this colored wastewater is diluted 10 to 100 times with water, it is still highly colored and cannot be discharged into rivers. Examples of the chlorinated isocyanuric acid used in the present invention include sodium salts or potassium salts of trichlorinated isocyanuric acid, dichlorinated isocyanuric acid, etc. The tablets included are prepared by blending the chlorinated isocyanuric acid with auxiliary agents, fillers, etc. Preferred tablets are obtained by blending trichlorinated isocyanuric acid with boric acid within a few percent and compressing the mixture. It can also be obtained by blending trichlorinated isocyanuric acid as the main component with sodium salt or potassium salt of dichlorinated isocyanuric acid and boric acid within a few percent, and then pressing into tablets. . Trichlorinated isocyanuric acid has a low dissolution rate in water, and sodium and potassium salts of dichlorinated isocyanuric acid have a high dissolution rate in water, so when the tablet is brought into contact with the colored wastewater, the flow rate of the wastewater is low. Alternatively, when the specific surface area of the tablet is sufficiently large, it is preferable to increase the proportion of trichlorinated isocyanuric acid in the tablet. Usually, the tablets used are preferably cylindrical or disc-shaped with a diameter of about 1 to several cm in order to facilitate tableting. When the particle size becomes small, for example, when a powdered product is brought into contact with the flowing dyeing process wastewater, it tends to settle in the lower part of the flowing water, making it impossible to efficiently purify the wastewater. Purification of the dyeing process wastewater according to the present invention is achieved by bringing the dyeing process wastewater into contact with the tablet containing the chlorinated isocyanuric acid. Upon contact, chlorinated isocyanuric acid is eluted from the tablet into the wastewater, decomposing the dissolved dye in the wastewater, decolorizing it, and avoiding an increase in COD and BOD in the wastewater. Preferred contact is achieved by placing the tablet in a water-permeable container, such as a screen, basket, etc., and immersing it in running water. Efficient decolorization and purification of wastewater can be easily achieved by appropriately selecting the flow rate of the wastewater and the contact surface area of the tablet. Thus, according to the present invention, dyeing process wastewater can be purified very easily and efficiently. The present invention will be described in more detail below with reference to Examples and Comparative Examples, but the technical scope of the present invention is not limited thereto. Example 1 The amount of wastewater from the dyeing process in a factory equipped with 40 dyeing machines that dyes textile products is approximately 100 m 3 of wastewater per day, which is approximately 100 m 3 of wastewater per day after being used for cleaning dyed products. Washing wastewater is approximately 200m 3 per day.
After the two are mixed, approximately 300 m 3 /day of colored wastewater is discharged from the factory. This wastewater contained about 5% of direct dyes, disperse dyes, reactive dyes, surfactants, inorganic salts, etc., and was reddish brown in color. Disc-shaped tablets (diameter 35 mm, height 19 mm, weight
30g) with length, width, and height of 40cm x 50cm x 30
5 kg was placed in a polyethylene strainer of 1.5 cm in size and immersed in the waste water stream. The flow rate of wastewater is
Although the waste water was 30 cm 3 /hour, the waste water after contacting the tablets was decolored to a slightly red color to the naked eye. Furthermore, the absorbance of wavelength 540mμ light, suspended solids, COD and
When the BOD was measured, the results shown in Table 1 were obtained. Comparative Example 1 15 g of polyaluminum chloride, 8 g of sodium carbonate, and 2 g of polyacrylamide were added as a coagulation-sedimentation agent to 1 cm 3 of the same wastewater as described in Example 1, and the wastewater was treated using a coagulation-sedimentation wastewater treatment facility.
The wastewater still has a strong reddish-brown color, and the absorbance, solid content,
When COD and BOD were measured in the same manner as in Example 1, the results listed in Table 1 were obtained. Example 2 Instead of the tablets in Example 1, tablets (diameter
The purification method of the present invention was carried out in the same manner as in Example 1, except that a 35 mm, height 19 mm, weight 30 g) was used and the wastewater flow rate was 30 m 3 /hour, and the results shown in Table 1 were obtained. I got it. Table 1 also shows the results of measurements on untreated wastewater, and it is recognized that the method of the present invention is extremely effective.

【表】【table】

【表】 質の量を表わす。
[Table] Represents quantity of quality.

Claims (1)

【特許請求の範囲】[Claims] 1 染色工程廃水を、塩素化イソシアヌール酸を
含む錠剤に接触させることを特徴とする前記染色
工程廃水の浄化方法。
1. A method for purifying dyeing process wastewater, which comprises bringing the dyeing process wastewater into contact with a tablet containing chlorinated isocyanuric acid.
JP2734580A 1980-03-06 1980-03-06 Purification of waste water in dyeing process Granted JPS56124490A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2734580A JPS56124490A (en) 1980-03-06 1980-03-06 Purification of waste water in dyeing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2734580A JPS56124490A (en) 1980-03-06 1980-03-06 Purification of waste water in dyeing process

Publications (2)

Publication Number Publication Date
JPS56124490A JPS56124490A (en) 1981-09-30
JPS631114B2 true JPS631114B2 (en) 1988-01-11

Family

ID=12218450

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2734580A Granted JPS56124490A (en) 1980-03-06 1980-03-06 Purification of waste water in dyeing process

Country Status (1)

Country Link
JP (1) JPS56124490A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04125307U (en) * 1991-05-08 1992-11-16 積水化学工業株式会社 partition unit

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5023412B2 (en) * 2001-05-09 2012-09-12 吉澤石灰工業株式会社 Formaldehyde waste liquid treatment agent
CN103787480A (en) * 2012-10-26 2014-05-14 无锡飞伊生物科技有限公司 Waste liquid treatment method of gram stain two-step method

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS505604U (en) * 1973-05-10 1975-01-21
JPS5199847A (en) * 1974-11-22 1976-09-03 Nippon Zeon Co Jukibutsushitsu ofukumu haisuino shoriho

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04125307U (en) * 1991-05-08 1992-11-16 積水化学工業株式会社 partition unit

Also Published As

Publication number Publication date
JPS56124490A (en) 1981-09-30

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