JPS5931398B2 - Treatment method for wastewater containing thiocyanine - Google Patents
Treatment method for wastewater containing thiocyanineInfo
- Publication number
- JPS5931398B2 JPS5931398B2 JP7223581A JP7223581A JPS5931398B2 JP S5931398 B2 JPS5931398 B2 JP S5931398B2 JP 7223581 A JP7223581 A JP 7223581A JP 7223581 A JP7223581 A JP 7223581A JP S5931398 B2 JPS5931398 B2 JP S5931398B2
- Authority
- JP
- Japan
- Prior art keywords
- thiocyanine
- thiocyanide
- oxygen
- wastewater
- wastewater containing
- 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
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Catalysts (AREA)
Description
【発明の詳細な説明】
本発明はチオシアン含有廃水の処理方法に関し、詳しく
はチオシアンを含む廃水をラネー銅触媒の存在下に酸素
と接触させ、チオシアンを酸化分解することによって廃
水中のチオシアンを除去する方法に関スるものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating wastewater containing thiocyanide, and more specifically, the present invention relates to a method for treating wastewater containing thiocyanide, and more specifically, the thiocyanide in the wastewater is removed by contacting the wastewater containing thiocyanine with oxygen in the presence of a Raney copper catalyst and oxidatively decomposing the thiocyanide. It is related to the method of
ここでいうチオシアンとはチオシアン酸、チオシアン酸
塩等のチオシアンイオンを遊離する化合物を意味する。The term thiocyanine used herein refers to compounds that liberate thiocyanine ions, such as thiocyanic acid and thiocyanate.
一般にチオシアン酸塩は合成樹脂、染料、医薬品等の製
造に用いられるため、これらの廃水中に含まれることが
多い。Since thiocyanate is generally used in the production of synthetic resins, dyes, pharmaceuticals, etc., it is often contained in these wastewaters.
また、石油精製装置の1種である流動接触分解装置(F
CC)より排出される廃水中には必ずチオシアン酸塩が
含まれている。In addition, fluid catalytic cracking equipment (F
Wastewater discharged from CC) always contains thiocyanate.
さらに、製鉄等で生ずるコークス炉廃水中には高濃度の
チオシアンが含まれており、この処理が問題となってい
る。Furthermore, coke oven wastewater produced in steel manufacturing and the like contains high concentrations of thiocyanide, which poses a problem in its treatment.
チオシアンはシアン化物には含まれていないので有害物
質ではないが、化学的酸素要求量(COD)に検出され
るため(チオシアン:C0D−約1:1)チオシアンを
含有する廃水を排出する場合、当然その処理が必要とな
る。Since thiocyanide is not included in cyanide, it is not a harmful substance, but since it is detected in chemical oxygen demand (COD) (thiocyanide: COD - approximately 1:1), when discharging wastewater containing thiocyanide, Naturally, that processing is necessary.
現在のところ廃水中のチオシアンは他のCOD成分と共
に活性汚泥、散水濾床等の微生物処理法によって処理さ
れているのが実情である。At present, thiocyanide in wastewater is treated together with other COD components by microbial treatment methods such as activated sludge and trickling filters.
しかしながら、チオシアンを微生物処理するためには、
チオシアンを分解するのに必要な接触時間を長くとらね
ばならず、またチオシアンイオンの濃度が高い場合は、
微生物に阻害を及ぼすことすらある。However, in order to treat thiocyanine with microorganisms,
If the contact time required to decompose the thiocyanide is long and the concentration of thiocyanide ions is high,
It may even inhibit microorganisms.
さらに、微生物処理法は微生物処理に適したDHの維持
、栄養物質の添加(窒素、リン分等)、汚泥濃度(ML
SS)の調整、余剰汚泥の処理等の繁雑な操作が必要と
なる。Furthermore, the microbial treatment method requires maintenance of DH suitable for microbial treatment, addition of nutrients (nitrogen, phosphorus, etc.), sludge concentration (ML
This requires complicated operations such as adjusting SS) and processing excess sludge.
その他、チオシアン含有廃水を高温高圧(30KV/c
rriG、。In addition, thiocyanine-containing wastewater is treated at high temperature and high pressure (30KV/c).
rriG,.
200℃程度)で湿式酸化する方法もあるが、経済的で
ないため、あまり行われていない。There is also a method of wet oxidation at a temperature of about 200°C, but it is not economical and is therefore not widely used.
このような微生物処理法および湿式酸化法の欠点を克服
し、短時間で、かつ効果的にチオシアンを含有する廃水
の処理法として本発明者らが既に出願した「ポリビニル
アルコール含有廃水の処理法」(特願昭55−1805
35号)および「シアン含有廃水の処理方法」(特願昭
56−36461号)で用いたものと同じラネー銅触媒
を用いることによって容易にチオシアンイオンを酸化分
解させることができることを見い出したものである。The present inventors have already applied for a "method for treating wastewater containing polyvinyl alcohol" as a method for effectively treating wastewater containing thiocyanine in a short time by overcoming the drawbacks of the microbial treatment method and wet oxidation method. (Special application 1805-1983)
We have discovered that thiocyanine ions can be easily oxidized and decomposed by using the same Raney copper catalyst as used in ``Method for treating cyanide-containing wastewater'' (Japanese Patent Application No. 36461/1983). be.
特に、チオシアンのように硫黄を含む化合物は通常触媒
の被毒物質である場合が多く、このような被毒物質を触
媒で酸化分解できることは画期的なことである。In particular, sulfur-containing compounds such as thiocyanide are often poisonous substances for catalysts, and the ability to oxidize and decompose such poisonous substances using a catalyst is revolutionary.
本発明はチオシアンを含む廃水をラネー銅触媒の存在下
で純酸素、酸素含有ガスおよび酸素を発生する物質より
なる群から選ばれた1種または2種以上のものと接触さ
せることを特徴とするチオシアン含有廃水の処理方法を
提供するものである。The present invention is characterized in that wastewater containing thiocyanide is brought into contact with one or more selected from the group consisting of pure oxygen, oxygen-containing gas, and oxygen-generating substances in the presence of a Raney copper catalyst. A method for treating wastewater containing thiocyanide is provided.
本発明で使用するラネー銅触媒とは、銅と水、アルカリ
、酸などによって侵される金属(マグネシウム、アルミ
ニウム、亜鉛、鉄、ニッケル、スズ、鉛、シリカ、チタ
ニウム、ホウ素など)の1種または2種以上との合金に
対して水酸化ナトリウムなどのアルカリ水溶液または塩
酸などの酸水溶液を作用させることによって得られるも
のを意味し、アルカリまたは酸による銅板外の金属の溶
出量は特に制限されない。The Raney copper catalyst used in the present invention refers to copper and one or two metals (magnesium, aluminum, zinc, iron, nickel, tin, lead, silica, titanium, boron, etc.) that are attacked by water, alkalis, acids, etc. It means something obtained by applying an alkaline aqueous solution such as sodium hydroxide or an acid aqueous solution such as hydrochloric acid to an alloy with at least one species, and the amount of metal eluted from outside the copper plate by the alkali or acid is not particularly limited.
また、銅と銅板外め金属との重量比については通常1:
1のものを用いるが、この比に限定されるものではない
。In addition, the weight ratio of copper to copper plate outer metal is usually 1:
1 is used, but it is not limited to this ratio.
ラネー銅触媒の調製法の一例を示すと、重量比で1:1
の銅−アルミニウム合金に水酸化ナトリウム水溶液を作
用させると溶出反応は速やかに起り、合金中のアルミニ
ウムの90%以上が溶出されたラネー銅触媒が得られる
。An example of a Raney copper catalyst preparation method is 1:1 by weight.
When a sodium hydroxide aqueous solution is applied to the copper-aluminum alloy, an elution reaction occurs rapidly, and a Raney copper catalyst in which more than 90% of the aluminum in the alloy is eluted is obtained.
このようにラネー銅触媒は、銅板外の金属の溶出によっ
て多孔質のものとなる。In this way, the Raney copper catalyst becomes porous due to the elution of metal outside the copper plate.
上記のようにして得られたラネー銅触媒は、通常強度上
の立場から200メツシュ程度の粒度に調整されるが、
チオシアン含有廃水との接触反応方式によって適当な粒
度を選定することが望ましく、必ずしもこの粒度にとら
れれる必要はない。The Raney copper catalyst obtained as described above is usually adjusted to have a particle size of about 200 mesh from the viewpoint of strength.
It is desirable to select an appropriate particle size depending on the method of contact reaction with thiocyanine-containing wastewater, and it is not necessary to select this particle size.
次に、チオシアン含有廃水とラネー銅触媒との接触方式
については特に制限がなく完全混合型、固定床、流動床
、移動床などのいずれの方式でも良い。Next, the method of contacting the thiocyanine-containing wastewater with the Raney copper catalyst is not particularly limited, and any method such as a completely mixed type, fixed bed, fluidized bed, or moving bed may be used.
又、酸化分解に必要な酸素は予め原水のチオシアン含有
廃水に溶は込ませておく方式でも反応槽で供給する方式
のいずれ・でも良い。Further, the oxygen necessary for oxidative decomposition may be dissolved in the raw water containing thiocyanide in advance, or may be supplied in a reaction tank.
さらに、酸素は純酸素ガス、液体酸素、空気、酸素を含
む廃ガス、過酸化水素などの如き酸素を発生する物質等
のいずれのものを単独であるいは組合せて用いても良い
。Further, oxygen may be pure oxygen gas, liquid oxygen, air, oxygen-containing waste gas, oxygen-generating substances such as hydrogen peroxide, etc., and may be used alone or in combination.
なお、酸素の供給量についてはチオシアンを酸化するの
に必要な理論酸素量の1.2倍程度の酸素を供給すれば
十分である。Regarding the amount of oxygen supplied, it is sufficient to supply about 1.2 times the theoretical amount of oxygen required to oxidize thiocyanide.
また、反応温度、反応圧力は常温、常圧で良く、特に温
度を上げたり、圧力をかけたりする必要はない。Further, the reaction temperature and reaction pressure may be normal temperature or normal pressure, and there is no need to particularly raise the temperature or apply pressure.
しかしながら、反応効率を高めることが望まれる場合に
は、温度を上げたり圧力をかけることにより目的を達成
することができる。However, if it is desired to increase the reaction efficiency, this can be achieved by increasing the temperature or applying pressure.
本発明によれば、チオシアン含有廃水中のチオシアンイ
オンを常温、常圧でラネー銅触媒存在下、酸素により容
易に酸化分解して除去できるので、従来の処理法に比し
て繁雑な操作もなり、シかも短時間で酸化分解できる等
の利点がある。According to the present invention, thiocyanine ions in thiocyanide-containing wastewater can be easily removed by oxidative decomposition using oxygen in the presence of a Raney copper catalyst at room temperature and pressure, which requires less complicated operations than conventional treatment methods. It has the advantage of being able to be oxidized and decomposed in a short time.
また、反応装置も微生物処理に比べて小さくなる。Furthermore, the reaction equipment is also smaller compared to microbial treatment.
さらに、ラネー銅触媒中にアルミニウムや鉄などが含ま
れているときは、これらが酸化されて溶出し水酸化物と
して廃水中の懸濁物質を凝集させ; る効果を発揮する
。Furthermore, when the Raney copper catalyst contains aluminum, iron, etc., these are oxidized and eluted as hydroxides, which have the effect of coagulating suspended substances in wastewater.
以下に本発明を実施例により詳しく説明する。The present invention will be explained in detail below using examples.
実施例 1
チオシアン酸カリウム約1100ppを含む廃水を2t
のビーカー2個に各々1.5tずつ取り1、 ラネー銅
触媒(粒度:20Cメツシユ、銅含量:96.2wt
%、アルミニウム含量:3.8wt%、用研ファインケ
ミカル帆製)30 ccをそのうちの1個に添加し、他
の1個には触媒を添加しないで各々について等量の空気
を吹き込み攪拌しな; がらチオシアンの酸化分解を行
った。Example 1 2 tons of wastewater containing about 1100 pp of potassium thiocyanate
1. Raney copper catalyst (particle size: 20C mesh, copper content: 96.2wt) was placed in two beakers of 1.5t each.
%, aluminum content: 3.8wt%, manufactured by Yoken Fine Chemical Ho) 30 cc was added to one of them, and no catalyst was added to the other one, and the same amount of air was blown into each and stirred; Oxidative decomposition of thiocyanate was carried out.
結果を表1に示す。The results are shown in Table 1.
表1から明らかなように、無触媒のものは3時間の接触
時間ではチオシアンの酸化分解は全くみられないが、ラ
ネー銅触媒を添加したものは容易に酸化分解が行われる
ことがわかる。As is clear from Table 1, oxidative decomposition of thiocyanate is not observed at all with a contact time of 3 hours in the case without catalyst, but oxidative decomposition easily occurs in the case in which Raney copper catalyst is added.
なお、チオシアン酸カリウム1100pp を含む同
じ廃水30tをp H7,0に調整し、チオシアンで馴
致した活性汚泥で処理したところ(MLSS=2000
ppm )、3時間後にチオシアン濃度が10ppm
となった。In addition, when 30 tons of the same wastewater containing 1100 pp of potassium thiocyanate was adjusted to pH 7.0 and treated with activated sludge admixed with thiocyanate (MLSS = 2000
ppm), and the thiocyanine concentration was 10 ppm after 3 hours.
It became.
このことからもラネー銅触媒による酸化の方が速度的に
速いことがわかる。This also shows that the oxidation rate using the Raney copper catalyst is faster.
Claims (1)
酸素、酸素含有ガスおよび酸素を発生する物質よりなる
群から選ばれた1種または2種以上のものと接触させる
ことを特徴とするチオシアン含有廃水の処理法。1. Thiocyanide-containing wastewater, which is characterized by contacting thiocyanin-containing wastewater with one or more selected from the group consisting of pure oxygen, oxygen-containing gas, and oxygen-generating substances in the presence of a Raney copper catalyst. Wastewater treatment methods.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7223581A JPS5931398B2 (en) | 1981-05-15 | 1981-05-15 | Treatment method for wastewater containing thiocyanine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7223581A JPS5931398B2 (en) | 1981-05-15 | 1981-05-15 | Treatment method for wastewater containing thiocyanine |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57187093A JPS57187093A (en) | 1982-11-17 |
| JPS5931398B2 true JPS5931398B2 (en) | 1984-08-01 |
Family
ID=13483412
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7223581A Expired JPS5931398B2 (en) | 1981-05-15 | 1981-05-15 | Treatment method for wastewater containing thiocyanine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931398B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2018053359A (en) * | 2016-09-22 | 2018-04-05 | 国立大学法人東北大学 | Porous sponge copper, manufacturing method of porous sponge copper, porous sponge copper catalyst and manufacturing method of porous sponge copper catalyst |
| JP7448129B2 (en) * | 2022-07-29 | 2024-03-12 | 株式会社片山化学工業研究所 | How to treat wastewater |
-
1981
- 1981-05-15 JP JP7223581A patent/JPS5931398B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57187093A (en) | 1982-11-17 |
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