JPS6043192B2 - Method for preventing arsenic leaching in arsenic-containing waste - Google Patents

Method for preventing arsenic leaching in arsenic-containing waste

Info

Publication number
JPS6043192B2
JPS6043192B2 JP55059063A JP5906380A JPS6043192B2 JP S6043192 B2 JPS6043192 B2 JP S6043192B2 JP 55059063 A JP55059063 A JP 55059063A JP 5906380 A JP5906380 A JP 5906380A JP S6043192 B2 JPS6043192 B2 JP S6043192B2
Authority
JP
Japan
Prior art keywords
arsenic
waste
amount
elution
ferric
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
JP55059063A
Other languages
Japanese (ja)
Other versions
JPS56155680A (en
Inventor
俊明 菅原
和英 菅原
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP55059063A priority Critical patent/JPS6043192B2/en
Publication of JPS56155680A publication Critical patent/JPS56155680A/en
Publication of JPS6043192B2 publication Critical patent/JPS6043192B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Removal Of Specific Substances (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は、ひ素を含有する固形、半流動状もしくは液
体廃棄物(以下単にひ素含有廃棄物と称す)から、ひ素
が溶出するのを防止する処理方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a treatment method for preventing arsenic from being leached from solid, semi-liquid or liquid waste containing arsenic (hereinafter simply referred to as arsenic-containing waste). .

産業廃棄物は、通常陸上埋立てや、海洋投棄によつて
処分されているが、これらの処分を行なつた産業廃棄物
からひ素が溶出して環境を汚染することが注目されるよ
うになり、これを防止するために、昭和4時2月17日
付官報号外第13号によつて、ひ素溶出試験が義務づけ
られ、ひ素の溶出が基準値以下でなければ前記のような
処分を行なつてはならないことになつた。 従つて、ひ
素を含有する汚泥または廃液を排出する業界としては、
このような規制に対処できる処理方法を確立する必要に
迫られている。
Industrial waste is usually disposed of by land-filling or ocean dumping, but attention has been drawn to the fact that arsenic is leached from these disposed industrial wastes and pollutes the environment. In order to prevent this, an arsenic elution test was required by Official Gazette Extra No. 13 dated February 17, 1939, and if the arsenic elution was less than the standard value, the above-mentioned punishment would be carried out. It turned out that it wasn't going to happen. Therefore, as an industry that discharges sludge or waste liquid containing arsenic,
There is an urgent need to establish a processing method that can comply with such regulations.

現在までのところ、溶出試験でひ素が基準値である1
.5m9ll(ppm)を超えて溶出するような汚泥や
液状廃棄物の処理には、これらの廃棄物をコンクリート
で被覆して固化する方法が広く採用されている。
So far, arsenic has reached the standard value in elution tests.
.. For the treatment of sludge and liquid waste that elute in excess of 5m9ll (ppm), a method of covering and solidifying these wastes with concrete is widely adopted.

しカルながらこの固化方法は、ひ素を含む廃棄物を単
にコンクリートで被覆して外周を固め、内部のひ素含有
廃棄物の流出を防止しているに過ぎず、固化のための設
備やセメントの消費に関連する経済上の問題に加へ、コ
ンクリートの破損などによるひ素の流出などの懸念を伴
ふ。
However, this solidification method simply covers the arsenic-containing waste with concrete and solidifies the outer periphery to prevent the arsenic-containing waste from leaking out, and does not require the use of solidification equipment or cement. In addition to the economic problems associated with this, there are also concerns about arsenic leaking due to concrete damage.

本発明は、これらの諸問題を解消できる処理方法を提
供することを目的とするものてある。
The present invention aims to provide a processing method that can solve these problems.

本発明によれば、ひ素含有廃棄物に第1鉄塩または第
2鉄塩などの塩類、第1鉄イオンまたは第2鉄イオンを
含む廃酸のうちいづれか1種直接添加することによつて
、前記ひ素含有廃棄物からのひ素の溶出を防止すること
ができる。 本発明の対象とするひ素含有廃棄物として
は、特殊ガラス工場、陶磁器工場、農薬製造工場などか
ら排出される汚泥廃酸などを挙げることができる。
According to the present invention, by directly adding any one of salts such as ferrous salts or ferric salts, and waste acids containing ferrous ions or ferric ions to arsenic-containing waste, Elution of arsenic from the arsenic-containing waste can be prevented. Examples of arsenic-containing waste to which the present invention is directed include waste acid sludge discharged from special glass factories, ceramic factories, agricultural chemical manufacturing factories, and the like.

ひ素含有廃棄物の処理としては、硫酸第1鉄、硫酸第
2鉄、塩化第1鉄、塩化第2鉄などの第1鉄塩または第
2鉄塩と第1鉄イオンまたは第2鉄イオンを含む廃酸と
から成る群から群ばれた1種を単独に使用する。
To treat arsenic-containing waste, use ferrous or ferric salts such as ferrous sulfate, ferric sulfate, ferrous chloride, ferric chloride, and ferrous ions or ferric ions. One type from the group consisting of waste acids is used alone.

これらの鉄塩、または第1鉄イオンあるいは第2鉄イオ
ンを含む廃液は、無償または極めて安価に入手すること
ができ、場合によつては廃棄物処理費を支給された上入
手できる場合もある。
These iron salts, or waste liquids containing ferrous or ferric ions can be obtained free of charge or at very low cost, and in some cases may be obtained with a waste disposal fee paid. .

これらの処理剤は、同形状のものは水に溶かし、液状の
ものは、そのま)処理すべきひ素含有廃棄物を混合させ
る。本発明の処理方法において、第1鉄塩イオンまたは
第2鉄塩の塩類あるいは第1鉄イオンまたは第2鉄イオ
ンを含む廃液などを処理剤として加えることにより、溶
出試験によつてひ素の溶出量が減少したり検出されれな
くなるのは、下記のような機構によるものと考えられる
These processing agents are mixed with the arsenic-containing waste to be treated (if they are in the same shape, they are dissolved in water, or if they are in liquid form, they are left as is). In the treatment method of the present invention, by adding salts of ferrous salt ions or ferric salts or waste liquid containing ferrous ions or ferric ions as a treatment agent, the amount of arsenic eluted is determined by an elution test. It is thought that the following mechanism is responsible for the decrease or undetectability.

前記処理剤の添加によつて第1鉄イオンまたは第2鉄イ
オンが含まれている廃棄物に対し溶出試験を行うと、溶
出後のPH値を弱酸性かアルカリ性に調整した状態では
、第1鉄イオンは水酸化第1鉄を、第2鉄イオンは水酸
化第2鉄を形成してフロックとして析出沈澱する。
When an elution test is performed on waste containing ferrous ions or ferric ions by adding the treatment agent, if the pH value after elution is adjusted to weak acidity or alkalinity, Iron ions form ferrous hydroxide, and ferric ions form ferric hydroxide, which precipitate as flocs.

この際液状または固形廃棄物中のひ素は、水酸化鉄フロ
ックと共に共沈して水酸化鉄−ひ素の安定なコンプレッ
クスを形成して液中から除去され、溶出液中からひ素が
検出されないようになるものと考えられる。添加する鉄
塩の量は、含有されているひ素量の2−1@量で十分あ
ることは後述する実施例に示されている通りであるが、
幾分過剰に添加することによりひ素除去の目的を確実に
達成できる。以下本発明を実施例により説明する。実施
例1 実験室的な方法として砒酸(HAsO2)を水に溶かし
、ひ素量として10ppmを含む水溶液に、硫酸、第2
鉄の添加量を20ppmおよび50ppmとして試験液
2種を準備した。
At this time, arsenic in liquid or solid waste co-precipitates with iron hydroxide flocs to form a stable iron hydroxide-arsenic complex and is removed from the liquid, so that arsenic is not detected in the eluate. This is considered to be the case. As shown in the examples below, the amount of iron salt added is sufficient to be 2-1@ of the amount of arsenic contained.
Adding a slight excess ensures that the purpose of arsenic removal is achieved. The present invention will be explained below with reference to Examples. Example 1 As a laboratory method, arsenic acid (HAsO2) was dissolved in water, and sulfuric acid,
Two test solutions were prepared with the amount of iron added at 20 ppm and 50 ppm.

この試験液のPH値を8.0に調整した後、6紛間振盪
してから枦紙NO.5で?過し、枦液中のひ素量を工場
排水試験方法JISKOlO2、48−2により測定し
た。
After adjusting the pH value of this test solution to 8.0, it was shaken for 6 minutes, and then tested using No. 1 paper. At 5? The amount of arsenic in the liquid was measured according to the factory wastewater test method JISKOIO2, 48-2.

2倍に相当する20ppmの硫酸第2鉄を添加すること
によりひ素の溶出を防止できることが判つた。
It was found that the elution of arsenic could be prevented by adding 20 ppm of ferric sulfate, which is twice as much.

実施例2 ひ素として10ppmを含有するだけの量の汚泥を準備
し、これに第2鉄イオン8.4%を含有する硫酸廃液の
添加量を、下記に示す5段階に区別して試験した。
Example 2 An amount of sludge containing 10 ppm of arsenic was prepared, and the amount of sulfuric acid waste solution containing 8.4% of ferric ions added to the sludge was tested in five stages as shown below.

上記の結果から、第2鉄イオンを含む廃液を使用してひ
素を含む汚泥からのひ素の溶出を防止することが判る。
The above results show that the use of waste liquid containing ferric ions prevents the elution of arsenic from arsenic-containing sludge.

第2鉄イオンを含む廃酸の添加量としては、100pp
mつまりひ素含有量の10f8以上でよいことが認めら
れた。実施例3 ひ素含有廃棄物に、処理剤を添加した溶液について行う
PH調整の際のPH値が、ひ素の除去におよぼす影響を
検討する目的で試験を行なつた。
The amount of waste acid containing ferric ions added is 100 pp.
It was recognized that the arsenic content should be 10f8 or more. Example 3 A test was conducted for the purpose of examining the influence of the pH value upon pH adjustment on arsenic removal in a solution prepared by adding a processing agent to arsenic-containing waste.

ひ素10ppm相当を含有する量の汚泥に塩化第2鉄5
0ppmを添加し、PH値を下記のように調整して環境
庁告示第13号により溶出試験を行なつ“た。溶出液中
のひ素量は工場排水試験法JISKOlO2、48−2
により測定した。この結果から、溶出液のPH値が多い
ほど、つまりアルカリ性が強いほど、ひ素の溶出防止の
効果゛が大きいことが判る。
Ferric chloride 5 was added to the sludge containing the equivalent of 10 ppm arsenic.
0 ppm was added, the pH value was adjusted as shown below, and an elution test was conducted in accordance with Environment Agency Notification No. 13.
It was measured by From this result, it can be seen that the higher the pH value of the eluate, that is, the stronger the alkalinity, the greater the effect of preventing arsenic elution.

実施例5 ひ素10ppmを含む量の廃液中の固形分が3%になる
ように水を加えて調整し、硫酸第2鉄を含む廃酸(Fe
として8.4%)の添加量を下記の3種とした。
Example 5 A waste solution containing 10 ppm of arsenic was adjusted by adding water so that the solid content was 3%, and a waste acid containing ferric sulfate (Fe
(8.4%) was added in the following three types.

この混合物のPH値を8.0に調整し前記実施例と同様
の方法でp液中のひ素量を測定した。
The pH value of this mixture was adjusted to 8.0, and the amount of arsenic in the p liquid was measured in the same manner as in the above example.

上記の結果から第2鉄塩を添加することによつてもひ素
の溶出を防止することがでできる。
From the above results, the elution of arsenic can also be prevented by adding a ferric salt.

Claims (1)

【特許請求の範囲】[Claims] 1 ひ素を含む固形、半流動状または流動状廃棄物に、
第1鉄塩または第2鉄塩と第1鉄イオンを50%超えて
含む廃酸とからなる群から選ばれたいづれか1種を主体
とする、塩または廃酸をそのpHを5〜12の範囲に調
整して処理剤とし、廃棄物中のひ素量と処理剤の種類に
よつて予め設定された量を上廻るだけの量を添加し、そ
れによつてひ素の溶出量を規制値以下に低減することを
特徴とするひ素含有廃棄物中のひ素の溶出を防止する方
法。
1 For solid, semi-liquid or fluid waste containing arsenic,
A salt or waste acid mainly composed of one selected from the group consisting of a ferrous salt or a ferric salt and a waste acid containing more than 50% of ferrous ions at a pH of 5 to 12. Adjust the amount of arsenic within the range and use it as a treatment agent, and add an amount that exceeds the preset amount depending on the amount of arsenic in the waste and the type of treatment agent, thereby reducing the amount of arsenic eluted below the regulatory value. A method for preventing elution of arsenic in arsenic-containing waste, characterized by reducing the elution of arsenic in arsenic-containing waste.
JP55059063A 1980-05-02 1980-05-02 Method for preventing arsenic leaching in arsenic-containing waste Expired JPS6043192B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55059063A JPS6043192B2 (en) 1980-05-02 1980-05-02 Method for preventing arsenic leaching in arsenic-containing waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55059063A JPS6043192B2 (en) 1980-05-02 1980-05-02 Method for preventing arsenic leaching in arsenic-containing waste

Publications (2)

Publication Number Publication Date
JPS56155680A JPS56155680A (en) 1981-12-01
JPS6043192B2 true JPS6043192B2 (en) 1985-09-26

Family

ID=13102507

Family Applications (1)

Application Number Title Priority Date Filing Date
JP55059063A Expired JPS6043192B2 (en) 1980-05-02 1980-05-02 Method for preventing arsenic leaching in arsenic-containing waste

Country Status (1)

Country Link
JP (1) JPS6043192B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL8400107A (en) * 1984-01-12 1985-08-01 Pelt & Hooykaas METHOD FOR PROCESSING SLUDGE, IN PARTICULAR SLUDGE OBTAINED FROM DREDGING, AND PARTICULATES, AND METHOD FOR PROCESSING SLUDGE USING A HEAVY METAL ION ABSORBING AGENT.
JPS62132579A (en) * 1985-12-06 1987-06-15 Sanyo Mokuzai Boufu Kk Treatment for making waste non-polluting
MX171672B (en) * 1988-07-19 1993-11-10 Safe Waste Systems Inc COMPOSITION TO ENCAPSULATE CHROME, ARSENIC AND OTHER TOXIC METALS PRESENT IN WASTE AND PROCEDURE TO TREAT THE SAME
JP4591641B2 (en) * 2000-12-05 2010-12-01 Necファシリティーズ株式会社 Method for coagulating and precipitating iron hydroxide in wastewater containing concentrated inorganic components
JP2002233858A (en) * 2001-02-09 2002-08-20 Dowa Mining Co Ltd Detoxification method for heavy metal contaminated soil
JP2010247057A (en) * 2009-04-15 2010-11-04 Kurosaki:Kk Water purification method combining fine particle-making method and membrane separation method
JP6385909B2 (en) * 2015-10-16 2018-09-05 株式会社ナガオカ Raw water treatment method

Also Published As

Publication number Publication date
JPS56155680A (en) 1981-12-01

Similar Documents

Publication Publication Date Title
Lee Role of hydrous metal oxides in the transport of heavy metals in the environment
Maruyama et al. Metal removal by physical and chemical treatment processes
US4343706A (en) Method of removing heavy metals from industrial waste streams
Bux et al. Zinc biosorption by waste activated and digested sludges
Randtke et al. Chemical pretreatment for activated‐carbon adsorption
Potts et al. Removal of radionuclides in wastewaters utilizing potassium ferrate (VI)
Tünay et al. Pretreatment of complexed metal wastewaters
JPS6043192B2 (en) Method for preventing arsenic leaching in arsenic-containing waste
EP2792645A1 (en) Process for removing fluorides from water
Mamtaz et al. Reduction of arsenic in groundwater by coprecipitation with iron
Gilliam et al. Solidification/stabilization of technetium in cement-based grouts
Valentine et al. Removing radium by adding preformed hydrous manganese oxides
Schenck et al. Recovery of 3-chloro-4-(dichloromethyl)-5-hydroxy-2 (5H)-furanone from water samples on XAD resins and the effect of chlorine on its mutagenicity
JP2001269689A (en) Solid denitrification/dephosphorization accelerating agent
JP2004008854A (en) Insolubilization method of heavy metal or the like in polluted soil
JPH03186393A (en) Treatment of waste water containing fluorine
US5384036A (en) Effluent treatment
peters∗ et al. The effect of tartrate, a weak complexing agent, on the removal of heavy metals by sulfide and hydroxide precipitation
McFarland et al. Chemical treatment of chelated metal finishing wastes
KR100258770B1 (en) A disposer of industrial waste water having a good ability for eliminating a heavy metal and harmful components
AU2001289136A1 (en) Process and elixirs for removing contaminants from liquids
RU2267176C1 (en) Method of neutralization of the low-mineralized and medium- mineralized low-active liquid wastes in the field conditions
US3378487A (en) Method of treating waste water containing nickel
ATE97115T1 (en) METHOD OF PURIFICATION OF AQUEOUS SOLUTIONS CONTAMINATED BY NITRIATIONS.
US20030132421A1 (en) Elixir for inducing high-speed settlement of precipitates