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JPS5853594B2 - Method for detoxifying incineration ash containing heavy metals - Google Patents
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JPS5853594B2 - Method for detoxifying incineration ash containing heavy metals - Google Patents

Method for detoxifying incineration ash containing heavy metals

Info

Publication number
JPS5853594B2
JPS5853594B2 JP51076055A JP7605576A JPS5853594B2 JP S5853594 B2 JPS5853594 B2 JP S5853594B2 JP 51076055 A JP51076055 A JP 51076055A JP 7605576 A JP7605576 A JP 7605576A JP S5853594 B2 JPS5853594 B2 JP S5853594B2
Authority
JP
Japan
Prior art keywords
heavy metals
incineration ash
water
solid
ash
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
JP51076055A
Other languages
Japanese (ja)
Other versions
JPS532381A (en
Inventor
正樹 近藤
孝史 渡部
輝高 平沢
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries 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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP51076055A priority Critical patent/JPS5853594B2/en
Publication of JPS532381A publication Critical patent/JPS532381A/en
Publication of JPS5853594B2 publication Critical patent/JPS5853594B2/en
Expired legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】 この発明は重金属を含む都市ゴミ、都市下水汚泥、塗装
スラッジなどの焼却灰の無害化方法に関するものである
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for detoxifying incineration ash such as municipal garbage, municipal sewage sludge, and paint sludge containing heavy metals.

都市ゴミなどの焼却炉で発生したダストをサイクロン、
電気集塵機などにより回収した焼却灰中には、焼却物質
の種類により含まれる金属の種類および濃度割合が異な
るが、鉛、カドミウム、亜鉛等の有害重金属類が含lれ
ている場合が多い。
A cyclone removes dust generated in incinerators such as city garbage.
Incineration ash collected by an electrostatic precipitator or the like often contains harmful heavy metals such as lead, cadmium, and zinc, although the types and concentration ratios of metals included vary depending on the type of incinerated material.

この処理方法の1つとして、水溶液と焼却灰とを混合し
、可溶性金属類を水の系に溶出させたのち分離する方法
が考えられてきたが、脱水機等により脱水された分離物
(一般には脱水ケーキ)の水分中にイオン状の有害重金
属が含まれている場合が多く、その1捷投棄すると二次
公害を引おこすかそれがある。
As one of the treatment methods, a method has been considered in which an aqueous solution and incinerated ash are mixed and the soluble metals are eluted into the water system and then separated. (dehydrated cake) often contains harmful ionic heavy metals in the water, and if one of them is dumped, it may cause secondary pollution.

また脱水機等に流入させる前に有害重金属等の不溶化剤
を添加1〜で不溶化後置液分離することも考えられるが
、この場合分離物は無害化されるが、分離物中に残る有
害重金属の絶対量は減少せず、また夾雑物質の含有割合
が多いため有価金属の回収もできないことが多いため適
当な方法とはいえなかった。
It is also possible to add an insolubilizer for harmful heavy metals, etc. before flowing into a dehydrator, etc., and separate the solution after insolubilization.In this case, the separated material is rendered harmless, but the harmful heavy metals that remain in the separated material The absolute amount of metals does not decrease, and valuable metals often cannot be recovered due to the high content of contaminants, so this method could not be considered an appropriate method.

この発明は上記欠点を除去するためになされたもので、
重金属を含む焼却灰を水または酸性溶液と混合し、焼却
灰中の可溶性重金属を溶解した後、多量の不溶解残灰を
含むスラリーを固液分離する際に、分離物に含1れろ水
分中および固形物表面に吸着されている重金属イオン類
を、1ず水洗浄によりできるだけ洗浄し、可溶性重金属
を分離し、次いで有機系不溶化剤、硫化ソーダ、燐酸ソ
ーダ等の不溶化剤を含む洗浄液で洗浄することを特徴と
するものである。
This invention was made to eliminate the above-mentioned drawbacks.
After incineration ash containing heavy metals is mixed with water or an acidic solution to dissolve the soluble heavy metals in the incineration ash, when the slurry containing a large amount of undissolved residual ash is subjected to solid-liquid separation, 1 is contained in the separated product and the filtrate is removed. The heavy metal ions adsorbed on the surface of the solid material are first washed with water to separate the soluble heavy metals, and then washed with a cleaning solution containing an insolubilizing agent such as an organic insolubilizing agent, sodium sulfide, or sodium phosphate. It is characterized by this.

またこの発明は重金属を含む焼却灰を水または酸性溶液
と混合し、焼却灰中の可溶性重金属を溶解した後、多量
の不溶解残灰を含むスラリーを脱水様等で第1段目の固
液分離を行い、その分離物を有害重金属の不溶化剤を含
む溶液でリパルピングし、その分離物に含1れる重金属
イオンを不溶化したスラリーを得、これに第2段目の固
液分離を行うことを特徴とするものである。
In addition, this invention mixes incinerated ash containing heavy metals with water or an acidic solution, dissolves the soluble heavy metals in the incinerated ash, and then dehydrates the slurry containing a large amount of undissolved residual ash to form a solid-liquid solution in the first stage. Separation is performed, and the separated product is repulped with a solution containing an insolubilizer for harmful heavy metals to obtain a slurry in which the heavy metal ions contained in the separated product are insolubilized, and this is subjected to a second stage of solid-liquid separation. This is a characteristic feature.

次に図に従いこの発明を都市ゴミ焼却灰に使用した場合
の一実施例について説明する。
Next, an embodiment in which the present invention is applied to municipal waste incineration ash will be described with reference to the drawings.

ゴミ貯槽に集められた都市ゴミは焼却炉により焼却され
るが、この際、炉底より回収される焼却灰と、焼却炉の
ガス排出部に接続された集じん機で回収される焼却灰と
を混合槽において混合する(炭の混合率5〜25係)。
Municipal garbage collected in the garbage storage tank is incinerated in an incinerator, but at this time, incinerated ash is collected from the bottom of the incinerator, and incinerated ash is collected by a dust collector connected to the gas discharge part of the incinerator. are mixed in a mixing tank (charcoal mixing ratio 5-25).

混合する前に水筐たは酸性溶液を加えておく。Add water or acidic solution before mixing.

混合槽に訃いて混合するに際し、可溶性の重金属が溶解
する。
When mixed in a mixing tank, soluble heavy metals are dissolved.

ここで焼却灰の溶解特性につして言及すると。Let me now mention the dissolution characteristics of incineration ash.

焼却灰組成中金属類が30〜4o%占める場合が多く、
これにはPb、Cd、Cr+’ 、T−Cr、Zn。
In many cases, metals account for 30-40% of the incineration ash composition,
These include Pb, Cd, Cr+', T-Cr, and Zn.

Mn、Cu、AI、に、Na、Fe、Mg、Ca、Si
、Sn。
Mn, Cu, AI, Na, Fe, Mg, Ca, Si
, Sn.

Hg、As等が含1れる。Contains Hg, As, etc.

このうち大半をNa、K。Zn、Ca、AI、Siが占
める。
Most of these are Na and K. Mainly occupied by Zn, Ca, AI, and Si.

これら金属の形態の大半が酸化物で、その他成る程度の
塩化物、硫酸化物を含む。
Most of these metals are in the form of oxides, with some chlorides and sulfides also present.

ここで塩化物および硫酸化物訃よび酸化物の一部が水に
可溶であり、Pbs”d2’Cr +6s Hg *
Mn m N を等は殆んど全てが水に可溶な成分のみ
からなる。
Here, some of the chlorides and sulfates and oxides are soluble in water, and Pbs"d2'Cr +6s Hg *
Mn m N etc. consist almost entirely of water-soluble components.

な$i、 o、 I NHClまたは0、1 NH2B
O4で溶解するとZn、Ni、Cu、Feの溶出割合は
増加するが、Pb、Cd、Cr+’Hg等は変らない。
$i, o, I NHCl or 0, 1 NH2B
When dissolved with O4, the elution ratios of Zn, Ni, Cu, and Fe increase, but Pb, Cd, Cr+'Hg, etc. do not change.

例として焼却灰15係混合スラリー溶液における水の系
に溶出した金属濃度を第1表に示す。
As an example, Table 1 shows the concentrations of metals eluted into the water system in the incinerated ash 15 mixed slurry solution.

このように重金属を含有したスラリーは固液分離機にか
けられ、濾過ケーキとF液とに分離される。
The slurry containing heavy metals is passed through a solid-liquid separator and separated into a filter cake and liquid F.

との固液分離機には水が噴射されスラリーは脱水されな
がら水洗浄され、その後不溶化剤で再度洗浄された後ケ
ーキとなり固液分離機の機外に排出される。
Water is injected into the solid-liquid separator, and the slurry is dehydrated and washed with water. After that, the slurry is washed again with an insolubilizer, and then turned into a cake and discharged outside the solid-liquid separator.

この方法による都市ゴミの焼却灰の処理例を以下に記す
An example of the treatment of incineration ash of municipal waste using this method is described below.

焼却灰の混合率15係、溶媒は水または0.IN硫酸、
溶解時間、15分〜30分、プレコート真空脱水機C濾
過面積0.9m2 )を使用して行った。
The mixing ratio of incinerated ash is 15 parts, and the solvent is water or 0. IN sulfuric acid,
The dissolution time was 15 to 30 minutes using a precoat vacuum dehydrator C (filtration area: 0.9 m2).

無洗浄の場合と洗浄した場合のケーキ中のイオン状重金
属濃度をそれぞれ第2表及び第3表に示す。
The ionic heavy metal concentrations in the cakes without washing and after washing are shown in Tables 2 and 3, respectively.

条件;洗浄水量 水 :固形物重量の2〜3位以上使用して洗浄不溶
化剤による洗浄後固形物の1〜3倍の水による再洗浄実
施不溶化剤:有機系不溶化剤又はリン酸卦よび硫化イオ
ンの混合溶液を酸またはアルカリでpH=6〜11台に
調整したものを使用した。
Conditions: Washing water amount Water: Wash with an insolubilizing agent using at least 2 to 3 times the weight of the solids, and then rewashing with 1 to 3 times the amount of water as the solids.Insolubilizing agent: Organic insolubilizing agent or phosphoric acid and sulfur. A mixed solution of ions whose pH was adjusted to pH 6 to 11 with acid or alkali was used.

また洗浄pH量は固形物量の1〜3倍 すた本実験例においては無害化ケーキの溶出性が環境庁
告示溶出試験の基準値以下になった。
In addition, in this experimental example, where the washing pH was 1 to 3 times the amount of solid matter, the dissolution of the detoxified cake was below the standard value of the dissolution test notified by the Environmental Agency.

+6 、、。+6,,.

すなわちHg・・・・・・検出されず、Cr ・
・・検出されず、Cd<0.05 、 Pb<0.3
、Mn<0.3 。
In other words, Hg... is not detected, and Cr.
...Not detected, Cd<0.05, Pb<0.3
, Mn<0.3.

Zn<0.1 、 Cu<0.1 、 As<0.05
、 CN==検出されず、という結果を得た。
Zn<0.1, Cu<0.1, As<0.05
, CN==not detected.

次に他の発明に関する実施例を第2図に示す。Next, an embodiment related to another invention is shown in FIG.

ここでは上記の発明と異なう脱水装置を2段に分け、第
1段の脱水装置にお・いて、水洗浄した後脱水ケーキを
不溶化剤を含む液でリパルピングし、必要に応じてpH
をほぼ中性に調整したのちその後再び脱水装置により含
水率50〜70係程度の無害化分離ケーキを得、機外に
排出する。
Here, a dehydration device different from the above invention is divided into two stages, and in the first stage dehydration device, after washing with water, the dehydrated cake is repulped with a liquid containing an insolubilizer, and the pH is adjusted as necessary.
After the mixture is adjusted to almost neutrality, a detoxified separated cake with a moisture content of about 50 to 70 is obtained using the dehydrator again, and is discharged outside the machine.

この方法は必要に応じてリパルピングまたあとの第2段
目の脱水装置で水洗浄を行う事により分離ケーキのpH
を調整し機外に排出することも可能である。
In this method, the pH of the separated cake is adjusted by repulping and washing with water in the second stage dehydration equipment as needed.
It is also possible to adjust the amount and discharge it outside the machine.

この発明により分離物中に含1れる有害重金属の絶対量
が少くなるとともに僅かに残存するものも不溶化剤で安
定な形にかわり、従来よう一歩進んだ熱化処理法となる
According to this invention, the absolute amount of harmful heavy metals contained in the separated product is reduced, and even the slightest remaining amount is converted into a stable form by the insolubilizing agent, resulting in a thermal treatment method that is one step ahead of conventional methods.

また無害化のための薬品費が従来の方式に比較して大幅
に削減され、且つ有価金属がP液中イオン状で分離され
るための有効利用が可能となる。
In addition, the cost of chemicals for detoxification is significantly reduced compared to conventional methods, and valuable metals are separated in ionized form in the P solution, making it possible to use them effectively.

なお、上記実施例では都市ゴミ焼却灰の例を挙げている
が1重金属を含む焼却灰であれば例えば都市下水汚泥、
塗装スラッジ等に使用できる。
Incidentally, in the above example, an example of municipal waste incineration ash is given, but incineration ash containing one heavy metal may be used, for example, municipal sewage sludge,
Can be used for paint sludge, etc.

【図面の簡単な説明】 第1図は本発明の1実施例、第2図は他の発明の1実施
例を示す概略図である。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram showing one embodiment of the present invention, and FIG. 2 is a schematic diagram showing another embodiment of the invention.

Claims (1)

【特許請求の範囲】 1 重金属を含む焼却灰を水筐たは酸性溶液と混合し、
焼却灰中の可溶性重金属を溶解した後、多量の不溶解残
灰を含むスラリーを固液分離する際に、分離物に台筐れ
る水分中ネーよび固形物表面(こ吸着されている重金属
イオン類を 筐ず水洗浄によシできるだけ洗浄し、可溶
性重金属を分離し、次いで不溶化剤を含む洗浄液で洗浄
することを特徴とする重金属を含む焼却灰の無害化方法
。 2 重金属を含む焼却灰を水または酸性溶液と混合し、
焼却灰中の可溶性重金属を溶解した後、多量の不溶解残
量を含むスラリーを脱水機等で第1段目の固液分離を行
い、その分離物を有害重金属の不溶化剤を含む溶液でリ
パルピング1−5その分離物に含1れる重金属イオンお
よび固形物表面に吸着されている重金属イオンを不溶化
したスラリーを得、これに第2段目の固液分離を行うこ
とを特徴とする重金属を含む焼却灰の無害化方法。
[Claims] 1. Mixing incineration ash containing heavy metals with a water container or an acidic solution,
After dissolving the soluble heavy metals in the incineration ash, when solid-liquid separation is performed on the slurry containing a large amount of undissolved residual ash, it is possible to remove the adsorbed heavy metal ions from the water contained in the separated product and the adsorbed heavy metal ions on the surface of the solid matter. A method for detoxifying incinerated ash containing heavy metals, which is characterized by washing as much as possible by washing with water, separating soluble heavy metals, and then washing with a cleaning solution containing an insolubilizing agent. 2. Converting incinerated ash containing heavy metals into water. or mixed with acidic solution,
After dissolving the soluble heavy metals in the incineration ash, the slurry containing a large amount of undissolved residue is subjected to the first solid-liquid separation using a dehydrator, etc., and the separated product is repulped with a solution containing an insolubilizer for harmful heavy metals. 1-5 A slurry containing heavy metals is obtained by insolubilizing the heavy metal ions contained in the separated product and the heavy metal ions adsorbed on the surface of the solid material, and the slurry is subjected to a second stage of solid-liquid separation. How to make incineration ash harmless.
JP51076055A 1976-06-29 1976-06-29 Method for detoxifying incineration ash containing heavy metals Expired JPS5853594B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51076055A JPS5853594B2 (en) 1976-06-29 1976-06-29 Method for detoxifying incineration ash containing heavy metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51076055A JPS5853594B2 (en) 1976-06-29 1976-06-29 Method for detoxifying incineration ash containing heavy metals

Publications (2)

Publication Number Publication Date
JPS532381A JPS532381A (en) 1978-01-11
JPS5853594B2 true JPS5853594B2 (en) 1983-11-30

Family

ID=13594081

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51076055A Expired JPS5853594B2 (en) 1976-06-29 1976-06-29 Method for detoxifying incineration ash containing heavy metals

Country Status (1)

Country Link
JP (1) JPS5853594B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61101711A (en) * 1984-10-24 1986-05-20 Hirochika Okuyama Method for making incinerated ash harmless
JP2722529B2 (en) * 1988-10-04 1998-03-04 大同特殊鋼株式会社 Detoxification method for heavy metal-containing dust
CH681810A5 (en) * 1990-10-22 1993-05-28 Von Roll Ag
JP2706634B2 (en) * 1995-05-25 1998-01-28 株式会社テクノフロンティア Recycling method of main ash of stalker type incinerator
JP4662338B2 (en) * 2005-02-02 2011-03-30 三菱重工環境・化学エンジニアリング株式会社 Waste combined gasification processing system and method
JP4702715B2 (en) * 2005-02-02 2011-06-15 三菱重工環境・化学エンジニアリング株式会社 Complex waste incineration treatment system and method

Also Published As

Publication number Publication date
JPS532381A (en) 1978-01-11

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