JPH10128287A - Treatment of solid waste - Google Patents

Treatment of solid waste

Info

Publication number
JPH10128287A
JPH10128287A JP8301132A JP30113296A JPH10128287A JP H10128287 A JPH10128287 A JP H10128287A JP 8301132 A JP8301132 A JP 8301132A JP 30113296 A JP30113296 A JP 30113296A JP H10128287 A JPH10128287 A JP H10128287A
Authority
JP
Japan
Prior art keywords
solid waste
ion exchanger
inorg
inorganic ion
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
JP8301132A
Other languages
Japanese (ja)
Inventor
Kazuo Hosoda
和夫 細田
Masaki Enome
正喜 柄目
Masafumi Moriya
雅文 守屋
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.)
Miyoshi Yushi KK
Miyoshi Oil and Fat Co Ltd
Original Assignee
Miyoshi Yushi KK
Miyoshi Oil and Fat Co 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 Miyoshi Yushi KK, Miyoshi Oil and Fat Co Ltd filed Critical Miyoshi Yushi KK
Priority to JP8301132A priority Critical patent/JPH10128287A/en
Publication of JPH10128287A publication Critical patent/JPH10128287A/en
Pending legal-status Critical Current

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  • Fire-Extinguishing Compositions (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To surely fix a harmful material together with a heavy metal and to prevent a generation of a toxic gas by adding an inorg. ion exchanger to a solid waste and fixing the harmful material in the solid waste with the inorg. ion exchanger. SOLUTION: A 10% water dispersion of the inorg. ion exchanger is added and mixed to 100g soot and dust being the solid waste obtained from a trash incineration plant so that an amount as the inorg. ion exchanger may be 10g. In this state, the harmful material in the solid waste is fixed with the inorg. ion exchanger. In this way, not only heavy metal element such as mercury, cadmium, lead, zinc, copper and chromium but also the element of arsenic acid and selenic acid are fixed efficiently, moreover, a fear of a generation of the toxic gas is eliminated.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、焼却灰、煤塵、鉱
滓、汚泥、土壌等の固体状廃棄物中に存在する重金属等
の有害物質を固定化し、これらの固体状廃棄物中からの
溶出を防止できる、固体状廃棄物の処理方法に関する。
The present invention relates to the immobilization of harmful substances such as heavy metals present in solid wastes such as incinerated ash, dust, slag, sludge, soil and the like, and elution from these solid wastes. And a method for treating solid waste.

【0002】[0002]

【従来の技術】ゴミ焼却場等で生じる焼却灰や煤塵、鉱
山から排出される鉱滓、廃水処理の際に生じる汚泥、汚
染された土壌等の固体状廃棄物中には種々の元素が含有
されており、水銀、カドミウム、鉛、亜鉛、銅、クロム
等の人体に有害な重金属元素も多く含有されている。こ
れら固体状廃棄物中に含まれる金属が流出すると、地下
水、河川、海水等が汚染される虞れがある。
2. Description of the Related Art Various elements are contained in solid waste such as incinerated ash and dust generated in garbage incineration plants, slag discharged from mines, sludge generated in wastewater treatment, and contaminated soil. It also contains a lot of heavy metal elements harmful to the human body, such as mercury, cadmium, lead, zinc, copper, and chromium. When metals contained in these solid wastes flow out, there is a possibility that groundwater, rivers, seawater, etc. will be contaminated.

【0003】このため、従来固体状廃棄物をセメントで
固めた後、埋め立てたり、海洋投棄したりする方法が採
られていたが、セメント壁を通して金属が流出する虞れ
があり、この方法は必ずしも安全な処理方法とは言えな
かった。このような問題を解決するため、本出願人は、
金属捕集剤によって固体状廃棄物中の金属を固定化する
方法を、種々提案している(例えば、特開昭64−90
083号、特開平1−99679号、特開平4−267
982号等)。
For this reason, conventionally, a method has been adopted in which solid waste is solidified with cement, and then landfilled or dumped into the ocean. However, there is a risk that metal may flow out through the cement wall. It was not a safe treatment. In order to solve such problems, the applicant has
Various methods have been proposed for immobilizing metals in solid waste with a metal collecting agent (see, for example, JP-A-64-90).
083, JP-A-1-99679, JP-A-4-267
982).

【0004】[0004]

【発明が解決しようとする課題】上記方法は、固体状廃
棄物中の水銀、カドミウム、鉛、亜鉛、銅、クロム等の
有害金属元素は効率良く、確実に固定化できる方法であ
る。しかしながら、固体状廃棄物中にはヒ酸やセレン酸
等の有害物質も含まれており、これらの物質は従来の金
属捕集剤のみを用いた処理方法では固定化することが困
難であった。このため金属捕集剤とともに塩化第二鉄、
硫酸アルミニウム、ポリ硫酸鉄等の添加剤を併用して、
ヒ酸やセレン酸を固定化する方法が検討された。しかし
ながら、固体状廃棄物中のヒ酸やセレン酸等を確実に固
定化するためには、固体状廃棄物の重量の30重量%も
の量の添加剤を添加しなければならず、経済的にも問題
であった。また固体状廃棄物処理に用いられている金属
捕集剤は、ジチオ酸基のような硫黄を含有する置換基を
有しているものが多いため、固体状廃棄物中に酸性物質
が含有されていると、有毒な硫化水素ガスを発生する等
の問題もあった。
The above-mentioned method is a method by which harmful metal elements such as mercury, cadmium, lead, zinc, copper and chromium in solid waste can be fixed efficiently and reliably. However, harmful substances such as arsenic acid and selenic acid are also contained in the solid waste, and it is difficult to immobilize these substances by a conventional treatment method using only a metal collecting agent. . For this reason, ferric chloride,
Using additives such as aluminum sulfate and polyiron sulfate together,
Methods for immobilizing arsenic acid and selenic acid were studied. However, in order to reliably fix arsenic acid, selenic acid, and the like in solid waste, it is necessary to add an additive as much as 30% by weight of the weight of solid waste. Was also a problem. In addition, since many metal collectors used for solid waste treatment have a substituent containing sulfur such as dithioic acid group, acidic substances are contained in solid waste. In this case, there is a problem that toxic hydrogen sulfide gas is generated.

【0005】本発明者等は上記課題を解決すべく鋭意研
究した結果、従来の金属捕集剤にかえて無機イオン交換
体を使用することにより、水銀、カドミウム、鉛、亜
鉛、銅、クロム等の重金属元素はもとより、ヒ酸やセレ
ン酸等の元素も効率良く固定化でき、しかも有毒ガスが
発生する虞もないことを見出し、本発明を完成するに至
った。
The present inventors have conducted intensive studies to solve the above problems, and as a result, by using an inorganic ion exchanger instead of a conventional metal collector, mercury, cadmium, lead, zinc, copper, chromium, etc. It has been found that not only heavy metal elements but also elements such as arsenic acid and selenic acid can be efficiently immobilized and that there is no risk of generating toxic gas, and the present invention has been completed.

【0006】[0006]

【課題を解決するための手段】即ち本発明の固体状廃棄
物の処理方法は、固体状廃棄物に無機イオン交換体を添
加し、固体状廃棄物中の有害物質を無機イオン交換体に
よって固定化することを特徴とする。本発明の対象とす
る固体状廃棄物としては、特に煤塵が好適である。
That is, in the method for treating solid waste according to the present invention, an inorganic ion exchanger is added to solid waste, and harmful substances in the solid waste are fixed by the inorganic ion exchanger. It is characterized in that Dust is particularly suitable as the solid waste targeted by the present invention.

【0007】[0007]

【発明の実施の形態】本発明において用いる無機イオン
交換体としては、例えば金属酸化物・含水酸化物、多価
金属酸性塩、不溶性ヘテロポリ酸塩、不溶性フェロシア
ン化物、アルミノ珪酸塩や粘土鉱物等が挙げられる。
BEST MODE FOR CARRYING OUT THE INVENTION The inorganic ion exchanger used in the present invention includes, for example, metal oxides and hydrated oxides, polyvalent metal acid salts, insoluble heteropolyacid salts, insoluble ferrocyanides, aluminosilicates and clay minerals. Is mentioned.

【0008】金属酸化物・含水酸化物としては、チタ
ン、ジルコニウム、アルミニウム、アンチモン、稀土類
元素等の酸化物・含水酸化物が挙げられる。多価金属酸
性塩としては、チタン、ジルコニウム、アルミニウム、
稀土類元素、クロム(III)等のリン酸塩等が、不溶性ヘ
テロポリ酸塩としては、リンアンチモン酸、モリブドリ
ン酸、モリブデン酸、アンチモン酸、チタン酸、ニオブ
酸、バナジン酸、アルミン酸等の、ナトリウム、カリウ
ム、カルシウム、マグネシウム、ジルコニウム、チタ
ン、アルミニウム、錫塩等が挙げられる。
The metal oxides and hydrated oxides include oxides and hydrated oxides of titanium, zirconium, aluminum, antimony, rare earth elements and the like. Polyvalent metal acid salts include titanium, zirconium, aluminum,
Rare earth elements, phosphates such as chromium (III), etc., as insoluble heteropolyacid salts, phosphorus antimonic acid, molybdophosphoric acid, molybdic acid, antimonic acid, titanic acid, niobic acid, vanadic acid, aluminate, etc. Sodium, potassium, calcium, magnesium, zirconium, titanium, aluminum, tin salts and the like.

【0009】また不溶性フェロシアン化物類としては、
フェロシアン化コバルト等が挙げられ、アルミノ珪酸塩
類や粘土鉱物類としては、ゼオライト、モルデナイト、
ベントナイト、バーミキュライト、スメクタイト(モン
モリロナイトを含む)等が挙げられる。更にこれらの他
に、ヒドロキシアパタイト、トバモライト、ゾノトライ
ト、マガディライト等や、炭酸カルシウム、珪酸カルシ
ウム、珪酸ナトリウム、珪酸マグネシウム、珪酸ジルコ
ニウム等も無機イオン交換体として用いることができ
る。これら無機イオン交換体は、1種または2種以上を
混合して用いることができる。これらの無機イオン交換
体は、その化学構造や結晶構造、層間距離等によって、
陽イオン或いは陰イオンに対する選択性やイオン交換物
性が異なるため、処理の対象となる固体状廃棄物から溶
出するイオンの種類と溶出量に基づき、無機イオン交換
体を選定する必要がある。
[0009] Insoluble ferrocyanides include:
Cobalt ferrocyanide and the like, aluminosilicates and clay minerals, zeolite, mordenite,
Bentonite, vermiculite, smectite (including montmorillonite) and the like. Further, in addition to these, hydroxyapatite, tobermorite, zonotolite, magadylite, and the like, calcium carbonate, calcium silicate, sodium silicate, magnesium silicate, zirconium silicate, and the like can also be used as the inorganic ion exchanger. These inorganic ion exchangers can be used alone or in combination of two or more. These inorganic ion exchangers, depending on their chemical structure, crystal structure, interlayer distance, etc.
Since the selectivity to cations or anions and the ion exchange properties are different, it is necessary to select an inorganic ion exchanger based on the type and amount of ions eluted from the solid waste to be treated.

【0010】本発明方法が対象とする固体状廃棄物は、
焼却灰や煤塵、鉱滓、汚泥、土壌等であるが、特に微粉
末状の煤塵の処理に好適である。これらの固体状廃棄物
を処理するには、無機イオン交換体を固体状廃棄物に添
加混合するだけで良いが、無機イオン交換体が固体状廃
棄物中の金属等を固定化する反応には、水の介在が必要
であるため、飛灰、煤塵、鉱滓等を処理する場合には、
無機イオン交換体を水に分散させた状態で固体状廃棄物
に添加して混合するか、無機イオン交換体と水とを固体
状廃棄物に添加して混合する。また汚泥や土壌等には一
般に水分が含有されているため、無機イオン交換体を添
加して混合するだけでも効果があるが、必要に応じて無
機イオン交換体を水に分散させて添加するか、別に水を
添加することが好ましい。例えば金属酸化物や含水酸化
物はヒ素やセレン等の元素の陰イオンに対する固定能に
優れ、多価金属酸性塩は陽イオンの固定化能に優れるた
め、陰イオンと陽イオンとを含む場合には金属酸化物や
含水酸化物と、多価金属酸性塩とを混合して用いること
が好ましい。
[0010] The solid wastes targeted by the method of the present invention include:
Although it is incinerated ash, dust, slag, sludge, soil, etc., it is particularly suitable for treating dust in the form of fine powder. To treat these solid wastes, it is only necessary to add and mix the inorganic ion exchanger with the solid waste. However, the inorganic ion exchanger is not suitable for the reaction of immobilizing metals and the like in the solid waste. , Because water is required, when processing fly ash, dust, slag, etc.,
The inorganic ion exchanger is dispersed in water and added to and mixed with solid waste, or the inorganic ion exchanger and water are added to and mixed with solid waste. In addition, since sludge and soil generally contain moisture, it is effective to simply add and mix an inorganic ion exchanger, but if necessary, disperse the inorganic ion exchanger in water and add it. Preferably, water is separately added. For example, metal oxides and hydrated oxides have excellent ability to fix anions of elements such as arsenic and selenium, and polyvalent metal acid salts have excellent ability to fix cations. Is preferably used by mixing a metal oxide or a hydrated oxide with a polyvalent metal acid salt.

【0011】無機イオン交換体の固体状廃棄物への添加
量は、固体状廃棄物中に含まれている固定化すべき金属
等の量によっても異なるが、通常、無機イオン交換体の
使用量は固体状廃棄物の重量の0.1〜50重量%程度
の量である。
The amount of the inorganic ion exchanger to be added to the solid waste varies depending on the amount of the metal to be immobilized contained in the solid waste. The amount is about 0.1 to 50% by weight of the weight of the solid waste.

【0012】本発明において使用する無機イオン交換体
には、特にヒ酸やセレン酸等に対しては従来の金属捕集
剤より固定化能が優れているものもある。しかしなが
ら、固体状廃棄物中に含有される重金属の種類や含有比
率等によっては、無機イオン交換体とともに、通常の金
属捕集剤を併用するとより効果的で、無機イオン交換体
の使用量を少なくすることができる場合もある。しかし
ながら金属捕集剤を併用する場合には、無機イオン交換
体の性能を損なわないようにする必要があるが、無機イ
オン交換体と金属捕集剤とを同時に添加すると、無機イ
オン交換体を金属捕集剤が被覆したり、イオン交換能を
阻害する虞れがあるため、別々に添加することが好まし
い。
[0012] Some of the inorganic ion exchangers used in the present invention have a higher immobilizing ability than conventional metal collectors, especially for arsenic acid and selenic acid. However, depending on the type and content ratio of heavy metals contained in the solid waste, it is more effective to use a normal metal collecting agent together with the inorganic ion exchanger, and the amount of the inorganic ion exchanger used is reduced. Sometimes you can. However, when a metal collecting agent is used in combination, it is necessary not to impair the performance of the inorganic ion exchanger. However, when the inorganic ion exchanger and the metal collecting agent are added simultaneously, the inorganic ion exchanger becomes Since there is a possibility that the collecting agent may coat or impair the ion exchange ability, it is preferable to add them separately.

【0013】本発明方法で処理した固体状廃棄物は、そ
のまま、あるいはセメント等で固めて埋設する等によっ
て最終処分することができる。
The solid waste treated by the method of the present invention can be finally disposed as it is, or by solidifying it with cement or the like and burying it.

【0014】[0014]

【実施例】以下、実施例を挙げて本発明を更に詳細に説
明する。 実施例1〜4 ゴミ焼却場から得た煤塵100g当たりに対し、表1に
示す無機イオン交換体の10%水分散液を、無機イオン
交換体としての添加量が10gとなるように添加し、3
0分間混練した。次に処理物からの金属等の溶出試験を
行った。処理物80gを、pH=8の1000ミリリッ
トルの水中で、常温で60分間振とうし、処理物から水
中に溶出した金属等の濃度を原子吸光分析法によって測
定した。結果を表1にあわせて示す。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples. Examples 1 to 4 For 100 g of dust obtained from a garbage incineration plant, a 10% aqueous dispersion of an inorganic ion exchanger shown in Table 1 was added so that the amount of the inorganic ion exchanger added was 10 g. 3
Kneaded for 0 minutes. Next, a dissolution test of metals and the like from the treated product was performed. 80 g of the treated product was shaken at room temperature for 60 minutes in 1000 ml of water at pH = 8, and the concentration of metals and the like eluted from the treated product into water was measured by atomic absorption spectrometry. The results are shown in Table 1.

【0015】[0015]

【表1】 [Table 1]

【0016】比較例1 無機イオン交換体のかわりに、金属捕集剤としてジメチ
ルジチオカルバミン酸ナトリウムの40%水溶液を用
い、実施例1〜4と同様に試験した。結果を表1にあわ
せて示す。
Comparative Example 1 A test was conducted in the same manner as in Examples 1 to 4, except that a 40% aqueous solution of sodium dimethyldithiocarbamate was used as a metal collector instead of the inorganic ion exchanger. The results are shown in Table 1.

【0017】実施例5〜10 汚泥(含水率70%)100g当たりに、表2に示す無
機イオン交換体7gを添加し、30分間混練した。次い
で処理物の溶出試験を実施例1〜4と同様にして行っ
た。結果を表2にあわせて示す。
Examples 5 to 10 7 g of an inorganic ion exchanger shown in Table 2 was added per 100 g of sludge (water content 70%) and kneaded for 30 minutes. Next, the dissolution test of the treated product was performed in the same manner as in Examples 1 to 4. The results are shown in Table 2.

【0018】[0018]

【表2】 [Table 2]

【0019】比較例2 無機イオン交換体のかわりに、金属捕集剤としてトリア
ジンチオールを用い、実施例5〜10と同様に試験し
た。結果を表2にあわせて示す。
Comparative Example 2 A test was conducted in the same manner as in Examples 5 to 10 except that triazine thiol was used as a metal collector instead of the inorganic ion exchanger. The results are shown in Table 2.

【0020】[0020]

【発明の効果】以上説明したように本発明方法は、無機
イオン交換体を固体状廃棄物に添加して固体状廃棄物中
の有害物質を固定化する方法を採用したものであり、従
来の金属捕集剤を用いた方法では固定化が困難であった
ヒ酸やセレン酸等の有害物質が、固体状廃棄物中に含ま
れる場合でも、これらの有害物質も重金属とともに確実
に固定化できる効果を有する。
As described above, the method of the present invention employs a method in which an inorganic ion exchanger is added to solid waste to fix harmful substances in the solid waste. Even when harmful substances such as arsenic acid and selenic acid, which are difficult to immobilize by the method using a metal trapping agent, are contained in solid waste, these harmful substances can also be immobilized reliably with heavy metals. Has an effect.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 11/14 B09B 3/00 304K C09K 3/00 107 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification symbol FI C02F 11/14 B09B 3/00 304K C09K 3/00 107

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 固体状廃棄物に無機イオン交換体を添加
し、固体状廃棄物中の有害物質を無機イオン交換体によ
って固定化することを特徴とする固体状廃棄物の処理方
法。
1. A method for treating solid waste, wherein an inorganic ion exchanger is added to the solid waste, and harmful substances in the solid waste are immobilized by the inorganic ion exchanger.
【請求項2】 固体状廃棄物が煤塵である請求項1記載
の固体状廃棄物の処理方法。
2. The method for treating solid waste according to claim 1, wherein the solid waste is dust.
JP8301132A 1996-10-25 1996-10-25 Treatment of solid waste Pending JPH10128287A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8301132A JPH10128287A (en) 1996-10-25 1996-10-25 Treatment of solid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8301132A JPH10128287A (en) 1996-10-25 1996-10-25 Treatment of solid waste

Publications (1)

Publication Number Publication Date
JPH10128287A true JPH10128287A (en) 1998-05-19

Family

ID=17893209

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8301132A Pending JPH10128287A (en) 1996-10-25 1996-10-25 Treatment of solid waste

Country Status (1)

Country Link
JP (1) JPH10128287A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004314058A (en) * 2003-03-28 2004-11-11 Miyoshi Oil & Fat Co Ltd Treatment method for waste

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JPS5768186A (en) * 1980-10-14 1982-04-26 Babcock Hitachi Kk Treatment of incineration ash
JPS57150477A (en) * 1981-03-10 1982-09-17 Mitsubishi Rayon Co Ltd Treatment of arsenic-containing water
JPS57201578A (en) * 1981-06-02 1982-12-10 Takashi Hashimoto Innoxious treatment of waste of electric furnace dust
JPS61187931A (en) * 1985-02-18 1986-08-21 Asahi Chem Ind Co Ltd Adsorbent of arsenic in aqueous solution
JPH07204605A (en) * 1994-01-28 1995-08-08 Kanegafuchi Chem Ind Co Ltd Waste disposal material
JPH10113636A (en) * 1996-10-14 1998-05-06 Kanegafuchi Chem Ind Co Ltd Waste treating material and waste treating method

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