JPH0461981A - Removal of heavy metal - Google Patents

Removal of heavy metal

Info

Publication number
JPH0461981A
JPH0461981A JP2168367A JP16836790A JPH0461981A JP H0461981 A JPH0461981 A JP H0461981A JP 2168367 A JP2168367 A JP 2168367A JP 16836790 A JP16836790 A JP 16836790A JP H0461981 A JPH0461981 A JP H0461981A
Authority
JP
Japan
Prior art keywords
incineration ash
heavy metal
heavy metals
granules
garbage incineration
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.)
Granted
Application number
JP2168367A
Other languages
Japanese (ja)
Other versions
JP2522717B2 (en
Inventor
Sanai Fujita
佐内 藤田
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 JP2168367A priority Critical patent/JP2522717B2/en
Publication of JPH0461981A publication Critical patent/JPH0461981A/en
Application granted granted Critical
Publication of JP2522717B2 publication Critical patent/JP2522717B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To efficiently remove a heavy metal by a method wherein garbage incineration ash containing a heavy metal and a molded and baked granular material containing animal powdered bones as an effective component are heated and mixed within a specific temp. range to adsorb the heavy metal by the granular material. CONSTITUTION:Garbage incineration ash containing a heavy metal and a molded and baked granular material containing animal powdered bones as an effective component are heated and mixed at 1000-1500 deg.C to adsorb the heavy metal in the garbage incineration ash by the granular material and the granular material after adsorption is separated from the garbage incineration ash. By this method, the heavy metal can efficiently be removed and a garbage incineration plant is prevented from becoming a heavy metal generating source. Further, since the obtained incineration ash substantially contains no heavy metal, it can be utilized in various uses.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、生ゴミ焼却灰からの重金属の除去方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for removing heavy metals from garbage incineration ash.

〔従来の技術〕[Conventional technology]

ゴミには日常生活により排出される都市ゴミと産業廃棄
物とがあり、経済活動の発展に伴いゴミは年毎に増大し
、今日生活環境問題として注目されている。
Garbage includes urban garbage and industrial waste discharged from daily life, and with the development of economic activities, the amount of garbage increases every year and is attracting attention as a living environment problem.

一般に都市ゴミを焼却すると、焼却灰中に有害重金属が
混入(例えば、カドミウム4.8ppm、鉛2600p
pm、クロム540ppm、水銀0、IPpm、)して
いる。
Generally, when municipal waste is incinerated, harmful heavy metals are mixed into the incinerated ash (for example, 4.8 ppm of cadmium, 2,600 ppm of lead).
pm, chromium 540ppm, mercury 0, IPpm).

都市ゴミ焼却灰は臨海都市の港湾埋め立て地などの処分
地で処理され、海岸線を持たない内陸都市では山間部な
どの陸上処分地で処理されているが、雨水、地下水等の
浸透によって焼却灰から有害重金属が溶出する可能性が
あり、環境汚染等の社会問題となっている。
Municipal garbage incineration ash is disposed of at disposal sites such as port landfills in coastal cities, and in inland cities that do not have coastlines, it is disposed of at land disposal sites such as mountainous areas, but incineration ash is disposed of by infiltration of rainwater, groundwater, etc. There is a possibility that harmful heavy metals may be leached out, which has become a social problem such as environmental pollution.

そこで本発明者は生ゴミ焼却灰中の重金属の除去につい
て種々検討した結果、動物骨粉を有効成分として含有す
る粒状物と生ゴミ焼却灰を加熱、混合することにより、
重金属を効率よく除去できることを見出し、本発明に到
達した。
Therefore, as a result of various studies on the removal of heavy metals from garbage incineration ash, the present inventor found that by heating and mixing granular material containing animal bone powder as an active ingredient and garbage incineration ash,
We have discovered that heavy metals can be removed efficiently and have arrived at the present invention.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明は、生ゴミ焼却灰中の重金属を効率よく除去する
方法を提供するものである。
The present invention provides a method for efficiently removing heavy metals from garbage incineration ash.

〔課題を解決するための手段〕[Means to solve the problem]

本発明は、重金属を含有する生ゴミ焼却灰を、動物骨粉
を有効成分として含有し粒状に、成形、焼成してなる粒
状物と、1000〜1500℃で加熱、混合し、生ゴミ
焼却灰中の重金属を粒状物に吸着させ、吸着後の粒状物
を生ゴミ焼却灰と分離することを特徴とする重金属の除
去方法である。
In the present invention, food waste incineration ash containing heavy metals is heated and mixed at 1000 to 1500°C with granules containing animal bone meal as an active ingredient, formed into granules, and fired. This is a method for removing heavy metals, which is characterized by adsorbing heavy metals onto granules and separating the adsorbed granules from garbage incineration ash.

生ゴミは日常生活により排出されるゴミであり、通常の
方法で焼却すると有機物、強熱減量成分、フミン酸、残
さく二酸化ケイ素)、金属類及び有害重金属(例えば、
カドミウム、鉛、クロム、水銀などン、等が含まれる。
Garbage is waste generated from daily life, and when incinerated in the usual way, organic matter, ignition loss components, humic acid, residual silicon dioxide), metals, and toxic heavy metals (e.g.
Contains cadmium, lead, chromium, mercury, etc.

生ゴミ焼却灰は粉砕して粉末にされる。粉末の大きさは
通常、50〜100メツシユである。
Garbage incineration ash is crushed into powder. The size of the powder is usually 50 to 100 mesh.

本発明において、動物骨粉を有効成分とする粒状物は重
金属の吸着に有効な動物骨粉と成形用のつなぎ材、及び
必要に応じて他の添加材を配合して混合し、粒状に成形
し、乾燥し、焼成してなるものである。
In the present invention, the granular material containing animal bone powder as an active ingredient is prepared by mixing animal bone powder effective for adsorbing heavy metals, a binder for molding, and other additives as necessary, and forming the mixture into granules. It is dried and fired.

ここで用いる動物骨粉は、従来畜産場等でほとんど廃棄
されていた骨、特に牛、馬、羊等の硬骨が主体の動物の
骨が採用される。
The animal bone meal used here uses bones that have conventionally been mostly discarded at livestock farms, especially bones of animals such as cows, horses, and sheep, which are mainly composed of hard bones.

これらの動物の生骨は焼成しやすい大きさに切断し、そ
の上で圧力釜に投入し、200〜400℃前後で、約9
0分前後煮沸する。次いでこの骨を焼成炉に入れ、90
0〜1100℃前後で、60〜180分前後焼成し、そ
のまま炉内で60分前後自然冷却させて室温乃至これに
近い状態に戻す、骨に青成分以外のゼラチン、脂肪、蛋
白スにかわ等の有機物が残存すると酸化腐敗の原因とな
るので、これを確実に除去しておくことが重要である。
The raw bones of these animals are cut into sizes that are easy to burn, then put into a pressure cooker and heated at around 200 to 400 degrees Celsius for about 90 minutes.
Boil for about 0 minutes. The bones were then placed in a kiln for 90
Bake at around 0~1100℃ for around 60~180 minutes, then let it cool naturally in the oven for around 60 minutes to return to room temperature or a state close to this. If any organic matter remains, it will cause oxidative decay, so it is important to ensure that this is removed.

上記煮沸工程によって、外側のみならず気孔内に付着し
ている有機物を骨から六方分離除去することができる。
By the above boiling process, organic matter adhering not only to the outside but also to the inside of the pores can be separated and removed from the bone in all directions.

その上で上記焼成工程を通すことによって、残存する有
機物を完全に除去することができ、同時に骨中の湿度(
水分)を数%以下、好ましくはほぼ0%にまで低下させ
ることができる。上記焼成条件によれば、骨は白骨化し
て無数の気孔を有した原形組織状態を維持する。
By then passing through the above baking process, remaining organic matter can be completely removed, and at the same time the humidity in the bone can be reduced.
The water content can be reduced to several percent or less, preferably to almost 0%. According to the above-mentioned firing conditions, the bone turns into a skeleton and maintains its original tissue state having countless pores.

上記焼成冷却後、この骨を破砕しパウダー機にかけて2
0〜200メツシユ前後、特に好ましくは50〜100
メツシユの粉状の骨粉とする。
After the above firing and cooling, the bones are crushed and put into a powder machine for 2
Around 0 to 200 meshes, particularly preferably 50 to 100 meshes
It is made into powdered bone meal.

上記骨粉は、牛骨の場合、原料の生骨に比して重量比的
40%の収量が得られる1粒子は、カルシウム(約33
重量%)を主成分とし、リン(約16.7%)、バリウ
ム(約1.03%)、ナトリウム(約0.76%)、イ
オウ(約0.64%)、他にマグネシウム、カリウム、
塩素、アミン、鉄等から成っており、粒子の内外に渡っ
て無数の微小気孔が連通存在している。この骨粉はカル
シウムを含有するためアルカリ性である。
In the case of the bone powder mentioned above, in the case of cow bones, one particle that yields 40% of the yield by weight compared to raw raw bone has calcium (approximately 33
The main components are phosphorus (about 16.7%), barium (about 1.03%), sodium (about 0.76%), sulfur (about 0.64%), and magnesium, potassium,
It is composed of chlorine, amine, iron, etc., and has countless microscopic pores that communicate with each other both inside and outside the particle. This bone meal is alkaline because it contains calcium.

つなぎ材は、動物骨粉を粒状に成形、焼成するためのつ
なぎの役目をするものであればよく、例えばベントナイ
ト、酸性白土、活性白土、カオリン粘土、セリサイト、
パイロフィライト、耐火粘土、モンモリロナイト、クロ
ライド、アルミナ等が挙げられる。つなぎ材の他に必要
に応じて他の充填材、添加材を加えてもよい。
The binder may be anything that acts as a binder for shaping and firing the animal bone meal into granules, such as bentonite, acid clay, activated clay, kaolin clay, sericite, etc.
Examples include pyrophyllite, fireclay, montmorillonite, chloride, and alumina. In addition to the binder, other fillers and additives may be added as necessary.

動物骨粉を有効成分とする粒状物中の動物骨粉の割合は
、粒状物が吸着作用を有すればよく特に限定されないが
、吸着速度を考慮すれば動物骨粉の量の多いものが好ま
しい、吸着速度の大きい好ましい組成として例えば、動
物骨粉とつなぎ材との合計量に対して動物骨粉が60〜
80%があげられる。
The proportion of animal bone meal in granules containing animal bone meal as an active ingredient is not particularly limited as long as the granules have an adsorption effect, but in consideration of adsorption speed, a large amount of animal bone meal is preferable. For example, a preferable composition with a large amount of animal bone meal is 60 to 60% of the total amount of animal bone meal and binder.
80% can be given.

粒状物は動物骨粉につなぎ材、必要に応じて他の充填材
、添加材、及び水を加え混合し、粒状に成形し、乾燥し
、焼成して得られる0粒状物の大きさは生ゴミ焼却戻粉
よりも大きく、その粒度の大きさによって生ゴミ焼却灰
との分離が容易なものであればよい。その大きさは、通
常、5〜20mmである。焼成炉としては例えば回転焼
成炉が用いられる。
The granular material is obtained by mixing animal bone meal with a binder, other fillers, additives, and water as necessary, forming it into granules, drying, and baking.The size of the granular material is similar to that of raw garbage. Any material may be used as long as it is larger than the incineration return powder and can be easily separated from the garbage incineration ash due to its particle size. Its size is usually 5 to 20 mm. As the firing furnace, for example, a rotary firing furnace is used.

本発明においては重金属を含有する生ゴミ焼却灰に対す
る動物骨粉を有効成分とする粒状物の割合を多くするこ
とによって重金属の吸着速度が大きくなるが、粒状物の
割合を30%〜50%にすれば重金属の吸着速度を十分
大きくし得る。
In the present invention, the rate of adsorption of heavy metals increases by increasing the ratio of granular materials containing animal bone meal as an active ingredient to the garbage incineration ash containing heavy metals, but the adsorption rate of heavy metals increases when the ratio of granular materials is 30% to 50%. In this case, the adsorption rate of heavy metals can be sufficiently increased.

生ゴミ焼却灰と粒状物は十分に混合しつつ1000〜1
500℃で加熱されるが、加熱時に十分に混合して重金
属と粒状物の接触をよくすることが好ましい。その点で
混合、焼成装置としてはロータリーキルンが好ましく、
傾斜されたキルンの入口から生ゴミ焼却灰と粒状物が供
給され、回転混合によって十分混合され加熱されて出口
から混合物が排出される。生ゴミ焼却灰は粉状であるの
で、減圧または真空吸引によって供給することができる
While thoroughly mixing the garbage incineration ash and granules,
Although it is heated at 500° C., it is preferable to thoroughly mix it during heating to improve the contact between the heavy metal and the particulate matter. From this point of view, a rotary kiln is preferable as a mixing and baking device.
Garbage incineration ash and granules are fed from the inclined inlet of the kiln, thoroughly mixed and heated by rotary mixing, and the mixture is discharged from the outlet. Since garbage incineration ash is in powder form, it can be supplied by reduced pressure or vacuum suction.

焼成後の混合物からの灰と粒状物との分離は、粒の大き
さを利用して行う。分離には振動ふるいを用いるのが効
率の点で好ましい。前記の混合、焼成にロータリーキル
ン、分離に振動ふるいを用いて、この両者を順に接続す
れば、連続的に混合焼成、分離が可能である。
Separation of ash and granules from the mixture after firing is performed by utilizing the size of the granules. From the viewpoint of efficiency, it is preferable to use a vibrating sieve for separation. If a rotary kiln is used for mixing and baking, and a vibrating screen is used for separation, and these are connected in sequence, mixing, baking, and separation can be performed continuously.

ふるいの穴の径は通常、3〜5mm程度で十分であり、
ふるいを用いると粒状物が上に残り、生ゴミ焼却灰は下
から回収される。
The diameter of the holes in the sieve is usually about 3 to 5 mm,
When using a sieve, the granules remain on top and the garbage incineration ash is collected from below.

かくして粒状物から分離することにより、重金属(水銀
、カドミウム、鉛、クロム等)を実質的に含まない生ゴ
ミ焼却灰が得られる。また、重金属を吸着した粒状物は
酸で洗浄することにより、再使用することができる。
By separating the granules in this manner, garbage incineration ash substantially free of heavy metals (mercury, cadmium, lead, chromium, etc.) can be obtained. Moreover, the granules that have absorbed heavy metals can be reused by washing with acid.

〔効果〕〔effect〕

本発明によれば、重金属を実質的に含まない生ゴミ焼却
灰が得られるので、本発明は生ゴミ焼却灰処理問題を解
決する一つの有力な手段となり得る。
According to the present invention, garbage incineration ash that is substantially free of heavy metals can be obtained, so the present invention can be an effective means for solving the problem of garbage incineration ash disposal.

また、ゴミ焼却場が重金属の発生源になるのを防止する
こともできる。
It can also prevent garbage incinerators from becoming a source of heavy metals.

さらに、本発明により得られた焼却灰は重金属を実質的
に含まないので、多面的な用途に利用し得るという利点
がある。
Furthermore, since the incineration ash obtained by the present invention does not substantially contain heavy metals, it has the advantage that it can be used for a variety of purposes.

〔実施例〕〔Example〕

■粒状物の製造 牛骨粉と粘土とを各々の割合が、60重量%、40重量
%になるように配合し、水を加えて混合し、径が5mm
の粒状に成形し、回転する焼成炉中で約1000℃で焼
成し、動物骨粉を有効成分とする粒状物を製造した。
■Manufacture of granules Blend beef bone powder and clay in proportions of 60% by weight and 40% by weight, add water and mix.
The mixture was molded into granules and fired at about 1000°C in a rotating kiln to produce granules containing animal bone powder as an active ingredient.

■生ゴミの焼却灰からの重金属分離 生ゴミ焼却灰(カドミウム4.8ppm、鉛2600p
pm、クロム540ppm、水銀0.1ppm)に上記
の粒状物を、各々の割合が60重量%、40重量%にな
るようにロータリーキルンの入口から供給し、1200
℃で加熱、混合し、出口から生ゴミ焼却灰と重金属を吸
着した粒状物の混合物を取り出し、そのまま振動ふるい
(穴の大きさ3mm)にかけた。
■Separation of heavy metals from garbage incineration ash (cadmium 4.8ppm, lead 2600p)
pm, chromium 540 ppm, mercury 0.1 ppm) from the inlet of a rotary kiln so that the respective ratios were 60% by weight and 40% by weight.
The mixture was heated and mixed at .degree. C., and the mixture of garbage incineration ash and heavy metal-adsorbed granules was taken out from the outlet and passed through a vibrating sieve (hole size: 3 mm).

粒状物はふるいの上に残り、生ゴミ焼却灰はふるいの下
から回収された。この生ゴミ焼却灰の溶出試験を行い原
子吸光光度法(計量の限界;カドミウム0.01mg/
l、鉛0.1mg/j+、クロム0.05mg/l、水
銀0.0005mg/l)で重金属の含量を測定したと
ころ、重金属は検出されなかった。
The granules remained on top of the sieve, and the garbage incineration ash was collected from below the sieve. The elution test of this garbage incineration ash was conducted using atomic absorption spectrophotometry (limit of measurement; cadmium 0.01mg/
When the content of heavy metals was measured, no heavy metals were detected.

Claims (2)

【特許請求の範囲】[Claims] (1)重金属を含有する生ゴミ焼却灰を、動物骨粉を有
効成分として含有し粒状に、成形、焼成してなる粒状物
と、1000〜1500℃で加熱、混合し、生ゴミ焼却
灰中の重金属を粒状物に吸着させ、吸着後の粒状物を生
ゴミ焼却灰と分離することを特徴とする重金属の除去方
法。
(1) Food waste incineration ash containing heavy metals is heated and mixed at 1000 to 1500°C with granules containing animal bone meal as an active ingredient, formed into granules, and fired. A method for removing heavy metals, which is characterized by adsorbing heavy metals onto granular materials and separating the adsorbed granular materials from garbage incineration ash.
(2)重金属を含有する生ゴミ焼却灰を、動物骨粉を有
効成分として含有し粒状に、成形、焼成してなる粒状物
と、1000〜1500℃で加熱、混合し、生ゴミ焼却
灰中の重金属を粒状物に吸着させ、吸着後の粒状物を分
離してなる重金属が除去された生ゴミ焼却灰。
(2) Food waste incineration ash containing heavy metals is heated and mixed at 1000 to 1500°C with granules containing animal bone meal as an active ingredient, molded and fired. Garbage incineration ash from which heavy metals have been removed is obtained by adsorbing heavy metals onto granules and separating the adsorbed granules.
JP2168367A 1990-06-28 1990-06-28 Heavy metal removal method Expired - Lifetime JP2522717B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2168367A JP2522717B2 (en) 1990-06-28 1990-06-28 Heavy metal removal method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2168367A JP2522717B2 (en) 1990-06-28 1990-06-28 Heavy metal removal method

Publications (2)

Publication Number Publication Date
JPH0461981A true JPH0461981A (en) 1992-02-27
JP2522717B2 JP2522717B2 (en) 1996-08-07

Family

ID=15866778

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2168367A Expired - Lifetime JP2522717B2 (en) 1990-06-28 1990-06-28 Heavy metal removal method

Country Status (1)

Country Link
JP (1) JP2522717B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7217401B2 (en) * 1999-08-17 2007-05-15 Wisconsin Electric Power Company Mercury removal from activated carbon and/or fly ash

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7217401B2 (en) * 1999-08-17 2007-05-15 Wisconsin Electric Power Company Mercury removal from activated carbon and/or fly ash

Also Published As

Publication number Publication date
JP2522717B2 (en) 1996-08-07

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