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JPH047034A - Flue gas treatment material - Google Patents

Flue gas treatment material

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Publication number
JPH047034A
JPH047034A JP2106552A JP10655290A JPH047034A JP H047034 A JPH047034 A JP H047034A JP 2106552 A JP2106552 A JP 2106552A JP 10655290 A JP10655290 A JP 10655290A JP H047034 A JPH047034 A JP H047034A
Authority
JP
Japan
Prior art keywords
flue gas
powder
weight
treatment material
gas treatment
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
JP2106552A
Other languages
Japanese (ja)
Other versions
JPH07102321B2 (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 JP2106552A priority Critical patent/JPH07102321B2/en
Priority to KR1019900008075A priority patent/KR970004694B1/en
Publication of JPH047034A publication Critical patent/JPH047034A/en
Publication of JPH07102321B2 publication Critical patent/JPH07102321B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To obtain a flue gas treatment material capable of desulfurization and desalination of the flue gas by molding a mixture of incinatrated ash of gabbage, animal bone powder, alumina, clay, and organic substance powder and firing the molded body. CONSTITUTION:Incinerated ash obtained by, if necessary, drying and pulverizing gabbage incinerated ash is mixed with animal bone powder, alumina, clay, and organic substance powder (e.g. wood powder), and the mixture is molded and fired to give a flue gas treatment material. The mixing ratio is commonly 30-90 pts. by weight of animal bone powder, 10-30 pts. by weight of clay, 7-26 pts. by weight of alumina, and 3-9 pts. by weight of the organic substance powder per 100 pts. by weight of the gabbage incinerated ash. The molded body has 1-15mm grain size commonly and the drying temperature and firing temperature are respectively about 200 deg.C and 800-1200 deg.C. Using the flue gas treatment material for desulfurization and desalination of flue gases environmental pollution of the flue gases is prevented.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、生ゴミ焼却灰を利用した排煙処理材に関する
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a flue gas treatment material using garbage incineration ash.

(従来の技術) 人類が開発した近代産業、工業によって新しい文化が生
み出されているが、その反面、それに伴って自然環境に
大きな影響を与え、自然の浄化作用を越えて自然の破壊
や汚染が発生している。
(Conventional technology) A new culture has been created by modern industry and industry developed by humans, but on the other hand, it has had a great impact on the natural environment, causing destruction and pollution of nature that exceeds the purification effect of nature. It has occurred.

人類か常に健康て文化的な生活を確保するためには、産
業の発展と共にその悪影響を取り除いて生活の発展に適
した新しい環境を作り出していく必要がある。その一番
身近な生活公害の生ゴミ焼却灰処理問題が日本のみなら
ず世界各国の悩みになっている。
In order to ensure that humankind always lives a healthy and cultured life, it is necessary to eliminate the negative effects of industrial development and create a new environment suitable for the development of life. The problem of disposal of garbage incineration ash, which is the most familiar daily pollution, is a concern not only in Japan but also in countries around the world.

この生ゴミ焼却灰処理問題については各国の各関係機関
等で色々と研究されているが、抜本的な解決策は見いだ
されていないのが現状である。
Various related organizations in various countries are conducting various studies on this issue of garbage incineration ash disposal, but at present no fundamental solution has been found.

一方、従来の排煙処理法、例えば排煙脱硫には乾式法と
湿式法の二つがあり、乾式法では活性炭、活性マンガン
などに吸着または反応後、硫酸、硫酸アンモニウムなど
として回収する。湿式法では二酸化硫黄を水酸化ナトリ
ウム、炭酸ナトリウムなどの水溶液で洗浄し、吸収液に
炭酸カルシウムを加えてセラコラとして回収する方法、
水酸化アンモニウム液に吸収後、8Mアンモニウムとじ
て回収する方法などがある。
On the other hand, conventional flue gas treatment methods such as flue gas desulfurization include a dry method and a wet method. In the dry method, after adsorption or reaction with activated carbon, activated manganese, etc., sulfuric acid, ammonium sulfate, etc. are recovered. In the wet method, sulfur dioxide is washed with an aqueous solution such as sodium hydroxide or sodium carbonate, and calcium carbonate is added to the absorption liquid to recover it as Ceracola.
There is a method of absorbing it in an ammonium hydroxide solution and recovering it with 8M ammonium.

(発明が解決しようとする課題) しかしながら、これらの方法では排ガスか酸性であつt
・す、特別の装置を要する等の欠点かあった。
(Problem to be solved by the invention) However, in these methods, if the exhaust gas is acidic or
・There were some drawbacks, such as the need for special equipment.

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
方法を提供するものであり、かつ従来の排煙処理法の難
点を克服し得る、新規で画期的な排煙処理材を提供する
ものである。
The present invention provides an effective method for solving the problem of garbage incineration ash disposal, and also provides a new and innovative flue gas treatment material that can overcome the difficulties of conventional flue gas treatment methods. It is something to do.

(課題を解決するための手段) 本発明の排煙処理材は、上記目的を達成するために、生
ゴミ焼却灰を必要に応じ乾燥し粉砕して得られた焼却灰
粉を、動物骨粉、アルミナ、粘土質及び有機物粉体と混
合し成形し焼成してなることを特徴とし、 また、同様の目的で、本発明の排煙処理材は、生ゴミ焼
却灰、動物骨粉、アルミナ、粘土質を構成成分とする多
孔質であることを特徴とする。
(Means for Solving the Problems) In order to achieve the above object, the flue gas treatment material of the present invention uses incinerated ash powder obtained by drying and pulverizing garbage incinerated ash as necessary, animal bone powder, The flue gas treatment material of the present invention is characterized by being mixed with alumina, clay, and organic powder, molded, and fired; It is characterized by being porous.

生ゴミは日常生活により排出されるゴミであり、生ゴミ
焼却灰には通常、有機物、強熱減量成分、フミン酸、残
さ(二酸化ケイ素)、金属類及び有害重金属、等が含ま
れる。
Food waste is waste generated in daily life, and food waste incineration ash usually contains organic matter, ignition loss components, humic acid, residue (silicon dioxide), metals, toxic heavy metals, etc.

本発明でいう生ゴミ焼却灰としては、有害重金属を実質
的に含まない生ゴミ焼却灰が好ましい。
The garbage incineration ash referred to in the present invention is preferably garbage incineration ash that does not substantially contain harmful heavy metals.

この有害重金属を実質的に含まない生ゴミ焼却圧粉は、
生ゴミ焼却圧粉から有害重金属を除いたもの、又は生ゴ
ミを焼却する際に重金属を除去しつつ焼却して得られた
焼却灰粉、例えば重金属の吸着材の存在下に水銀、カド
ミウム、鉛、クロム等を吸着させつつ焼却して得られた
焼却灰粉である。
This garbage incineration powder, which does not substantially contain harmful heavy metals,
Food waste incineration powder from which toxic heavy metals have been removed, or incinerated ash powder obtained by incinerating food waste while removing heavy metals, such as mercury, cadmium, and lead in the presence of heavy metal adsorbents. This is incinerated ash powder obtained by incineration while adsorbing chromium, etc.

本発明で有害重金属を実質的に含まない生ゴミ焼却灰は
、通常、生ゴミ焼却灰1kg当たり、アルキル水銀0.
05mg以下、カドミウム1mg以下、鉛10mg以下
、六価クロム5mg以下であり、好ましくはこれら重金
属が検出されない焼却灰粉である。この焼却灰粉はアル
カリ性である。
In the present invention, the garbage incineration ash that is substantially free of harmful heavy metals usually has 0.00% alkylmercury per 1 kg of garbage incineration ash.
05 mg or less, cadmium 1 mg or less, lead 10 mg or less, and hexavalent chromium 5 mg or less, preferably incinerated ash powder in which these heavy metals are not detected. This incinerated ash powder is alkaline.

また、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か採
用される。
In addition, the animal bone meal is made from bones that have conventionally been mostly discarded at livestock farms, especially the bones of animals such as cows, horses, sheep, etc., which are mainly 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、9
00〜1100℃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。
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. Next, this bone is placed in a kiln and heated to 9
Baked at around 00~1100℃ for around 60~180 minutes,
Let it cool naturally in the furnace for about 60 minutes to return it to room temperature or a state close to it.

骨に骨成分以外のセラチン、脂肪、蛋白質、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。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。
If organic substances other than bone components such as seratin, fat, protein, and glue remain in the bones, they will cause oxidative decay, so it is important to ensure that they are removed. 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 bones become skeletonized and maintain the original structure having numerous pores.

上記焼成、冷却後、この骨を破砕しパウダー機にかけて
20〜200メツシユ前後、特に好ましくは50〜10
0メツシユの粉状の骨粉とする。
After the above-mentioned baking and cooling, the bone is crushed and powdered into a powder of about 20 to 200 meshes, particularly preferably 50 to 10 meshes.
0 mesh 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%の収量か得られる。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、鉄等からなっており、粒子の内外に渡っ
て無数の微小気孔か連通存在している。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 bovine bones, the above-mentioned bone powder can be obtained at a yield of 40% by weight compared to raw raw bones. The particles contain 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 consists of chlorine, amine, iron, etc., and there are countless microscopic pores that communicate inside and outside the particle. This bone meal is alkaline because it contains calcium.

粘土質はつなぎ材の役目をするものであればよく、例え
ばヘントナイト、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、等があげられる。
The clay may be anything that acts as a binder, such as hentonite, acid clay, activated clay, kaolin clay,
Examples include sericite, pyrophyllite, fireclay, montmorillonite, chloride, etc.

アルミナもつなぎ材の役目をし、添加によって、処理材
の強度が増大するが、多すぎると処理材中の細孔が少な
くなる傾向がある。
Alumina also acts as a binder, and adding it increases the strength of the treated material, but if it is added too much, the number of pores in the treated material tends to decrease.

有機物粉体は他の成分と混合し形成し焼成することによ
って焼成温度で分解し成形体中に微細孔を生ぜしぬるも
のであり、その作用を成すものであればよいが、処理材
を安価に得るには安価な材料、例えば木粉、米ぬか、麦
カス、もみがら、澱粉カス、焼酎カス、廃材の粉末、等
が好ましい。
When organic powder is mixed with other ingredients, formed, and fired, it decomposes at the firing temperature and creates micropores in the molded product, so it is fine as long as it has this effect, but it is possible to use a treatment material that is inexpensive. It is preferable to use inexpensive materials, such as wood flour, rice bran, wheat dregs, rice husks, starch dregs, shochu dregs, and waste wood powder.

本発明で用いる各成分の量割合は本発明の目的が達成さ
れる範囲内であればよい。
The amount ratio of each component used in the present invention may be within a range that achieves the object of the present invention.

その割きは通常、生ゴミ焼却圧粉100重量部に対して
、動物骨粉30〜90重量部、好ましくは45〜75重
量部:粘土質10〜30重量部、好ましくは15〜25
重量部:アルミナ7〜26重量部、好ましくは10〜1
8重量部:有機物粉体3〜9重量部、好ましくは4〜8
重量部である。
The ratio is usually 30 to 90 parts by weight of animal bone powder, preferably 45 to 75 parts by weight, and 10 to 30 parts by weight of clay, preferably 15 to 25 parts by weight, per 100 parts by weight of green waste incineration powder.
Parts by weight: 7 to 26 parts by weight of alumina, preferably 10 to 1 parts by weight
8 parts by weight: 3 to 9 parts by weight of organic powder, preferably 4 to 8 parts by weight
Parts by weight.

生ゴミ焼却圧粉は処理材の強度を大にし、かつ排煙処理
能力を増大させる。また、動物骨粉は吸着性を有し、か
つ排煙中の酸性ガスと反応する性質を有し、さらに処理
材の細孔の量を増大させる効果がある。
Garbage incineration powder increases the strength of the treated material and increases the flue gas treatment capacity. In addition, animal bone powder has adsorption properties and has the property of reacting with acidic gas in flue gas, and has the effect of increasing the amount of pores in the treated material.

本発明の処理材は上記各成分を所望の組成になるように
計量し混合し加水し成形し焼成し冷却することによって
得られる。各成分の配合割合の一態様を示すと、例えば
生ゴミ焼却灰50部(重量部、以下同じ)、動物骨粉3
0部、粘土質10部、アルミナ7部、及び有機物粉体3
部があげられる。
The treated material of the present invention is obtained by weighing and mixing the above-mentioned components to obtain a desired composition, adding water, molding, firing, and cooling. One aspect of the blending ratio of each component is, for example, 50 parts of garbage incineration ash (parts by weight, the same applies hereinafter), 3 parts of animal bone powder
0 parts, clay 10 parts, alumina 7 parts, and organic powder 3
Department can be given.

成形体は通常、粒状で大きさは1mm〜15mm程度て
あり、乾燥温度、焼成温度は通常、それぞれ200℃前
後、800〜1200℃前後である。
The molded body is usually granular and has a size of about 1 mm to 15 mm, and the drying temperature and firing temperature are usually about 200°C and 800 to 1200°C, respectively.

本発明の処理材は排煙の流路に配置し排煙と接触させて
用いられる。
The treatment material of the present invention is placed in a flue gas flow path and used in contact with the flue gas.

(効果) 本発明の処理材は生ゴミ焼却灰を利用するものであり、
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。
(Effects) The processing material of the present invention uses garbage incineration ash,
This could be an effective means of solving the problem of garbage incineration ash disposal.

本発明によれば、排煙の脱硫または脱塩を行って排煙公
害を除去することができる。例えば、工場、ゴミ焼却場
等の煙突から出る硫黄酸化物を本発明の処理材と反応さ
せて硫酸にしたり、車から出る窒素酸化物を反応させて
硝酸にしてこれらの有害物質を反応させ、かつ吸着除去
することができる。また、排煙は酸性(PH3〜4)で
あるが、本発明の処理材を用いれば処理後の排煙は中性
となる。
According to the present invention, flue gas pollution can be removed by desulfurizing or desalting flue gas. For example, sulfur oxides emitted from chimneys of factories, garbage incinerators, etc. are reacted with the treatment material of the present invention to produce sulfuric acid, nitrogen oxides emitted from cars are reacted to produce nitric acid, and these harmful substances are reacted. It can also be removed by adsorption. Moreover, although flue gas is acidic (PH3-4), if the treatment material of the present invention is used, the flue gas after treatment becomes neutral.

本発明の処理材は極めて多孔質であるため処理速度が大
きいという利点がある。
Since the treatment material of the present invention is extremely porous, it has the advantage of high treatment speed.

本発明の処理材を用いれば特別の装置を要せず、簡易に
これらの処理を行うことができる。
By using the treatment material of the present invention, these treatments can be easily performed without requiring any special equipment.

(実施例) 生ゴミ焼却灰50部、牛骨粉30部、粘土質10部、ア
ルミナ7部、及び有機物粉体3部に水を加え混合し、8
mm前後に造粒し、200℃前後で乾燥し、1000℃
前後で焼成して排煙処理材を得た。
(Example) Water was added to 50 parts of garbage incineration ash, 30 parts of beef bone powder, 10 parts of clay, 7 parts of alumina, and 3 parts of organic powder, and mixed.
Pelletize around mm, dry at around 200℃, and 1000℃
A flue gas treatment material was obtained by firing before and after.

重油の燃焼により生じた、硫黄酸化物を含むPH2〜3
の排煙を上記排煙処理材を充填した処理層を通過させた
ところ、通過後の煙りは中性で、硫黄酸化物を殆ど含ん
でいなかった。
PH2-3 containing sulfur oxides produced by combustion of heavy oil
When the flue gas was passed through a treatment layer filled with the above flue gas treatment material, the smoke after passing through was neutral and contained almost no sulfur oxides.

Claims (2)

【特許請求の範囲】[Claims] (1)生ゴミ焼却灰を必要に応じ乾燥し粉砕して得られ
た焼却灰粉を、動物骨粉、アルミナ、粘土質及び有機物
粉体と混合し成形し焼成してなる排煙処理材。
(1) A flue gas treatment material made by drying and pulverizing garbage incineration ash as necessary, mixing incineration ash powder with animal bone powder, alumina, clay, and organic powder, shaping and firing.
(2)生ゴミ焼却灰、動物骨粉、アルミナ、粘土質を構
成成分とする多孔質の排煙処理材。
(2) A porous flue gas treatment material whose constituent components are garbage incineration ash, animal bone powder, alumina, and clay.
JP2106552A 1990-04-24 1990-04-24 Flue gas treatment material Expired - Lifetime JPH07102321B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2106552A JPH07102321B2 (en) 1990-04-24 1990-04-24 Flue gas treatment material
KR1019900008075A KR970004694B1 (en) 1990-04-24 1990-05-31 Porous active material for removing harmful ingredients mainly from raw incineration ash, method for removing harmful ingredients and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2106552A JPH07102321B2 (en) 1990-04-24 1990-04-24 Flue gas treatment material

Publications (2)

Publication Number Publication Date
JPH047034A true JPH047034A (en) 1992-01-10
JPH07102321B2 JPH07102321B2 (en) 1995-11-08

Family

ID=14436510

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2106552A Expired - Lifetime JPH07102321B2 (en) 1990-04-24 1990-04-24 Flue gas treatment material

Country Status (1)

Country Link
JP (1) JPH07102321B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5288674A (en) * 1991-10-29 1994-02-22 Taylor Jr Jack H Catalytic device for treatment of combustion gases and its method of use, and the catalytic material used in the catalytic device
US5387565A (en) * 1991-10-29 1995-02-07 Taylor, Jr.; Jack H. Catalytic alloy material and catalytic device containing the same
US5505745A (en) * 1991-10-29 1996-04-09 Taylor, Jr.; Jack H. Catalytic liquid fuel product, alloy material with improved properties and method of generating heat using catalytic material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5288674A (en) * 1991-10-29 1994-02-22 Taylor Jr Jack H Catalytic device for treatment of combustion gases and its method of use, and the catalytic material used in the catalytic device
US5380506A (en) * 1991-10-29 1995-01-10 Taylor, Jr.; Jack H. Catalytic device for treatment of combustion gases and its method of use, and the catalytic material used in the catalytic device
US5387565A (en) * 1991-10-29 1995-02-07 Taylor, Jr.; Jack H. Catalytic alloy material and catalytic device containing the same
US5505745A (en) * 1991-10-29 1996-04-09 Taylor, Jr.; Jack H. Catalytic liquid fuel product, alloy material with improved properties and method of generating heat using catalytic material
US5626689A (en) * 1991-10-29 1997-05-06 Taylor, Jr.; Jack H. Method of generating heat using catalytic material
US5667751A (en) * 1991-10-29 1997-09-16 Taylor, Jr.; Jack H. Alloy material with improved catalytic properties

Also Published As

Publication number Publication date
JPH07102321B2 (en) 1995-11-08

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