JP3869695B2 - Waste melting furnace operation method - Google Patents
Waste melting furnace operation method Download PDFInfo
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- JP3869695B2 JP3869695B2 JP2001306869A JP2001306869A JP3869695B2 JP 3869695 B2 JP3869695 B2 JP 3869695B2 JP 2001306869 A JP2001306869 A JP 2001306869A JP 2001306869 A JP2001306869 A JP 2001306869A JP 3869695 B2 JP3869695 B2 JP 3869695B2
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- waste
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Description
【0001】
【発明の属する技術分野】
本発明は、都市ごみと都市ごみ以外の掘り起こしごみなど灰分の高い異種ごみを竪型シャフト炉で溶融処理する廃棄物の溶融処理方法に関する。
【0002】
【従来の技術】
廃棄物には、都市ごみを主体とした一般廃棄物、各種産業廃棄物又はそれらの焼却処理によって得られた中間処理物である焼却灰、飛灰、破砕不純物やそれらをいったん埋立処理した後、再度掘り起こした土砂分を含む埋立ごみ、汚泥等がある。この廃棄物溶融処理は、廃棄物を溶融炉の上部より装入し、また、1回に投入するごみ量に対して副原料として石灰石や珪石などの塩基度調整剤とともにコークスを一定量装入し、炉底部の羽口から酸素含有ガスまたは酸素富化ガス、あるいはその上方の羽口から空気を吹き込み、廃棄物を乾燥、予熱、熱分解、燃焼、溶融し、スラグやメタルとして取り出すものである。スラグの有効活用のためには、そのスラグの物性が重要になってくる。また、スラグの流動性は、炉底部からの排出にあたっての重要な要因であり、前記したスラグの物性、品質に大きく影響する。
【0003】
例えば、特公昭55−21923号公報には、溶融炉における廃棄物の溶融処理方法において、スラグの成分が1>CaO/SiO2>0.5になるように廃棄物に石灰類を補給して操業することが記載されている。この操業は、比較的性状の安定した都市ごみを主とし、最終的なスラグの塩基度のみを副資材の投入目標としている。
【0004】
昨今、最終処分場不足から溶融処理によるスラグ化が推進されており、中でも異種ごみの処理が注目されている。異種ごみとは、他工場(ストーカ炉・流動床)から排出された焼却灰、焼却飛灰や最終処分場から埋め立てごみを掘り起こした灰分の高いものである。特に掘り起こしごみには飛散・臭気の観点から覆土が混入しているが、重金属等の有害物に汚染されていることから一括して溶融・無害化が求められている。
【0005】
【発明が解決しようとする課題】
現在、竪型シャフト炉では、混合率管理のため異種ごみを炉頂から層状に投入し、塩基度調整剤(石灰類)はスラグの塩基度が0.5〜1.1になるように調整している。
【0006】
しかし、雑多なごみを処理する場合において、例えば、掘り起こしごみの場合、焼却に適さないプラスチック、焼却灰、覆土、建設廃材等が混在し、灰分が都市ごみの5〜10%に比べて15〜30%と高く、一定量の塩基度調整剤を投入しても、部分的には塩基度の偏差が大きい。特に掘り起こしごみの処理では覆土の混入の多寡により単味の塩基度が0.02〜0.3と大きく変動し、部分的に塩基度の高低が激しい。更に、灰や掘り起こしごみ等の不燃層と石灰層が厚く、混合性が悪いために、スラグの融点が高くなる傾向にある。その結果、羽口前ではスラグ粘性が高くなり、羽口やコークスへのスラグの付着等でコークスの燃焼性が阻害され、結果として、羽口輝度悪化、スラグ温度低下によりスラグの流動性が悪化し最悪の時は出湯不能となる。そのためのランスによるスラグ加熱作業の負荷の増加が生じ、またその対策としてCR上昇が必要となる。
【0007】
そこで、本発明は、都市ごみと、都市ごみ以外の焼却灰や掘り起こしごみなど灰分の高い異種ごみとを廃棄物溶融炉で溶融処理する廃棄物溶融炉の操業方法において、スラグの流動性を良好にして安定した操業ができる廃棄物溶融炉の操業方法を提供するものである。
【0008】
【課題を解決するための手段】
本発明は、都市ごみと、都市ごみ以外の焼却灰や掘り起こしごみなど灰分の高い異種ごみとを廃業物溶融炉で溶融処理する廃棄物溶融炉の操業方法において、異種ごみに必要とされる塩基度を算出し、異種ごみの灰分毎の土混入率と塩基度との関係から異種ごみに混合する石灰石の量を求め、この求められた量の石灰石類を、あらかじめ、異種ごみと混合し、該異種ごみと前記都市ごみをピット内でクレーンにて混合して装入することを特徴とする。更に、該混合物中の都市ごみに必要とされる石灰石類と交互に装入してもよい。
【0009】
また、本発明は、都市ごみと、都市ごみ以外の焼却灰や掘り起こしごみなど灰分の高い異種ごみとを廃棄物溶融炉で溶融処理する廃棄物溶融炉の操業方法において、都市ごみと異種ごみとを混合した時に必要とされる塩基度を算出し、該塩基度に基づいて決定された量の石灰石類を、あらかじめ、異種ごみと混合し、該異種ごみと前記都市ごみをピット内でクレーンにて混合して装入することを特徴とする。
【0010】
【発明の実施の形態】
図1は、溶融炉内におけるごみと石灰分の分布(装入状態)を示す模式図で、(a)及び(b)は本発明、(c)及び(d)は比較例である。
【0011】
図1(d)は、都市ごみのみを処理する場合で、都市ごみ1と、該都市ごみに必要とされる量の石灰2を炉頂から交互に層状に投入して溶融処理する一般的なものである。
【0012】
都市ごみは一般的に雑多なものから構成されているため、この場合、全体の塩基度は、0.8〜1の範囲に維持されるように、まず、平均的なごみ質から、ごみltあたりに必要とする石灰石類の量を決定し、ごみの投入量(kg/ch)にあわせて、その都度、投入量を決定し装入する。都市ごみは、灰分が少ないため炉下部の灰層が薄く石灰石も混じり易く、溶融物の融点も下がり、安定操業が出来る。
【0013】
図1(c)は、都市ごみ1と異種ごみ3を合わせて同時に処理せんとするもので、都市ごみと異種ごみとのそれぞれの平均的ごみ質から1t当たりに必要とする塩基度を算出し、更に、両者の混合率を正確に把握し、その両者のごみ装入量に合わせて装入すべき石灰石類の量を決定する。
【0014】
その装入方法は以下の要領で行った。
【0015】
(c−1)は、都市ごみ1と異種ごみ3とは混合せず、単独で交互に炉頂から層状に装入し、その間に、都市ごみ1に必要とする量の石灰石類2及び異種ごみ3に必要とする量の石灰石類4をそれぞれ層状に装入した。
【0016】
(c−2)は、事前に都市ごみ1と異種ごみ3とは混合して、その混合物を炉頂から層状に装入し、その間に、両者に必要とする量の石灰石類2及び4を合わせてそれぞれ層状に装入した。
【0017】
(c−1)にあっては、それぞれのごみ1,3と石灰石2,4の境界面は塩基度が調整されるが、層状の異種ごみ中央部分は塩基度調整が不十分で融点が下がってくれず、スラグの流動性が低下して、羽口へのスラグの付着等により、ますます羽口前の燃焼が悪化し、安定した操業が出来なかった。
【0018】
(c−2)にあっては、都市ごみ1と異種ごみ3とは混合しているため、当然の事ながらごみの層が厚くなり、それだけ、均一な塩基度調整は難しく、(c−1)と同じように境界面以外の融点が下がってくれずスラグの流動性が低下して、安定した操業が出来なかった。特に、異種ごみが掘り起こしごみの場合、石灰石が混じっていない層の塩基度が極度に下がるため、出湯出来ない等の現象が生じた。
【0019】
また、通常、都市ごみと異種ごみの混合は、ごみピットとごみクレーンで行われるため、(c−2)の場合1chの混合したごみの中の各の重量比率を正確に把握することは難しく、1chの塩基度にも大きなバラツキが生じた。
【0020】
図1(a)は、本発明方法で、あらかじめ、異種ごみに必要とされる塩基度を算出し、該塩基度に基づいて装入すべき石灰石量を決定し、この決定された量の石灰石4を炉内に装入する前に、事前に、異種ごみ3と混合する。次に、この混合物3,4を、更に、都市ごみ1と混合する。
【0021】
この3者1,3,4の混合物を、都市ごみ1に必要とされる量の石灰石類2と交互に層状に装入する。
【0022】
本発明者は、実験で、異種ごみの塩基度は0.5〜1.2の範囲にすれば、所望とするスラグの流動性が得られることを見いだした。
【0023】
更に、0.5〜1.2の範囲の塩基度に維持するには、異種ごみ1tに対して石灰石類のCaO量で56〜224kg(石灰石量で100〜400kg)装入すればよいことも見いだした。
【0024】
このように、事前に異種ごみ3と石灰石類4を事前に混合して装入すれば、常に、異種ごみ部分の塩基度は調整され融点が下がるため溶けやすくなり、且つ、全体的に石灰が分散されて炉内の塩基度のバラツキが平滑化される。更に、事前に石灰石を混合した異種ごみと一般ごみの混合作業は、ピット内でクレーンを使って行うため、それぞれの重量比率を正確に把握することは難しいが、多少、異種ごみ、特に、掘り起こしごみの場合、混合率がバラツイても異種ごみ自体の塩基度が事前に調整されているため、1chの塩基度のバラツキが少なく安定した操業が得られる。
【0025】
図1(b)は、本発明の別の態様を示すもので、まず、都市ごみ1と異種ごみ3を混合したときに必要とされる塩基度を算出し、該塩基度に基づいて石灰石の量を決定し、この決定された量の石灰石2,4を炉内に装入する前に、まず、異種ごみ3と混合し、次に、都市ごみ1と混合して炉内に装入している。
【0026】
この方法にあっても、異種ごみ部分の塩基度が調整されているため、被溶融物の融点が下がり炉全体として安定操業が得られた。
【0027】
本発明者の実験では、都市ごみと一般ごみとの混合物の塩基度は、0.8〜1の範囲を維持するように石灰石類を装入すれば、適正な溶融が得られることを見いだした。
【0028】
図2は、異種ごみ中の土混入率と事前石灰石混合量(kg/異種ごみt)と石灰混合後の異種ごみ部分の塩基度との関係の一例を示す図である。図2は、異種ごみ(土混入前)の灰分が30%の場合を示し、土の混入割合に応じて土混入後の異種ごみ部分の塩基度を0.5〜1.2にするために、異種ごみlt当たりに事前に混合する事前混合石灰石比(kg)を求めることが出来る。
【0029】
例えば、覆土の混入率30%未満の場合で事前混合石灰石比を100〜200、30〜70%の場合では、事前混合石灰石比を200〜400にすればよい。
【0030】
このように、異種ごみの灰分毎に土混入率と塩基度との関係を求めておけば、異種ごみの種類に応じて混合する石灰石量を容易に求めることが出来る。
【0031】
都市ごみ700kg、灰分30%の異種ごみ(掘り起こしごみ)231kg(そのうち覆土69kg)を溶融処理する場合、異種ごみを図2のグラフから69kgの石灰石と混合して塩基度を0.85とし、全体の塩基度を0.88なるように石灰石を50kg投入する。なお、石灰類とは、石灰石をはじめ、CaOを含む物質全般を示し、例えば消石灰を含んだ廃棄物溶融炉集じん灰も利用できる。また、CaOだけでなくMgOを含む物質でも同等の効果が得られる。
【0032】
【発明の効果】
本発明によれば、都市ごみと異種ごみを溶融処理する場合、スラグの流動性を悪化させることなく良好に維持することができ、その結果、作業負荷やCRが低減できる。
【図面の簡単な説明】
【図1】溶融炉内におけるごみと石灰分の分布を示す模式図で、(a)及び(b)は本発明、(c)〜(d)は比較例である。
【図2】異種ごみの土混合率と塩基度との関係を示す図である。
【符号の説明】
1:都市ごみ
2:石灰
3:異種ごみ
4:石灰[0001]
BACKGROUND OF THE INVENTION
TECHNICAL FIELD The present invention relates to a waste melting method for melting different types of waste with high ash content such as municipal waste and digging waste other than municipal waste in a vertical shaft furnace.
[0002]
[Prior art]
Wastes include municipal waste, mainly industrial waste, various industrial wastes, or incineration ash, fly ash, crushed impurities and intermediate treatment products obtained by incineration, There are landfill waste, sludge, etc. that contain earth and sand that have been dug up again. In this waste melting treatment, waste is charged from the upper part of the melting furnace, and a certain amount of coke is charged as a secondary raw material with a basicity adjusting agent such as limestone or silica as the auxiliary material. In addition, oxygen-containing gas or oxygen-enriched gas is blown from the tuyeres at the bottom of the furnace, or air is blown from the tuyere above, and the waste is dried, preheated, pyrolyzed, burned, melted, and taken out as slag or metal. is there. For the effective use of slag, the physical properties of the slag are important. The slag fluidity is an important factor in discharging from the bottom of the furnace and greatly affects the physical properties and quality of the slag.
[0003]
For example, in Japanese Patent Publication No. 55-21923, in a method for melting waste in a melting furnace, lime is supplied to the waste so that the component of slag is 1> CaO / SiO 2 > 0.5. It is stated that it will operate. This operation is mainly for municipal waste with relatively stable properties, and only the basicity of the final slag is set as the input target for secondary materials.
[0004]
In recent years, slag conversion by melting treatment has been promoted due to the shortage of final disposal sites. Heterogeneous waste is incinerated ash discharged from other factories (stoker furnaces / fluidized beds), incinerated fly ash, and high ash content from landfill waste from the final disposal site. In particular, the excavated waste is covered with soil covering from the viewpoint of scattering and odor, but since it is contaminated with heavy metals and other harmful substances, melting and detoxification are required in a lump.
[0005]
[Problems to be solved by the invention]
Currently, in vertical shaft furnaces, different types of waste are introduced in layers from the top of the furnace to control the mixing rate, and the basicity modifier (limes) is adjusted so that the basicity of the slag is 0.5 to 1.1. is doing.
[0006]
However, when miscellaneous waste is treated, for example, in the case of digging waste, plastics, incineration ash, covering soil, construction waste, etc. that are not suitable for incineration are mixed, and ash content is 15 to 30% compared to 5 to 10% of municipal waste. Even if a certain amount of basicity adjusting agent is added, the basicity deviation is partially large. In particular, in the treatment of excavated waste, the simple basicity varies greatly from 0.02 to 0.3 due to the amount of covering soil, and the basicity is partially high and low. Furthermore, since the incombustible layer such as ash and digging waste and the lime layer are thick and the mixing property is poor, the melting point of the slag tends to increase. As a result, the slag viscosity increases in front of the tuyere, and the flammability of the coke is hindered due to adhesion of slag to the tuyere and coke. In the worst case, it becomes impossible to pour hot water. For this purpose, an increase in the load of the slag heating work due to the lance occurs, and it is necessary to raise the CR as a countermeasure.
[0007]
Therefore, the present invention provides good slag fluidity in a waste melting furnace operating method in which municipal waste and high-ash waste such as incineration ash and excavated waste other than municipal waste are melted in the waste melting furnace. Therefore, the present invention provides a method for operating a waste melting furnace capable of stable operation.
[0008]
[Means for Solving the Problems]
The present invention relates to a waste melting furnace operating method in which municipal waste and high-ash waste such as incineration ash and excavated waste other than municipal waste are melted in a waste melting furnace. Calculate the amount of limestone mixed with the different types of waste from the relationship between the soil contamination rate and basicity for each ash content of the different types of waste, and mix this amount of limestone with the different types of waste in advance. The dissimilar waste and the municipal waste are mixed and charged by a crane in a pit. Furthermore, you may charge alternately with the limestone required for the municipal waste in this mixture.
[0009]
The present invention also relates to a waste melting furnace operating method in which municipal waste and different types of high-ash waste such as incineration ash and excavated waste other than municipal waste are melted in a waste melting furnace. The basicity required when mixing the wastewater, the amount of limestone determined based on the basicity is mixed with the foreign waste in advance, and the foreign waste and the municipal waste are put into the crane in the pit. It is characterized by mixing and charging.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a schematic diagram showing the distribution (charged state) of dust and lime in the melting furnace, (a) and (b) are the present invention, and (c) and (d) are comparative examples.
[0011]
FIG. 1 (d) shows a case in which only municipal waste is treated, and the
[0012]
Since municipal waste is generally composed of miscellaneous items, in this case, from the average waste quality, the average basic waste is The amount of limestone required for the operation is determined, and the input amount is determined and charged according to the input amount of garbage (kg / ch). Municipal waste has a low ash content, so the ash layer at the bottom of the furnace is thin and easy to mix with limestone, and the melting point of the melt is lowered, enabling stable operation.
[0013]
Fig. 1 (c) shows that
[0014]
The charging method was as follows.
[0015]
(C-1) does not mix the
[0016]
(C-2) mixes
[0017]
In (c-1), the basicity is adjusted at the boundary between each of the
[0018]
In (c-2), since the
[0019]
In addition, since municipal waste and different types of waste are usually mixed with a waste pit and a waste crane, in the case of (c-2), it is difficult to accurately grasp each weight ratio in 1ch mixed waste. There was a large variation in the basicity of 1ch.
[0020]
FIG. 1 (a) shows a method for calculating the basicity required for different kinds of waste in advance by the method of the present invention, determining the amount of limestone to be charged based on the basicity, and determining the determined amount of limestone. Before charging 4 into the furnace, it is mixed with the
[0021]
The mixture of the three
[0022]
The inventor has found through experiments that the desired fluidity of the slag can be obtained if the basicity of the different types of waste is in the range of 0.5 to 1.2.
[0023]
Furthermore, in order to maintain the basicity in the range of 0.5 to 1.2, it is only necessary to charge 56 to 224 kg (100 to 400 kg in terms of limestone) of CaO of limestone with respect to 1 t of different types of waste. I found it.
[0024]
In this way, if different kinds of
[0025]
FIG. 1 (b) shows another embodiment of the present invention. First, the basicity required when the
[0026]
Even in this method, since the basicity of the different types of waste was adjusted, the melting point of the melted material was lowered, and stable operation was obtained as a whole furnace.
[0027]
In the experiments of the present inventors, it was found that the basic melt of the mixture of municipal waste and general waste can obtain proper melting if limestones are charged so as to maintain the range of 0.8-1. .
[0028]
FIG. 2 is a diagram showing an example of the relationship between the soil mixing rate in different types of waste, the amount of limestone mixed in advance (kg / type of different types of waste t), and the basicity of different types of trash after mixing with lime. FIG. 2 shows a case where the ash content of different kinds of waste (before soil mixing) is 30%, in order to make the basicity of the different kinds of garbage after soil mixing 0.5 to 1.2 according to the soil mixing ratio. The pre-mixed limestone ratio (kg) to be mixed in advance per different kind of waste lt can be obtained.
[0029]
For example, when the premixed limestone ratio is less than 30% and the premixed limestone ratio is 100 to 200 and 30 to 70%, the premixed limestone ratio may be 200 to 400.
[0030]
Thus, if the relationship between soil mixing rate and basicity is calculated | required for every ash content of different kinds of garbage, the amount of limestone mixed according to the kind of different kinds of garbage can be calculated | required easily.
[0031]
When melting waste of 231 kg of municipal waste (kg kg) and ash content of 30% (of which 69 kg of covered soil) is melted, the basic waste is mixed with 69 kg of limestone from the graph in FIG. 50 kg of limestone is added so that the basicity of the mixture becomes 0.88. Lime refers to limestone and all materials containing CaO. For example, waste melting furnace dust containing slaked lime can also be used. Further, not only CaO but also a substance containing MgO can obtain the same effect.
[0032]
【The invention's effect】
According to the present invention, when municipal waste and different types of waste are melted, it can be maintained well without deteriorating the fluidity of slag, and as a result, work load and CR can be reduced.
[Brief description of the drawings]
FIG. 1 is a schematic diagram showing the distribution of trash and lime in a melting furnace, (a) and (b) are the present invention, and (c) to (d) are comparative examples.
FIG. 2 is a diagram showing the relationship between soil mixing ratio and basicity of different types of waste.
[Explanation of symbols]
1: Municipal waste 2: Lime 3: Heterogeneous waste 4: Lime
Claims (4)
異種ごみに必要とされる塩基度を算出し、異種ごみの灰分毎の土混入率と塩基度との関係から異種ごみに混合する石灰石量を求め、この求められた量の石灰石類を、あらかじめ、異種ごみと混合し、該異種ごみと前記都市ごみをピット内でクレーンにて混合して装入することを特徴とする廃棄物溶融炉の操業方法。In the operation method of waste melting furnace that melts municipal waste and different kinds of high-ash waste such as incineration ash and digging waste other than municipal waste in the waste melting furnace,
The basicity required for different types of waste is calculated, the amount of limestone mixed in the different types of waste is calculated from the relationship between the soil contamination rate and the basicity of each type of ash in the different types of waste, and this amount of limestone is determined in advance. A method for operating a waste melting furnace, comprising mixing with different kinds of garbage, mixing the different kinds of garbage and the municipal waste with a crane in a pit, and charging them.
異種ごみに必要とされる塩基度を算出し、異種ごみの灰分毎の土混入率と塩基度との関係から異種ごみに混合する石灰石の量を求め、この求められた量の石灰石類を、あらかじめ、異種ごみと混合し、更に、該異種ごみと前記都市ごみをピット内でクレーンにて混合し、該混合物中の都市ごみに必要とされる石灰石類と交互に装入することを特徴とする廃棄物溶融炉の操業方法。In the operation method of the waste melting furnace that melts municipal waste and different types of waste with high ash content such as incineration ash and digging waste other than municipal waste in the waste melting furnace,
The basicity required for different types of waste is calculated, the amount of limestone mixed in the different types of waste is calculated from the relationship between the soil contamination rate and basicity of each type of ash in the different types of waste, and this amount of limestone is Mixing with different types of waste in advance, further mixing the different types of waste and the municipal waste with a crane in a pit, and alternately charging with limestones required for the municipal waste in the mixture To operate waste melting furnace.
都市ごみと異種ごみとを混合した時に必要とされる塩基度を算出し、該塩基度に基づいて決定された量の石灰石類を、あらかじめ、異種ごみと混合し、更に、該異種ごみと前記都市ごみをピット内でクレーンにて混合して装入することを特徴とする廃棄物溶融炉の操業方法。 In the operation method of the waste melting furnace that melts municipal waste and different types of waste with high ash content such as incineration ash and digging waste other than municipal waste in the waste melting furnace,
The basicity required when mixing municipal waste and different types of waste is calculated, the amount of limestone determined based on the basicity is mixed with the different types of waste in advance, and further A method for operating a waste melting furnace, characterized in that municipal waste is mixed and charged in a pit with a crane .
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