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JP3575958B2 - Apparatus and method for reducing soluble heavy metals in slag water - Google Patents
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JP3575958B2 - Apparatus and method for reducing soluble heavy metals in slag water - Google Patents

Apparatus and method for reducing soluble heavy metals in slag water Download PDF

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Publication number
JP3575958B2
JP3575958B2 JP20700397A JP20700397A JP3575958B2 JP 3575958 B2 JP3575958 B2 JP 3575958B2 JP 20700397 A JP20700397 A JP 20700397A JP 20700397 A JP20700397 A JP 20700397A JP 3575958 B2 JP3575958 B2 JP 3575958B2
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Prior art keywords
slag
water
crushed
heavy metals
pit
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JP20700397A
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JPH1151575A (en
Inventor
清一 阿部
史朗 上林
正治 岡田
哲夫 清田
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Kubota Corp
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Kubota Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、廃棄物溶融炉の燃焼室の下方に設けられたピット内に貯溜され、燃焼室より落下する溶融スラグを水砕するスラグ水砕水中の溶解性重金属の低減装置および低減方法に関する。
【0002】
【従来の技術】
廃棄物溶融炉として、たとえば図2に示したような表面溶融炉がある。この表面溶融炉では、都市ごみ焼却残渣などの廃棄物21を内筒22と外筒23との間に周方向に均一に投入して自重により炉心方向に移動させ、内筒22の内側の燃焼室24内で、燃焼装置25の燃焼熱と廃棄物21の自己燃焼熱とにより内周面側を燃焼・溶融させ、生じた溶融スラグ26を燃焼排ガスとともにスラグポート27より連続的に落下させ、冷却して凝固したスラグを取り出すようにしている。
【0003】
溶融スラグを冷却させる装置としては、操作性、メンテナンス容易性の点で優れたスラグ水砕装置が利用されることが多い。スラグ水砕装置はピット28内に水29を貯溜した簡単な構造であり、溶融スラグ26はこのスラグ水砕水29中に落下して急冷されることにより急激に熱収縮し、細粒化する。
【0004】
【発明が解決しようとする課題】
しかしながら、上記した従来のスラグ水砕装置では、スラグ水砕水はpH非調整であったため、排ガス中の酸性ガスが溶解してpHが低下し、それにより排ガス中の鉛などの重金属類が溶解することがあった。このような溶解性重金属を含んだスラグ水砕水がスラグの無数のクラックに吸収されると、将来、スラグより重金属が徐々に溶出する恐れがある。
【0005】
本発明は上記課題を解決するもので、スラグ水砕水中の溶解性重金属を低減することを目的とするものである。
【0006】
【課題を解決するための手段】
上記問題を解決するために、本発明のスラグ水砕水中の溶解性重金属の低減装置は、廃棄物溶融炉の燃焼室の下方のピット内に貯溜され、燃焼室より落下する溶融スラグを水砕するスラグ水砕水中の溶解性重金属の低減装置であって、前記スラグ水砕水のpHを連続的に測定するpH測定手段と、スラグ水砕水にアルカリ水溶液を注入するアルカリ注入手段と、前記pH測定手段とアルカリ注入手段とに接続した制御手段とを有し、この制御手段により、pH測定手段により測定されたpH値に基づいてアルカリ注入手段を制御し、スラグ水砕水をpH9〜12に維持する適当量のアルカリ水溶液を自動注入するように構成し、凝集剤注入手段を備えてピットから取り出すスラグ水砕水の全量を凝集沈殿処理する沈殿槽と、沈殿槽の上澄水をピットへ返送する手段とを有したものである。
【0007】
アルカリ水溶液としては、水酸化ナトリウム、水酸化カルシウムなどの種々のアルカリ水溶液を使用できる。また本発明のスラグ水砕水中の溶解性重金属の低減方法は、廃棄物溶融炉の燃焼室の下方のピット内に貯溜され、燃焼室より落下する溶融スラグを水砕するスラグ水砕水中の溶解性重金属の低減方法であって、前記スラグ水砕水中に飽和濃度以上の固形水酸化マグネシウムを存在させることによりスラグ水砕水のpHを自動的に10.5に維持するようにしたものである。
【0008】
上記した各構成によれば、スラグ水砕水のpHが自動的に9〜12または10.5に維持されるので、スラグ水砕水に排ガスが接触して吸収された場合も鉛などの重金属類は水酸化物を形成してSS化する。したがって、スラグ水砕水中の溶解性重金属は非常に低濃度となり、重金属類がスラグに吸収される確率、および将来スラグから重金属類が溶出する確率は非常に低くなる。
【0009】
【発明の実施の形態】
以下、本発明の実施形態を図面を参照しながら説明する。
図1において、廃棄物溶融炉の燃焼室(図示せず)の下方に設けられたピット1内に、燃焼室より落下する溶融スラグ2を水砕するスラグ水砕水3が貯溜されている。
【0010】
ピット1の内部および近傍には、スラグ水砕水3のpHを連続的に測定するpH計4と、スラグ水砕水3にNaOH水溶液を注入するNaOH注入手段5と、pH計4とNaOH注入手段5とにラインL1,L2により接続した制御装置6とが設けられており、pH計4とNaOH注入手段5と制御装置6とでスラグ水砕水中の溶解性重金属を低減する低減装置が構成されている。制御装置6は、pH計4により測定されたpH値に基づいて、スラグ水砕水3のpHが約9〜12に維持される適当量のNaOHを注入するように、NaOH注入手段5を制御するものである。
【0011】
ピット1の外部には、凝集剤注入手段7を備え、ピット1より移送されるスラグ水砕水3を凝集沈殿処理する沈殿槽8と、沈殿槽8より移送される沈降物9を脱水する脱水機10と、脱水機10より排出される脱離液と沈殿槽8より移送される上澄水11とを一旦貯溜する貯溜槽12とが設けられている。
【0012】
上記した構成における作用を説明する。
燃焼室より排出された溶融スラグ2は、ピット1内のスラグ水砕水3中に落下し、急冷されて急激に熱収縮することにより細粒化する。
【0013】
溶融スラグ2とともに燃焼室より排出された燃焼排ガスの一部はスラグ水砕水3と接触し、燃焼排ガス中の酸性ガスはスラグ水砕水3中に吸収される。
しかしこのとき、pH計4によってスラグ水砕水3のpHが連続的に測定され、測定されたpH値が制御装置6に送信され、送信されたpH値に基づいて制御装置6によりNaOH注入手段5が制御されて適当量のNaOHが注入されることにより、スラグ水砕水3のpHは9〜12に調整される。
【0014】
その結果、排ガス中の鉛などの重金属類の大部分はスラグ水砕水3に溶解することなく排ガス中に含まれたまま炉外へ流出していき、スラグ水砕水3に吸収された重金属も水酸化物を形成してSS化し、スラグ水砕水3中への溶解は防止される。
【0015】
細粒化したスラグ2Aは適宜取り出されるが、上記したようにしてスラグ水砕水3への重金属の溶解が低減されるので、スラグ2Aのクラックに重金属類が吸収される確率は低くなり、将来スラグ2Aから重金属類が溶出する恐れはほとんどない。したがって、スラグ2Aを資源として利用することも可能である。
【0016】
ピット1内の重金属水酸化物などのSSを含んだスラグ水砕水3は沈殿槽8へ移送された後に凝集剤注入手段7により凝集剤を注入され、それによりスラグ水砕水3中のSSが凝集沈殿し、沈降物9と上澄水11とに分離する。
【0017】
沈殿槽8内の沈降物9は脱水機10へ移送されて脱水され、脱水ケーキ14は系外へ搬出される。脱水機10より排出される脱離液と沈殿槽8内の上澄水11とは貯溜槽12へ移送されて一旦貯溜され、これらが混合してなる貯溜水13はピット1へ返送されて再使用される。
【0018】
上記したような溶解性重金属低減装置に代えて、ピット1内のスラグ水砕水3中に飽和濃度以上の固形水酸化マグネシウムを存在させるようにしてもよく、これによりスラグ水砕水3のpHは自動的に約10.5に維持されるので、上記と同様に鉛などの重金属類の大部分をSS化させることができ、スラグ水砕水3への重金属の溶解を低減できる。この方法は、固形水酸化マグネシウムを投入するだけなので、既設の設備で容易に実施できる。
【0019】
【発明の効果】
以上のように、本発明によれば、破砕不燃物のようにClを多く含んだ廃棄物を溶融する場合もスラグ水砕水を自動的にpH9〜12に調整できるので、排ガスよりスラグ水砕水中に持ち込まれる重金属を低減できるとともに、スラグ水砕水中に持ち込まれた重金属を水酸化物として不溶化させることができ、スラグ水砕水中の溶解性重金属を低減できる。この結果、従来のように重金属を含んだ水砕水がスラグに吸収されることがなくなり、重金属類が溶出する恐れがないスラグが得られるので、スラグの利用用途が広がり、埋め立て処分する必要もなくなる。
【図面の簡単な説明】
【図1】本発明の一実施形態におけるスラグ水砕水中の溶解性重金属の低減装置の構成を示した説明図である。
【図2】従来よりある廃棄物溶融炉の全体構成を示した断面図である。
【符号の説明】
1 ピット
2 溶融スラグ
3 スラグ水砕水
4 pH計
5 NaOH注入手段
6 制御装置
[0001]
TECHNICAL FIELD OF THE INVENTION
TECHNICAL FIELD The present invention relates to an apparatus and a method for reducing soluble heavy metals in slag granulated water for granulating molten slag that is stored in a pit provided below a combustion chamber of a waste melting furnace and falls from the combustion chamber.
[0002]
[Prior art]
As a waste melting furnace, for example, there is a surface melting furnace as shown in FIG. In this surface melting furnace, waste 21 such as municipal waste incineration residue is uniformly introduced in the circumferential direction between the inner cylinder 22 and the outer cylinder 23 and moved in the core direction by its own weight, and the combustion inside the inner cylinder 22 is performed. In the chamber 24, the inner peripheral surface side is burned and melted by the combustion heat of the combustion device 25 and the self-combustion heat of the waste 21, and the generated molten slag 26 is continuously dropped from the slag port 27 together with the combustion exhaust gas. The slag that has cooled and solidified is taken out.
[0003]
As a device for cooling the molten slag, a slag granulator excellent in operability and ease of maintenance is often used. The slag granulator has a simple structure in which water 29 is stored in a pit 28, and the molten slag 26 falls into the slag granulated water 29, is rapidly cooled, and rapidly undergoes thermal contraction to be granulated. .
[0004]
[Problems to be solved by the invention]
However, in the above-described conventional slag granulator, the pH of the granulated slag water is not adjusted, so that the acidic gas in the exhaust gas is dissolved and the pH is lowered, thereby dissolving heavy metals such as lead in the exhaust gas. There was something to do. If the slag crushed water containing such soluble heavy metals is absorbed by countless cracks in the slag, the heavy metals may be gradually eluted from the slag in the future.
[0005]
The present invention has been made to solve the above problems, and has as its object to reduce soluble heavy metals in crushed slag water.
[0006]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the apparatus for reducing soluble heavy metals in slag granulated water according to the present invention is capable of granulating molten slag stored in a pit below a combustion chamber of a waste melting furnace and falling from the combustion chamber. A device for reducing soluble heavy metals in crushed slag water, comprising: pH measuring means for continuously measuring the pH of the crushed slag water; alkali injecting means for injecting an aqueous alkali solution into the crushed slag water; and a control means connected to the pH measuring device and the alkali injection means, the control means controls the alkali injection means on the basis of the pH value measured by the pH measuring means, the slag water砕水p H9 ~ A sedimentation tank configured to automatically inject an appropriate amount of an alkaline aqueous solution maintained at 12 and equipped with a coagulant injection means to coagulate and settle the entire amount of slag crushed water taken out of the pit; It is obtained and means for returning to the pit.
[0007]
As the alkaline aqueous solution, various alkaline aqueous solutions such as sodium hydroxide and calcium hydroxide can be used. Further, the method for reducing soluble heavy metals in the crushed slag water of the present invention is characterized in that the slag is stored in a pit below a combustion chamber of a waste melting furnace, and the molten slag that falls from the combustion chamber is granulated into the slag water. a method for reducing sexual heavy metals, which was in order to maintain automatically 1 0.5 the pH of the slag water砕水by the presence of solid magnesium hydroxide over the saturation concentration in said slag water in砕水is there.
[0008]
According to the configuration described above, since the pH of the slag water砕水is maintained automatically 9-12 or 1 0.5, the slag water砕水such as lead may exhaust gas is absorbed in contact Heavy metals form hydroxides to form SS. Therefore, the soluble heavy metal in the slag crushed water has a very low concentration, and the probability that the heavy metal is absorbed by the slag and the probability that the heavy metal is eluted from the slag in the future become extremely low.
[0009]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
In FIG. 1, crushed slag water 3 for granulating molten slag 2 falling from the combustion chamber is stored in a pit 1 provided below a combustion chamber (not shown) of the waste melting furnace.
[0010]
Inside and near the pit 1, a pH meter 4 for continuously measuring the pH of the crushed slag water 3, NaOH injection means 5 for injecting an aqueous NaOH solution into the crushed slag water 3, and a pH meter 4 and NaOH injection A control device 6 connected to the means 5 by lines L1 and L2 is provided, and the pH meter 4, the NaOH injection means 5 and the control device 6 constitute a reduction device for reducing soluble heavy metals in the crushed slag water. Have been. The control device 6 controls the NaOH injecting means 5 based on the pH value measured by the pH meter 4 so as to inject an appropriate amount of NaOH so that the pH of the crushed slag water 3 is maintained at about 9 to 12. To do.
[0011]
A flocculant injection means 7 is provided outside the pit 1, and a sedimentation tank 8 for coagulating and sedimenting the crushed slag water 3 transferred from the pit 1 and a dehydration for dewatering the sediment 9 transferred from the sedimentation tank 8. An apparatus 10 and a storage tank 12 for temporarily storing the desorbed liquid discharged from the dehydrator 10 and the supernatant water 11 transferred from the sedimentation tank 8 are provided.
[0012]
The operation of the above configuration will be described.
The molten slag 2 discharged from the combustion chamber falls into the crushed slag water 3 in the pit 1, is rapidly cooled, and rapidly shrinks in heat to be refined.
[0013]
A part of the flue gas discharged from the combustion chamber together with the molten slag 2 comes into contact with the crushed slag water 3, and the acid gas in the flue gas is absorbed into the crushed slag water 3.
However, at this time, the pH of the crushed slag water 3 is continuously measured by the pH meter 4, the measured pH value is transmitted to the control device 6, and based on the transmitted pH value, the NaOH injection means is controlled by the control device 6. The pH of the slag crushed water 3 is adjusted to 9 to 12 by controlling 5 and injecting an appropriate amount of NaOH.
[0014]
As a result, most of the heavy metals such as lead in the exhaust gas flow out of the furnace without being dissolved in the crushed slag water 3 without being dissolved in the crushed slag water 3, and are absorbed by the crushed slag water 3. Also forms hydroxide to form SS, and dissolution in slag crushed water 3 is prevented.
[0015]
The finely divided slag 2A is appropriately taken out. However, since the dissolution of heavy metals in the crushed slag water 3 is reduced as described above, the probability of absorption of heavy metals into cracks in the slag 2A is reduced, and in the future, There is almost no risk that heavy metals elute from the slag 2A. Therefore, the slag 2A can be used as a resource.
[0016]
The crushed slag water 3 containing SS such as heavy metal hydroxide in the pit 1 is transferred to the sedimentation tank 8 and then the coagulant is injected by the coagulant injection means 7, whereby the SS in the crushed slag water 3 is removed. Coagulate and precipitate, and are separated into a sediment 9 and a supernatant water 11.
[0017]
The sediment 9 in the sedimentation tank 8 is transferred to a dehydrator 10 to be dehydrated, and the dehydrated cake 14 is carried out of the system. The desorbed liquid discharged from the dehydrator 10 and the supernatant water 11 in the sedimentation tank 8 are transferred to the storage tank 12 and temporarily stored, and the stored water 13 formed by mixing these is returned to the pit 1 for reuse. Is done.
[0018]
Instead of the above-described apparatus for reducing soluble heavy metals, solid magnesium hydroxide having a saturated concentration or more may be present in the crushed slag water 3 in the pit 1. Is automatically maintained at about 10.5, so that most of heavy metals such as lead can be converted to SS similarly to the above, and the dissolution of heavy metals in the crushed slag water 3 can be reduced. This method can be easily carried out with existing equipment since only solid magnesium hydroxide is charged.
[0019]
【The invention's effect】
As described above, according to the present invention, the slag crushed water can be automatically adjusted to pH 9 to 12 even when melting a waste containing a large amount of Cl such as crushed incombustibles. The heavy metals brought into the water can be reduced, and the heavy metals brought into the granulated slag water can be insolubilized as hydroxides, so that the soluble heavy metals in the granulated slag water can be reduced. As a result, water crushed water containing heavy metals is no longer absorbed by the slag as in the past, and slag is obtained without the risk of elution of heavy metals. Gone.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing a configuration of an apparatus for reducing soluble heavy metals in crushed slag water in one embodiment of the present invention.
FIG. 2 is a cross-sectional view showing the entire configuration of a conventional waste melting furnace.
[Explanation of symbols]
Reference Signs List 1 pit 2 molten slag 3 slag crushed water 4 pH meter 5 NaOH injection means 6 controller

Claims (2)

廃棄物溶融炉の燃焼室の下方のピット内に貯溜され、燃焼室より落下する溶融スラグを水砕するスラグ水砕水中の溶解性重金属の低減装置であって、前記スラグ水砕水のpHを連続的に測定するpH測定手段と、スラグ水砕水にアルカリ水溶液を注入するアルカリ注入手段と、前記pH測定手段とアルカリ注入手段とに接続した制御手段とを有し、この制御手段により、pH測定手段により測定されたpH値に基づいてアルカリ注入手段を制御し、スラグ水砕水をpH9〜12に維持する適当量のアルカリ水溶液を自動注入するように構成し、凝集剤注入手段を備えてピットから取り出すスラグ水砕水の全量を凝集沈殿処理する沈殿槽と、沈殿槽の上澄水をピットへ返送する手段とを有したことを特徴とするスラグ水砕水中の溶解性重金属の低減装置。A device for reducing soluble heavy metals in slag granulated water which is stored in a pit below a combustion chamber of a waste melting furnace and granulates molten slag falling from the combustion chamber, wherein the pH of the slag granulated water is adjusted. PH measuring means for continuously measuring, alkali injecting means for injecting an aqueous alkali solution into slag crushed water, and control means connected to the pH measuring means and the alkali injecting means, based on the measured pH value by the measuring means to control the alkali injection means, the alkaline aqueous solution in the appropriate amount to maintain the slag water砕水the p H9 to 12 configured to automatically inject, comprising a coagulant injection means Heavy water in the crushed slag water, comprising: a settling tank for coagulating and settling all of the crushed slag water taken out from the pit; and means for returning the supernatant water of the settling tank to the pit. Reduction device. 廃棄物溶融炉の燃焼室の下方のピット内に貯溜され、燃焼室より落下する溶融スラグを水砕するスラグ水砕水中の溶解性重金属の低減方法であって、前記スラグ水砕水中に飽和濃度以上の固形水酸化マグネシウムを存在させることによりスラグ水砕水のpHを自動的に10.5に維持することを特徴とするスラグ水砕水中の溶解性重金属の低減方法。A method for reducing soluble heavy metals in granulated slag water, which granulates molten slag falling from the combustion chamber and stored in a pit below a combustion chamber of a waste melting furnace, wherein the saturated concentration of the slag granulated water is reduced. the method for reducing solubility heavy metal of the slag water in砕水characterized by maintaining the pH of the slag water砕水automatically 1 0.5 the presence of more solid magnesium hydroxide.
JP20700397A 1997-08-01 1997-08-01 Apparatus and method for reducing soluble heavy metals in slag water Expired - Fee Related JP3575958B2 (en)

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JP2000335916A (en) * 1999-05-31 2000-12-05 Akio Henmi Method and apparatus for producing artificial zeolite from slag
JP4776064B2 (en) * 2000-09-01 2011-09-21 奥多摩工業株式会社 Waste stabilization treatment agent and treatment method
JP5008943B2 (en) * 2006-10-25 2012-08-22 株式会社タクマ Molten slag treatment equipment and molten slag treatment method using the equipment
JP2009120427A (en) * 2007-11-13 2009-06-04 Showa Kogyo Kk Manufacturing method for civil engineering and building materials
JP6306864B2 (en) * 2013-11-28 2018-04-04 パンパシフィック・カッパー株式会社 Method and equipment for adjusting pH of slag granulated water
CN105157438A (en) * 2015-08-17 2015-12-16 苏小明 Lead and zinc smelting cooling device fast in heat dissipation

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