JP2001096134A - Treatment method of combustion gas containing heavy metal - Google Patents
Treatment method of combustion gas containing heavy metalInfo
- Publication number
- JP2001096134A JP2001096134A JP27548599A JP27548599A JP2001096134A JP 2001096134 A JP2001096134 A JP 2001096134A JP 27548599 A JP27548599 A JP 27548599A JP 27548599 A JP27548599 A JP 27548599A JP 2001096134 A JP2001096134 A JP 2001096134A
- Authority
- JP
- Japan
- Prior art keywords
- heavy metals
- heavy metal
- exhaust gas
- gas containing
- combustion exhaust
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Incineration Of Waste (AREA)
- Treating Waste Gases (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Chimneys And Flues (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】 本発明は、燃焼排ガス中に
含まれる水銀およびその他の重金属を効率的かつ低コス
トで除去することができる重金属を含む燃焼排ガスの処
理方法に関するものである。TECHNICAL FIELD The present invention relates to a method for treating a flue gas containing a heavy metal, which can remove mercury and other heavy metals contained in the flue gas efficiently and at low cost.
【0002】[0002]
【従来の技術】 廃棄物の焼却炉から排出される燃焼排
ガス中には水銀や鉛、砒素等の有害な重金属が含まれて
おり、このような重金属を含む燃焼排ガスの処理方法と
しては集塵機やスクラバ等を用いて重金属の除去処理を
行なっているのが普通で、除去した燃焼排ガス中の重金
属は焼却灰や大気やスクラバ排水等の中に排出されてい
る。そして現在、焼却灰および排水中の重金属濃度は排
出規制がなされており、焼却灰の場合には溶出基準値も
クリアさせる必要がある。BACKGROUND ART Harmful heavy metals such as mercury, lead, and arsenic are contained in flue gas discharged from waste incinerators. As a method for treating such flue gas containing heavy metals, dust collectors, It is common to use a scrubber or the like to remove heavy metals, and the heavy metals in the removed combustion exhaust gas are discharged into incinerated ash, air, scrubber drainage, and the like. At present, emissions of heavy metals in incineration ash and wastewater are regulated, and in the case of incineration ash, it is necessary to clear the elution standard value.
【0003】 一方、将来的には排ガス中の重金属濃
度、特に水銀が規制対象になると言われているが、水銀
は水溶性/非水溶性の二つの存在形態があるため、スク
ラバでは水溶性の水銀は除去されるが非水溶性の水銀は
除去されず大気内に排出されてしまうという問題点があ
った。また、集塵処理した焼却灰の溶出基準値厳格化に
伴い、焼却灰に対して重金属の安定化処理を施す必要性
が高まってくるが、焼却灰への重金属固定剤の混練やセ
メント固化や溶融固化等の従来法による安定化処理方法
では焼却灰全量を対象に行う必要があるため、処理コス
トが高くなるという問題点があった。更には、大気に水
銀等の重金属を排出させない処理手段として活性炭や吸
着剤等による吸着除去方法も知られているが、余分な処
理コストがかかるという問題点があった。On the other hand, it is said that the concentration of heavy metals in exhaust gas, particularly mercury, will be regulated in the future. However, since mercury has two water-soluble and non-water-soluble forms, scrubbers use water-soluble. There is a problem that mercury is removed but non-water-soluble mercury is not removed and is discharged into the atmosphere. In addition, the need to stabilize heavy metals in incinerated ash has increased with the tightening of the elution standard value for incinerated ash after dust collection.However, kneading of heavy metal fixing agents into incinerated ash, cement solidification, In the stabilization method by the conventional method such as melting and solidification, since it is necessary to perform the entire incineration ash, there is a problem that the processing cost is increased. Further, as a treatment means for preventing the discharge of heavy metals such as mercury into the atmosphere, an adsorption removal method using activated carbon, an adsorbent or the like is known, but there is a problem that extra treatment cost is required.
【0004】[0004]
【発明が解決しようとする課題】 本発明は上記のよう
な従来の問題点を解決して、集塵処理工程を効率的かつ
低コストで行うことができるとともに、水溶性/非水溶
性の二つの存在形態がある水銀の除去についても活性炭
や吸着剤等を必要とせず低コストで行うことができる重
金属を含む燃焼排ガスの処理方法を提供することを目的
として完成されたものである。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems and enables the dust collection process to be performed efficiently and at low cost. The present invention has been completed for the purpose of providing a method for treating combustion exhaust gas containing heavy metals, which can be performed at low cost without requiring activated carbon or an adsorbent for the removal of mercury having two forms.
【0005】[0005]
【課題を解決するための手段】 上記の課題を解決する
ためになされた本発明は、廃棄物の焼却炉から排出され
る重金属を含む燃焼排ガスの処理方法において、高効率
集塵機により集塵処理を施す前に燃焼排ガスに重金属固
定剤と焼却灰と水から得た焼却灰スラリーを噴霧し、燃
焼排ガス中の重金属を該スラリーに吸着させるようにし
たことを特徴とするものである。なお、前記の処理を施
す前に、焼却炉から排出される重金属を含む燃焼排ガス
をホットサイクロンあるいはセラミックフィルタにより
重金属の沸点以上の温度で集塵処理し、低沸点の重金属
を焼却灰内へ移行させることなく有害性の低い焼却灰と
して取り出しておけば処理効率を著しく高めることがで
き好ましい。また、反応塔の後段に高効率集塵機とスク
ラバが順次配置し、重金属固定剤と高効率集塵機で集塵
した焼却灰とスクラバの排水とで焼却灰スラリーを得る
ことが好ましい。更に、反応塔を出た燃焼排ガスを高効
率集塵機内のフィルタに形成された焼却灰と重金属固定
剤の混合物からなる1次濾過層を通過させることにより
ガス状の重金属元素を吸着除去するようにすることもで
きる。なお、高効率集塵機としてはセラミックフィルタ
またはバグフィルタを用いればよい。Means for Solving the Problems The present invention made to solve the above-mentioned problems is directed to a method for treating combustion exhaust gas containing heavy metals discharged from a waste incinerator. Before application, incineration ash slurry obtained from a heavy metal fixing agent, incineration ash and water is sprayed on the combustion exhaust gas, and the heavy metal in the combustion exhaust gas is adsorbed on the slurry. Before performing the above treatment, the combustion exhaust gas containing heavy metals discharged from the incinerator is subjected to dust collection at a temperature higher than the boiling point of the heavy metals by a hot cyclone or a ceramic filter, and the heavy metals having a low boiling point are transferred into the incineration ash. It is preferable to take out the incinerated ash with low toxicity without causing the treatment efficiency to be significantly increased. In addition, it is preferable that a high-efficiency dust collector and a scrubber are sequentially arranged at the subsequent stage of the reaction tower, and an incineration ash slurry is obtained from the heavy metal fixing agent, the incineration ash collected by the high-efficiency dust collector, and the scrubber wastewater. Furthermore, the gaseous heavy metal element is adsorbed and removed by passing the combustion exhaust gas exiting the reaction tower through a primary filtration layer formed of a mixture of incineration ash and a heavy metal fixing agent formed in a filter in a high-efficiency dust collector. You can also. Note that a ceramic filter or a bag filter may be used as the high-efficiency dust collector.
【0006】[0006]
【発明の実施の形態】 以下に、図面を参照しつつ本発
明の好ましい実施の形態を示す。図面は、本発明に供さ
れる処理装置の一例を示す概略図であり、図中1は流動
炉のような廃棄物の焼却炉、2は該焼却炉1から排出さ
れた燃焼排ガスを集塵処理するためのホットサイクロ
ン、3は該ホットサイクロンで捕集されない燃焼排ガス
中の重金属を吸着処理するためのベンチュリー式あるい
はサイクロン式の反応塔であり、前記ホットサイクロン
2と反応塔3の間には流動空気予熱用の予熱器4aおよ
び白煙防止用の予熱器4bが設けられている。5は反応
塔3から出た焼却灰を含む燃焼排ガスを集塵処理するた
めのセラミックフィルタあるいはバグフィルタ等の高効
率の集塵機、6は該集塵機5の燃焼排ガスから更に重金
属を除去するための循環型のスクラバ、7は煙突であ
る。そして、前記集塵機5で集塵した焼却灰とスクラバ
6からの排水、および薬剤投入器8から投入した高分子
キレート剤や硫化剤等の重金属固定剤をスラリー化する
ための焼却灰スラリー槽9が設けられ、得られたスラリ
ーを前記の反応塔3へ供給されるよう構成されている。Preferred embodiments of the present invention will be described below with reference to the drawings. The drawings are schematic views showing an example of a processing apparatus provided for the present invention. In the drawing, reference numeral 1 denotes a waste incinerator such as a fluidized-bed furnace, and 2 denotes a dust collecting apparatus for collecting combustion exhaust gas discharged from the incinerator 1. The hot cyclone 3 for the treatment is a Venturi-type or cyclone-type reaction tower for adsorbing heavy metals in the combustion exhaust gas not collected by the hot cyclone, and the hot cyclone 2 and the reaction tower 3 are disposed between the hot cyclone 2 and the reaction tower 3. A preheater 4a for preheating the flowing air and a preheater 4b for preventing white smoke are provided. Reference numeral 5 denotes a high-efficiency dust collector such as a ceramic filter or a bag filter for collecting dust from the combustion exhaust gas containing incineration ash from the reaction tower 3, and 6 denotes a circulation for further removing heavy metals from the combustion exhaust gas of the dust collector 5. The mold scrubber, 7 is a chimney. An incineration ash slurry tank 9 for slurrying the incineration ash collected by the dust collector 5 and the drainage from the scrubber 6 and the heavy metal fixing agent such as a polymer chelating agent and a sulfide agent introduced from the chemical injector 8 is provided. The slurry is provided to be supplied to the reaction tower 3.
【0007】 次に、以上のような処理装置により燃焼
排ガスを処理する工程を説明する。先ず最初に、焼却炉
1から排出された水銀や鉛、砒素等の重金属を含む燃焼
排ガスはホットサイクロン2により粒子の大きな灰分が
集塵処理される。この時、ホットサイクロン2は700
〜850℃程度の高温場になっており、水銀等の重金属
は粒子径が約10μm 以下の微粒子状あるいはガス状で
あるのでホットサイクロン2では捕集されない。従っ
て、ホットサイクロン2では有害な重金属を含まない無
害の焼却灰を大量に捕集できることとなり、以後の工程
では灰分の少なくなった重金属を含んだ燃焼排ガスのみ
を対象に処理すればよく、効率的な処理が可能となる。Next, a description will be given of a process of treating the combustion exhaust gas by the above-described processing apparatus. First, the combustion exhaust gas containing heavy metals such as mercury, lead, and arsenic discharged from the incinerator 1 is subjected to dust collection by the hot cyclone 2 to remove ash having large particles. At this time, hot cyclone 2 is 700
It is in a high temperature field of about 850 ° C., and heavy metals such as mercury are not collected in the hot cyclone 2 because they are in the form of fine particles or gas having a particle diameter of about 10 μm or less. Therefore, the hot cyclone 2 can collect a large amount of harmless incinerated ash that does not contain harmful heavy metals. In the subsequent steps, only the flue gas containing ash-reduced heavy metals needs to be treated, so that it is efficient. Processing can be performed.
【0008】 次に、焼却炉1から排出された燃焼排ガ
スは流動空気予熱用の予熱器4aおよび白煙防止用の予
熱器4bを通過して約350℃とされ、反応塔3へ導入
される。そしてこの反応塔3内における冷却過程おいて
燃焼排ガス中の重金属が凝縮し、該重金属が反応塔3内
に供給されたスラリーに吸着・固定化して安定した状態
で効率よく重金属が除去されることとなる。この時、図
示の装置においては、反応塔3の後段にある集塵機5で
集塵した焼却灰とスクラバ6からの排水、および薬剤投
入器8から投入した重金属固定剤をスラリー化するため
の焼却灰スラリー槽9が設けられ、ここで得られた焼却
灰スラリーを反応塔3へ供給されるよう構成されている
ので、低コストでの処理が可能となる。なお、前記の重
金属固定剤としてはキレート化合物化する高分子キレー
ト剤や、硫化物化する硫化ソーダや水硫化ソーダ等の硫
化剤が用いられ、焼却灰に対し1〜10%の範囲で混合
する。また、スクラバ6からの排水は焼却灰に対し10
〜100倍量の範囲で混合する。Next, the combustion exhaust gas discharged from the incinerator 1 passes through a preheater 4 a for preheating the flowing air and a preheater 4 b for preventing white smoke, and is brought to about 350 ° C., and is introduced into the reaction tower 3. . During the cooling process in the reaction tower 3, heavy metals in the combustion exhaust gas are condensed, and the heavy metals are adsorbed and fixed on the slurry supplied into the reaction tower 3 so that the heavy metals are efficiently removed in a stable state. Becomes At this time, in the illustrated apparatus, the incinerated ash collected by the dust collector 5 and the drainage from the scrubber 6 at the subsequent stage of the reaction tower 3 and the incinerated ash for slurrying the heavy metal fixing agent supplied from the chemical input device 8 are used. Since the slurry tank 9 is provided, and the incinerated ash slurry obtained here is configured to be supplied to the reaction tower 3, the processing can be performed at low cost. As the heavy metal fixing agent, a polymer chelating agent for forming a chelate compound or a sulphidating agent such as sodium sulfide or sodium hydrosulfide for sulphidizing is used, and is mixed in the range of 1 to 10% with respect to incinerated ash. In addition, the wastewater from the scrubber 6 is 10
Mix in a range of ~ 100 times.
【0009】 次に、反応塔3から排出された燃焼排ガ
スはセラミックフィルタあるいはバグフィルタのような
高効率な集塵機5により更に集塵処理されることとな
る。ここでは燃焼排ガスがフィルタに形成された焼却灰
と重金属固定剤の混合物からなる1次濾過層を通過する
ことにより、ガス状態にある水銀等の重金属元素が重金
属固定剤により効率よく吸着除去されることとなる。ま
た更に、次工程のスクラバ6によって水銀のような水溶
性の重金属元素を除去することにより、最終的に基準値
以下の安全な浄化ガスとして煙突7より大気へ放出す
る。なお、スクラバ6により除去処理された重金属は焼
却灰スラリー槽9へ導入され、重金属固定剤と反応して
安定化されることとなる。Next, the combustion exhaust gas discharged from the reaction tower 3 is further subjected to dust collection processing by a highly efficient dust collector 5 such as a ceramic filter or a bag filter. Here, the combustion exhaust gas passes through a primary filtration layer formed of a mixture of incineration ash and a heavy metal fixing agent formed on the filter, so that heavy metal elements such as mercury in a gaseous state are efficiently adsorbed and removed by the heavy metal fixing agent. It will be. Further, by removing a water-soluble heavy metal element such as mercury by a scrubber 6 in the next step, the gas is finally discharged from the chimney 7 to the atmosphere as a safe purified gas having a reference value or less. The heavy metal removed by the scrubber 6 is introduced into the incineration ash slurry tank 9 and is stabilized by reacting with the heavy metal fixing agent.
【0010】 以上のように、集塵機5により集塵処理
を施す前に燃焼排ガスに重金属固定剤と焼却灰と水から
得た焼却灰スラリーを噴霧し、燃焼排ガス中の重金属を
該スラリーに吸着させるようにすることにより、重金属
を安定化して集塵処理工程を効率的かつ低コストで行う
ことができることとなる。また、最初の段階において燃
焼排ガスをホットサイクロン2で重金属の沸点以上の温
度で集塵処理することにより、燃焼排ガス中から重金属
をほとんど含まない無害な焼却灰として取り出すととも
に、後段の反応塔3と高効率の集塵機5とスクラバ6で
有害な重金属を除去処理するようにし、効率的かつ低コ
ストな処理が実現できることとなる。As described above, before performing dust collection processing by the dust collector 5, the incineration ash slurry obtained from the heavy metal fixing agent, the incineration ash, and the water is sprayed on the combustion exhaust gas, and the heavy metal in the combustion exhaust gas is adsorbed on the slurry. By doing so, the heavy metal can be stabilized and the dust collection process can be performed efficiently and at low cost. In the first stage, the flue gas is subjected to dust collection in a hot cyclone 2 at a temperature equal to or higher than the boiling point of heavy metals, thereby taking out as harmless incinerated ash containing almost no heavy metals from the flue gas. The harmful heavy metal is removed by the high-efficiency dust collector 5 and the scrubber 6, so that efficient and low-cost processing can be realized.
【0011】 なお、以上の処理方法により下水汚泥の
燃焼排ガスの処理を行いホットサイクロン2で回収され
た焼却灰および高効率の集塵機5で回収された焼却灰に
対し、環境庁告示第13号に基づき重金属の溶出試験を
行った結果、いずれも有害物質の溶出基準値を下回るも
のであることが確認できた(表1参照)。また、スクラ
バ6から排出される燃焼排ガス中の重金属濃度も検出限
界値以下であることも確認できた。また、都市ゴミの燃
焼排ガスについても同様の処理を行った結果、いずれも
基準値をクリアするものであることが確認でき(表2参
照)、特にこの場合にはホットサイクロン2により焼却
灰を分離処理しておかなくても水銀の除去が満足に行わ
れていることが確認できた。In addition, the incineration ash collected by the hot cyclone 2 and the incineration ash collected by the high-efficiency dust collector 5 after the treatment of the sewage sludge combustion exhaust gas by the above-mentioned treatment method are notified to the Environment Agency Notification No. 13 As a result of performing a dissolution test for heavy metals based on the results, it was confirmed that all were below the standard value for dissolution of harmful substances (see Table 1). It was also confirmed that the concentration of heavy metals in the combustion exhaust gas discharged from the scrubber 6 was below the detection limit. In addition, as a result of performing the same treatment on the flue gas of municipal garbage, it was confirmed that all of them cleared the reference value (see Table 2). In this case, in particular, incineration ash was separated by hot cyclone 2. It was confirmed that the mercury was removed satisfactorily without any treatment.
【0012】[0012]
【表1】下水汚泥焼却灰の溶出 [Table 1] Elution of sewage sludge incineration ash
【0013】[0013]
【表2】都市ゴミ焼却飛灰の溶出 [Table 2] Leaching of fly ash from incineration of municipal waste
【0014】[0014]
【発明の効果】 以上の説明からも明らかなように、本
発明は集塵処理工程を効率的かつ低コストで行うことが
できるとともに、水溶性/非水溶性の二つの存在形態が
ある水銀の除去についても活性炭や吸着剤等を必要とせ
ず低コストで行うことができるものである。更には、最
初の段階において燃焼排ガスをホットサイクロンで集塵
処理することにより燃焼排ガス中から重金属をほとんど
含まない無害な焼却灰として取り出し、残りの排ガスの
みを対象に集塵処理することにより効率的かつ低コスト
な処理が実現できるものである。よって本発明は従来の
問題点を一掃した重金属を含む燃焼排ガスの処理方法と
して、産業の発展に寄与するところは極めて大である。As is clear from the above description, the present invention can perform the dust collection process efficiently and at low cost, and has two water-soluble / water-insoluble forms of mercury. The removal can be performed at low cost without requiring activated carbon or an adsorbent. Furthermore, in the first stage, the flue gas is subjected to dust collection in a hot cyclone to remove it from the flue gas as harmless incineration ash containing almost no heavy metals, and the remaining flue gas is collected only for efficient treatment. In addition, low-cost processing can be realized. Therefore, the present invention greatly contributes to the development of industry as a method for treating combustion exhaust gas containing heavy metals that has eliminated the conventional problems.
【図1】 本発明の一実施の形態に供される処理装置を
示す概略図である。FIG. 1 is a schematic diagram showing a processing apparatus provided for an embodiment of the present invention.
1 焼却炉、2 ホットサイクロン、3 反応塔、5
高効率な集塵機、6スクラバ、9 焼却灰スラリー槽。1 incinerator, 2 hot cyclone, 3 reaction tower, 5
High efficiency dust collector, 6 scrubbers, 9 incineration ash slurry tank.
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3K070 DA01 DA11 DA17 DA24 DA29 DA45 3K078 AA05 BA03 BA21 CA24 4D002 AA28 AA29 AC04 BA04 BA12 BA13 BA14 CA01 DA02 DA15 DA35 DA61 DA66 GA02 GA03 GB02 GB03 GB08 4K056 AA05 CA20 DB07 DB13 ────────────────────────────────────────────────── ─── Continued on the front page F term (reference) 3K070 DA01 DA11 DA17 DA24 DA29 DA45 3K078 AA05 BA03 BA21 CA24 4D002 AA28 AA29 AC04 BA04 BA12 BA13 BA14 CA01 DA02 DA15 DA35 DA61 DA66 GA02 GA03 GB02 GB03 GB08 4K056 AA05 CA20 DB07 DB13
Claims (5)
含む燃焼排ガスの処理方法において、高効率集塵機によ
り集塵処理を施す前に燃焼排ガスに重金属固定剤と焼却
灰と水から得た焼却灰スラリーを噴霧し、燃焼排ガス中
の重金属を該スラリーに吸着させるようにしたことを特
徴とする重金属を含む燃焼排ガスの処理方法。1. A method for treating a combustion exhaust gas containing heavy metals discharged from a waste incinerator, wherein the combustion exhaust gas is obtained from a heavy metal fixing agent, incineration ash, and water before being subjected to dust collection by a high-efficiency dust collector. A method for treating a combustion exhaust gas containing a heavy metal, comprising spraying an ash slurry and adsorbing the heavy metal in the combustion exhaust gas to the slurry.
排出される重金属を含む燃焼排ガスをホットサイクロン
あるいはセラミックフィルタにより重金属の沸点以上の
温度で集塵処理し、低沸点の重金属を焼却灰内へ移行さ
せることなく有害性の低い焼却灰として取り出しておく
請求項1に記載の重金属を含む燃焼排ガスの処理方法。2. The method according to claim 1, wherein the flue gas containing heavy metals discharged from the incinerator is subjected to dust collection at a temperature higher than the boiling point of the heavy metals by a hot cyclone or a ceramic filter to remove heavy metals having a low boiling point. The method for treating a combustion exhaust gas containing heavy metals according to claim 1, wherein the ash is taken out as incineration ash having low harm without being transferred into the incineration ash.
よびスクラバが順次配置され、重金属固定剤と高効率集
塵機で集塵した焼却灰とスクラバの排水とで焼却灰スラ
リーを得るようにした請求項1または2に記載の重金属
を含む燃焼排ガスの処理方法。3. A reactor, a high-efficiency dust collector, and a scrubber are sequentially arranged at a stage subsequent to the incinerator, and an incineration ash slurry is obtained by using a heavy metal fixing agent, incineration ash collected by the high-efficiency dust collector, and drainage of the scrubber. A method for treating a combustion exhaust gas containing a heavy metal according to claim 1.
内のフィルタに形成された焼却灰と重金属固定剤の混合
物からなる1次濾過層を通過させることによりガス状の
重金属元素を吸着除去するようにした請求項1または2
または3に記載の重金属を含む燃焼排ガスの処理方法。4. A gaseous heavy metal element is adsorbed and removed by passing a flue gas discharged from a reaction tower through a primary filtration layer formed of a mixture of incinerated ash and a heavy metal fixing agent formed on a filter in a high efficiency dust collector. Claim 1 or 2 wherein
Or a method for treating a combustion exhaust gas containing a heavy metal according to item 3.
またはバグフィルタを用いた請求項1または2または3
または4に記載の重金属を含む燃焼排ガスの処理方法。5. A high efficiency dust collector using a ceramic filter or a bag filter.
Or a method for treating a combustion exhaust gas containing a heavy metal according to 4.
Priority Applications (1)
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JP27548599A JP2001096134A (en) | 1999-09-29 | 1999-09-29 | Treatment method of combustion gas containing heavy metal |
Applications Claiming Priority (1)
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JP27548599A JP2001096134A (en) | 1999-09-29 | 1999-09-29 | Treatment method of combustion gas containing heavy metal |
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Publication Number | Publication Date |
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JP2001096134A true JP2001096134A (en) | 2001-04-10 |
Family
ID=17556189
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JP27548599A Pending JP2001096134A (en) | 1999-09-29 | 1999-09-29 | Treatment method of combustion gas containing heavy metal |
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JP2002336641A (en) * | 2001-05-18 | 2002-11-26 | Nkk Corp | Method for refining gas generated from waste |
JP2005211877A (en) * | 2004-02-02 | 2005-08-11 | Ngk Insulators Ltd | Method for reducing heavy metal in ash of gasification furnace |
JP2006116526A (en) * | 2004-09-24 | 2006-05-11 | Ngk Insulators Ltd | Treatment method for exhaust gas of sewage sludge incinerator |
JP2008221205A (en) * | 2007-02-13 | 2008-09-25 | Metawater Co Ltd | Dust collection method of exhaust gas from sludge incinerator |
WO2010084594A1 (en) * | 2009-01-22 | 2010-07-29 | 太平洋セメント株式会社 | Heavy metal removing apparatus and cement production system |
KR20110031975A (en) * | 2008-07-14 | 2011-03-29 | 게아 프로세스 엔지니어링 아/에스 | Spray dryer absorption process for flue gas with entrained coarse particles |
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1999
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002336641A (en) * | 2001-05-18 | 2002-11-26 | Nkk Corp | Method for refining gas generated from waste |
JP4573536B2 (en) * | 2004-02-02 | 2010-11-04 | メタウォーター株式会社 | Method for reducing heavy metals in ash in gasifier |
JP2005211877A (en) * | 2004-02-02 | 2005-08-11 | Ngk Insulators Ltd | Method for reducing heavy metal in ash of gasification furnace |
JP2006116526A (en) * | 2004-09-24 | 2006-05-11 | Ngk Insulators Ltd | Treatment method for exhaust gas of sewage sludge incinerator |
JP4630156B2 (en) * | 2004-09-24 | 2011-02-09 | メタウォーター株式会社 | Exhaust gas treatment method for sewage sludge incinerator |
JP2008221205A (en) * | 2007-02-13 | 2008-09-25 | Metawater Co Ltd | Dust collection method of exhaust gas from sludge incinerator |
KR20110031975A (en) * | 2008-07-14 | 2011-03-29 | 게아 프로세스 엔지니어링 아/에스 | Spray dryer absorption process for flue gas with entrained coarse particles |
KR101686153B1 (en) | 2008-07-14 | 2016-12-28 | 게아 프로세스 엔지니어링 아/에스 | Spray dryer absorption process for flue gas with entrained coarse particles |
WO2010084594A1 (en) * | 2009-01-22 | 2010-07-29 | 太平洋セメント株式会社 | Heavy metal removing apparatus and cement production system |
US8679234B2 (en) | 2009-01-22 | 2014-03-25 | Taiheiyo Cement Corporation | Heavy metal removing apparatus and cement production system |
KR101610988B1 (en) * | 2009-01-22 | 2016-04-08 | 타이헤이요 세멘트 가부시키가이샤 | Heavy metal removing apparatus and cement production system |
JP2012242029A (en) * | 2011-05-23 | 2012-12-10 | Metawater Co Ltd | Heat recovery system from exhaust gas of incinerator |
CN112781059A (en) * | 2019-11-06 | 2021-05-11 | 中国石油化工股份有限公司 | Incineration device and method for treating solid hazardous waste |
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