JP2003055010A - Pretreating method for raw material in manufacture of cement - Google Patents

Pretreating method for raw material in manufacture of cement

Info

Publication number
JP2003055010A
JP2003055010A JP2001239541A JP2001239541A JP2003055010A JP 2003055010 A JP2003055010 A JP 2003055010A JP 2001239541 A JP2001239541 A JP 2001239541A JP 2001239541 A JP2001239541 A JP 2001239541A JP 2003055010 A JP2003055010 A JP 2003055010A
Authority
JP
Japan
Prior art keywords
raw material
cement
metal component
gas
volatile metal
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
Application number
JP2001239541A
Other languages
Japanese (ja)
Inventor
Junichi Terasaki
淳一 寺崎
Yasuhiro Uchiyama
康広 内山
Osamu Yamaguchi
修 山口
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.)
Taiheiyo Cement Corp
Original Assignee
Taiheiyo Cement Corp
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 Taiheiyo Cement Corp filed Critical Taiheiyo Cement Corp
Priority to JP2001239541A priority Critical patent/JP2003055010A/en
Publication of JP2003055010A publication Critical patent/JP2003055010A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/36Manufacture of hydraulic cements in general
    • C04B7/364Avoiding environmental pollution during cement-manufacturing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Ecology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Environmental Sciences (AREA)
  • Public Health (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for reducing a volatile metal component such as mercury contained in a raw material used for the manufacture of cement. SOLUTION: This method for manufacturing cement is characterized in that the concentration of the volatile metal component in the raw material is reduced by introducing the raw material used for the manufacture of cement to a heating furnace to gasify the volatile metal component contained in the raw material, introducing this high temperature gas to a cooling section, cooling the gas down to a temperature below the deposition temperature of the volatile metal component and liquefying or solidifying the metal component to separate the metal component from the gas and the resultant raw material is introduced to a cement manufacturing stage to calcine cement clinker.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、セメント製造に使
用する原料中の水銀等の揮発性金属成分を効率よく除去
して、その濃度を低減する原料の前処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a raw material pretreatment method for efficiently removing volatile metal components such as mercury in raw materials used for cement production to reduce the concentration thereof.

【0002】[0002]

【従来の技術】セメント製造において、各種汚泥、焼却
灰などの廃棄物を原料や燃料として使用する機会が増え
ている。しかし、これらの廃棄物に重金属が多少なりと
も含有されており、このためセメント製造工程に持ち込
まれる重金属の量が増大することが懸念される。これら
の廃棄物に含まれる重金属類のうち、揮発性が比較的高
い水銀、亜鉛、セレン等、およびこれらの化合物は、セ
メント製造工程の高温部において揮発し、ガス中に含有
される。その後、ガスの温度が低下するのに伴いガス中
に含有されるダストの表面にこれらの重金属が析出し、
あるいは重金属やその化合物自身の微粒子となる。これ
らのダストや微粒子は煙道の電気集塵機(EP)で捕集
され、排ガスから除去される。なお、特に揮発性が高い
水銀はその一部がガス状のまま残存し、排煙に含有され
たまま排出される。
2. Description of the Related Art In cement production, there are increasing opportunities to use various sludges, incinerator ash and other waste materials as raw materials and fuels. However, these wastes contain some heavy metals, which may increase the amount of heavy metals brought into the cement manufacturing process. Of the heavy metals contained in these wastes, mercury, zinc, selenium, etc., which have relatively high volatility, and these compounds volatilize in the high temperature part of the cement manufacturing process and are contained in the gas. Then, as the temperature of the gas decreases, these heavy metals are deposited on the surface of the dust contained in the gas,
Alternatively, they become fine particles of heavy metals or their compounds themselves. These dusts and particles are collected by the flue gas electrostatic precipitator (EP) and removed from the exhaust gas. Part of mercury, which has a particularly high volatility, remains in a gaseous state and is discharged while being contained in the flue gas.

【0003】[0003]

【発明が解決しようとする課題】この電気集塵機で捕集
されたダスト(集塵ダスト)は、セメント製造工程にお
いて新たに粉砕された原料に混ぜられて原料の一部とな
り、集塵ダストに含まれる揮発性の重金属は、その一部
はクリンカに含有されるものの大部分はプレヒータ部あ
るいはロータリーキルンの高温部で再び揮発し、ガス中
に含有されて再び排ガス系に導かれ、セメント製造工程
を循環している。このためセメント製造工程に使用する
原料の揮発性重金属の持ち込みを低減する手段を設けな
いと、原料から持ち込まれる揮発性重金属量が増大する
のに伴い、セメント工程内の循環量が増加し、系外に排
出される揮発性重金属量が増えるという問題がある。
The dust collected by the electric dust collector (dust collecting dust) is mixed with the newly crushed raw material in the cement manufacturing process and becomes a part of the raw material, which is included in the dust collecting dust. Most of the volatile heavy metals contained in the clinker are volatilized again in the preheater part or the high temperature part of the rotary kiln, but they are contained in the gas and led to the exhaust gas system again to circulate in the cement manufacturing process. is doing. For this reason, unless measures are provided to reduce the carry-on of volatile heavy metals from the raw materials used in the cement manufacturing process, as the amount of volatile heavy metals brought in from the raw materials increases, the amount of circulation in the cement process increases and There is a problem that the amount of volatile heavy metals discharged to the outside increases.

【0004】[0004]

【課題を解決する手段】本発明は、このようなセメント
製造工程に使用する原料の水銀等の揮発性金属を効率よ
く除去し、系外に排出される排ガス中の揮発性重金属量
を低減する方法を提供する。本発明の処理方法は、原料
を加熱することによって揮発性金属をガス化して原料と
分離し、このガスを冷却して揮発成分を分離回収し、セ
メント焼成系内に揮発性金属の流入を防ぐ方法である。
The present invention efficiently removes volatile metals such as mercury, which is a raw material used in such a cement manufacturing process, and reduces the amount of volatile heavy metals in exhaust gas discharged outside the system. Provide a way. In the treatment method of the present invention, by heating the raw material, the volatile metal is gasified and separated from the raw material, and this gas is cooled to separate and recover the volatile components to prevent the volatile metal from flowing into the cement firing system. Is the way.

【0005】すなわち、本発明は以下の構成からなるセ
メント製造における原料の揮発成分の低減法に関する。 (1)セメント製造に使用する原料を加熱炉に導き、原
料に含まれる揮発性金属成分をガス化し、この高温ガス
を冷却部に導いて揮発性金属成分の析出温度以下に冷却
し、これを液化ないし固化してガス中から分離すること
によって、原料中の揮発性金属成分の濃度を低減し、そ
の原料をセメント製造工程に導いてセメントクリンカを
焼成することを特徴とするセメント製造方法。 (2)セメント製造工程において排出された熱排ガスに
よって加熱炉を加熱する上記(1)のセメント製造方
法。
That is, the present invention relates to a method for reducing volatile components of raw materials in cement production having the following constitution. (1) The raw material used for cement production is introduced into a heating furnace, the volatile metal component contained in the raw material is gasified, and this high-temperature gas is introduced into a cooling section to be cooled to a temperature below the precipitation temperature of the volatile metal component. A method for producing cement, which comprises liquefying or solidifying and separating from gas to reduce the concentration of volatile metal components in the raw material, guiding the raw material to the cement production process, and firing the cement clinker. (2) The cement manufacturing method according to (1), wherein the heating furnace is heated by the heat exhaust gas discharged in the cement manufacturing process.

【0006】[0006]

【発明の実施の形態】以下、本発明を実施形態に基づい
て具体的に説明する。本発明の処理方法は、セメント製
造に使用する原料を加熱炉に導き、原料に含まれる揮発
金属成分の揮発温度以上に加熱して上記揮発性金属成分
をガス化し、この高温ガスを冷却部に導いて、揮発性金
属成分の析出温度以下に冷却し、これを液化ないし固化
してガス中から分離し、その原料をセメント製造工程に
導いてセメントクリンカを焼成することを特徴とするセ
メント製造方法である。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below based on embodiments. The treatment method of the present invention introduces a raw material used for cement production to a heating furnace, gasifies the volatile metal component by heating it to a temperature equal to or higher than the volatilization temperature of the volatile metal component contained in the raw material, and cools this high temperature gas to a cooling part. The method for producing cement, characterized by cooling to below the precipitation temperature of the volatile metal component, liquefying or solidifying it and separating it from the gas, and introducing the raw material to the cement production process and firing the cement clinker. Is.

【0007】本発明に係わる処理方法の概略を図1に示
す。図示するように、本発明の処理系等には、セメント
製造工程の原料10を受け入れる加熱炉30,加熱炉3
0から排出された高温ガスを冷却する冷却部31、およ
び冷却部31から排出された冷却ガスを送り出す吸引フ
ァン32が設けられている。
The outline of the processing method according to the present invention is shown in FIG. As shown in the figure, the treatment system of the present invention includes a heating furnace 30, a heating furnace 3 for receiving the raw material 10 of the cement manufacturing process.
A cooling unit 31 for cooling the high-temperature gas discharged from 0 and a suction fan 32 for sending the cooling gas discharged from the cooling unit 31 are provided.

【0008】セメント焼成キルンなどの製造工程では、
原料10は、粉砕機20に導入され、所定の粒度に粉砕
される。本発明の対象となる原料は、セメント製造工程
で使用する原料であれば何れでも良く、特に水銀、セレ
ン、カドミウム、亜鉛などの揮発性金属またはその塩化
物などの揮発性金属化合物(これらを揮発性金属成分と
略称する)が含有している原料を優先的に処理する。こ
れらの原料を加熱炉30に導入する。加熱炉30は、例
えば内部にスクリューフィーダ30aを備えた物が好ま
しい。炉30の一端から送入された原料が炉内を搬送さ
れる間に揮発性金属成分の揮発温度以上に加熱され、揮
発性金属成分がガス化する。具体的には概ね300〜5
00℃に加熱するのが好ましい。因みに1mmHgの蒸
気圧を生じる温度は、水銀が約126℃、セレン、砒
素、カドミウムがそれぞれ約356〜約394℃、亜鉛
が約487℃であり、また塩化物では、塩化アンチモン
(SbCl3)が約49℃、塩化水銀が約136℃、塩
化錫(SbCl2)が約316℃塩化亜鉛(ZnCl2
が約428℃である。従って、300〜500℃の加熱
下において概ねこれらが揮発する。ただし、装置上の制
約が許す限り、これ以上の高温でも揮発性金属のガス化
には問題ない。また、加熱炉での処理時間を長くするこ
とが可能ならば、300℃より低い温度(対象とする金
属が揮発する温度)で処理しても良い。
In the manufacturing process of cement burning kiln, etc.,
The raw material 10 is introduced into the crusher 20 and crushed to a predetermined particle size. The raw material to be the subject of the present invention may be any raw material used in the cement manufacturing process, in particular, volatile metals such as mercury, selenium, cadmium and zinc, or volatile metal compounds such as chlorides thereof (volatilizing these compounds). The raw material contained in the (abbreviated as a metallic component) is preferentially treated. These raw materials are introduced into the heating furnace 30. It is preferable that the heating furnace 30 has, for example, a screw feeder 30a therein. The raw material fed from one end of the furnace 30 is heated above the volatilization temperature of the volatile metal component while being transported in the furnace, and the volatile metal component is gasified. Specifically, about 300 to 5
Heating to 00 ° C is preferred. Incidentally temperature which the vapor pressure of 1mmHg the mercury about 126 ° C., selenium, arsenic, cadmium about 356~ about 394 ° C., respectively, of zinc is about 487 ° C., and in the chloride, antimony chloride (SbCl 3) is About 49 ° C, about 136 ° C for mercury chloride, about 316 ° C for tin chloride (SbCl 2 ), zinc chloride (ZnCl 2 ).
Is about 428 ° C. Therefore, these are mostly volatilized under heating at 300 to 500 ° C. However, as long as the restrictions on the equipment permit, there is no problem in gasification of volatile metals even at higher temperatures. In addition, if the treatment time in the heating furnace can be extended, the treatment may be performed at a temperature lower than 300 ° C. (a temperature at which the target metal is volatilized).

【0009】この加熱源はセメント焼成キルン等のセメ
ント製造工程から排出された熱排ガスなどを利用すると
良い。揮発性金属成分がガス化した後の原料は、加熱炉
30の排出口から取り出される。
As the heat source, heat exhaust gas discharged from the cement manufacturing process such as a cement burning kiln may be used. The raw material after the volatile metal component is gasified is taken out from the outlet of the heating furnace 30.

【0010】加熱炉から排出された高温ガスは冷却部3
1に導入される。冷却部31は、例えば、外周に冷却ジ
ャケット31aを有し、下部に傾斜板31bを設けた構
造のものなどが用いられる。冷却部31は冷却ジャケッ
ト31aによって揮発性金属成分の析出温度以下に冷却
される。具体的には例えば50℃以下に冷却される。こ
の冷却によってガス中の揮発性金属成分、例えば、水銀
は液化して傾斜板表面に析出し、またセレン、カドミウ
ムなどは固化し、微粒子となって冷却部31の底部に堆
積する。なお、冷却部31の温度は50℃より高くても
ガス中から水銀を除去することはできるが、温度が高い
とガス中に残存する水銀量が多くなり、効率的に水銀を
ガス中から除去できないので、冷却温度は50℃以下が
適当であり、低ければ低い方が良い。また、吸引ファン
32のガス流量が大きすぎると、ガス中の揮発性金属の
濃度と冷却部での揮発性金属の飽和濃度との差が小さく
なり、効率的に除去できなくなるので、原料中の揮発性
金属の含有量によってガス流量を調整するのがよい。
The high temperature gas discharged from the heating furnace is cooled by the cooling unit 3.
Introduced in 1. As the cooling unit 31, for example, one having a structure in which a cooling jacket 31a is provided on the outer periphery and an inclined plate 31b is provided on the lower portion, or the like is used. The cooling unit 31 is cooled to a temperature not higher than the deposition temperature of the volatile metal component by the cooling jacket 31a. Specifically, it is cooled to, for example, 50 ° C. or lower. By this cooling, a volatile metal component in the gas, for example, mercury is liquefied and deposited on the surface of the inclined plate, and selenium, cadmium and the like are solidified and deposited as fine particles on the bottom of the cooling unit 31. Even if the temperature of the cooling unit 31 is higher than 50 ° C., mercury can be removed from the gas, but when the temperature is high, the amount of mercury remaining in the gas is large, and mercury is efficiently removed from the gas. Since it is not possible, it is appropriate that the cooling temperature be 50 ° C. or lower, and the lower the better, the better. Further, if the gas flow rate of the suction fan 32 is too large, the difference between the concentration of the volatile metal in the gas and the saturation concentration of the volatile metal in the cooling section becomes small, and it becomes impossible to efficiently remove it. The gas flow rate may be adjusted depending on the content of the volatile metal.

【0011】冷却部の底に溜まった水銀等は定期的に取
り出す。一方、冷却部から排出されたガスは吸引ファン
32を通じて系外に導く。この冷却ガスの揮発性金属成
分の濃度は大幅に低減されており、例えば、水銀は30
mg/m3N以下、亜鉛は0.050mg/m3N以下、
カドミウムは0.001mg/m3N以下である。この
冷却ガスは加熱器への導入空気として戻し、循環させる
のが好ましい。このように、排ガスを加熱炉30から冷
却部31を経て加熱器導入空気に循環させることによっ
て、排ガス中に含まれる水銀などの揮発性金属成分を外
部に直接排出しないようにする。
Mercury and the like accumulated on the bottom of the cooling unit are periodically taken out. On the other hand, the gas discharged from the cooling unit is guided to the outside of the system through the suction fan 32. The concentration of volatile metal components in this cooling gas is greatly reduced, and for example, mercury is 30%.
mg / m 3 N or less, zinc is 0.050mg / m 3 N or less,
Cadmium is 0.001 mg / m 3 N or less. This cooling gas is preferably returned as air introduced into the heater and circulated. In this way, the exhaust gas is circulated from the heating furnace 30 to the air introduced into the heater through the cooling unit 31, so that volatile metal components such as mercury contained in the exhaust gas are not directly discharged to the outside.

【0012】上記の加熱処理を終えたセメント原料は、
粉砕機20に導かれ、以後はセメント焼成プロセスに供
せられる。上記の加熱処理により、セメント原料中に含
まれる水銀等の揮発性成分は低減されており、その結
果、セメント製造工程を循環する揮発性成分も低減さ
れ、排ガス中に含まれる揮発性成分も低減される。
The cement raw material that has been subjected to the above heat treatment is
It is guided to the crusher 20 and thereafter subjected to the cement firing process. By the above heat treatment, the volatile components such as mercury contained in the cement raw material are reduced, and as a result, the volatile components circulating in the cement manufacturing process are also reduced, and the volatile components contained in the exhaust gas are also reduced. To be done.

【0013】[0013]

【実施例1】セメント製造工場において原料に用いられ
ている火力発電書由来の石炭灰10kgを両端が開口し
た管(80mmφ×1000mm)の中央部に充填し、
200〜500℃で30分加熱した。このとき試験管の
片側開口部から空気を100ml/分導入し、他端から
排出したガスを冷却管に導いて室温まで冷却した。原料
に含まれる水銀含有量と処理効果を表1に示した。
Example 1 10 kg of coal ash derived from a thermal power generation certificate used as a raw material in a cement manufacturing plant was filled in the center of a pipe (80 mmφ × 1000 mm) having open ends,
It heated at 200-500 degreeC for 30 minutes. At this time, 100 ml / min of air was introduced from one side opening of the test tube, and the gas discharged from the other end was introduced into a cooling tube and cooled to room temperature. Table 1 shows the content of mercury contained in the raw materials and the treatment effect.

【0014】[0014]

【表1】 [Table 1]

【0015】[0015]

【実施例2】図1に示す処理システムを用い、セメント
製造工程の原料一部を加熱炉に供給し、所定温度に加熱
し、その加熱ガスを冷却部に導入して冷却ガス中の水銀
を分離した。冷却したガスは吸引ファンを通じて再び加
熱器に戻した。この処理結果を表2に示した。
[Embodiment 2] Using the treatment system shown in FIG. 1, a part of the raw material of the cement manufacturing process is supplied to a heating furnace and heated to a predetermined temperature, and the heating gas is introduced into a cooling section to remove mercury in the cooling gas. separated. The cooled gas was returned to the heater again through a suction fan. The results of this treatment are shown in Table 2.

【0016】[0016]

【表2】 [Table 2]

【0017】この実施例2の結果を、10t/hrの規
模の処理システムに拡大した場合、同等の性能を示すと
すると、排ガス中の水銀濃度を0.05mg/m3N程
度低減することが可能であると推定できる。
When the result of Example 2 is expanded to a treatment system of 10 t / hr, if the same performance is shown, the mercury concentration in the exhaust gas can be reduced by about 0.05 mg / m 3 N. It can be estimated that it is possible.

【0018】[0018]

【発明の効果】セメント製造工程から排出された水銀等
の揮発性金属成分は大部分が廃棄物原料から持ち込まれ
るので、本発明の処理方法によれば、この原料を処理す
ることによってセメント製造工程に持ち込まれる水銀等
の揮発性成分を効率よく除去することができる。その結
果、セメント製造プロセスを循環する揮発性成分が低減
され、系外に排出される揮発性成分を低減することがで
きる。また、本発明の方法はおもに揮発性金属成分を含
む原料を処理するので、大掛かりな設備を必要とせず、
既存の原料投入工程に付設するだけで容易に実施するこ
とができる。
Most of the volatile metal components such as mercury discharged from the cement manufacturing process are brought in from the waste raw material. Therefore, according to the treatment method of the present invention, the cement manufacturing process is performed by treating this raw material. It is possible to efficiently remove volatile components such as mercury that are brought into the room. As a result, the volatile components circulating in the cement manufacturing process are reduced, and the volatile components discharged to the outside of the system can be reduced. Further, since the method of the present invention mainly treats the raw material containing the volatile metal component, it does not require large-scale equipment,
It can be easily implemented by simply attaching it to the existing raw material charging process.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の処理工程を示すフロー図FIG. 1 is a flow chart showing the processing steps of the present invention.

【符号の説明】[Explanation of symbols]

10−原料、20−粉砕機、30−加熱炉、31−冷却
部、32−冷却ファン
10-raw material, 20-crusher, 30-heating furnace, 31-cooling unit, 32-cooling fan

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D076 AA05 AA16 BD07 DA10 DA28 FA04 FA11 HA05 JA01 JA04   ─────────────────────────────────────────────────── ─── Continued front page    F term (reference) 4D076 AA05 AA16 BD07 DA10 DA28                       FA04 FA11 HA05 JA01 JA04

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 セメント製造に使用する原料を加熱炉に
導き、原料に含まれる揮発性金属成分をガス化し、この
高温ガスを冷却部に導いて揮発性金属成分の析出温度以
下に冷却し、これを液化ないし固化してガス中から分離
することによって、原料中の揮発性金属成分の濃度を低
減し、その原料をセメント製造工程に導いてセメントク
リンカを焼成することを特徴とするセメント製造方法。
1. A raw material used for cement production is introduced into a heating furnace, the volatile metal component contained in the raw material is gasified, and this high temperature gas is introduced into a cooling section to be cooled to a temperature below the precipitation temperature of the volatile metal component, By liquefying or solidifying this and separating it from the gas, the concentration of the volatile metal component in the raw material is reduced, and the raw material is introduced into the cement manufacturing process to burn the cement clinker, and the cement manufacturing method is characterized. .
【請求項2】 セメント製造工程において排出された熱
排ガスによって加熱炉を加熱する請求項1のセメント製
造方法。
2. The cement manufacturing method according to claim 1, wherein the heating furnace is heated by the hot exhaust gas discharged in the cement manufacturing process.
JP2001239541A 2001-08-07 2001-08-07 Pretreating method for raw material in manufacture of cement Pending JP2003055010A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001239541A JP2003055010A (en) 2001-08-07 2001-08-07 Pretreating method for raw material in manufacture of cement

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001239541A JP2003055010A (en) 2001-08-07 2001-08-07 Pretreating method for raw material in manufacture of cement

Publications (1)

Publication Number Publication Date
JP2003055010A true JP2003055010A (en) 2003-02-26

Family

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Family Applications (1)

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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008050678A1 (en) 2006-10-24 2008-05-02 Taiheiyo Cement Corporation Method for removing lead from cement kiln
JP2011132091A (en) * 2009-12-25 2011-07-07 Cosmo Oil Co Ltd Apparatus and method for separating-to-recover
JP2014172000A (en) * 2013-03-11 2014-09-22 Nihon Yamamura Glass Co Ltd System and method for recovering selenium in exhaust gas

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008050678A1 (en) 2006-10-24 2008-05-02 Taiheiyo Cement Corporation Method for removing lead from cement kiln
US7837963B2 (en) * 2006-10-24 2010-11-23 Taiheiyo Cement Corporation Method for removing lead from cement burning furnace
JP5213119B2 (en) * 2006-10-24 2013-06-19 太平洋セメント株式会社 Method for removing lead from cement firing furnace
KR101410301B1 (en) * 2006-10-24 2014-06-20 다이헤이요 세멘토 가부시키가이샤 Method for removing lead from cement kiln
TWI460279B (en) * 2006-10-24 2014-11-11 Taiheiyo Cement Corp Method of removing lead from cement kiln
JP2011132091A (en) * 2009-12-25 2011-07-07 Cosmo Oil Co Ltd Apparatus and method for separating-to-recover
JP2014172000A (en) * 2013-03-11 2014-09-22 Nihon Yamamura Glass Co Ltd System and method for recovering selenium in exhaust gas

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