JP3864443B2 - Method for producing high-fluidity calcium hydroxide - Google Patents
Method for producing high-fluidity calcium hydroxide Download PDFInfo
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- JP3864443B2 JP3864443B2 JP32927895A JP32927895A JP3864443B2 JP 3864443 B2 JP3864443 B2 JP 3864443B2 JP 32927895 A JP32927895 A JP 32927895A JP 32927895 A JP32927895 A JP 32927895A JP 3864443 B2 JP3864443 B2 JP 3864443B2
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- Prior art keywords
- calcium hydroxide
- fluidity
- water
- producing high
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- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 title claims description 26
- 239000000920 calcium hydroxide Substances 0.000 title claims description 26
- 229910001861 calcium hydroxide Inorganic materials 0.000 title claims description 26
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 10
- 239000000292 calcium oxide Substances 0.000 claims description 8
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims description 6
- 229920000151 polyglycol Polymers 0.000 claims description 5
- 239000010695 polyglycol Substances 0.000 claims description 5
- 239000004094 surface-active agent Substances 0.000 claims description 5
- 125000004432 carbon atom Chemical group C* 0.000 claims description 3
- 229920002545 silicone oil Polymers 0.000 claims description 3
- 150000005846 sugar alcohols Polymers 0.000 claims description 3
- 239000012530 fluid Substances 0.000 claims 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 23
- 239000000843 powder Substances 0.000 description 12
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 9
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 8
- 235000012255 calcium oxide Nutrition 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 5
- 230000029087 digestion Effects 0.000 description 5
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 5
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 235000011187 glycerol Nutrition 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 230000032683 aging Effects 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 230000009257 reactivity Effects 0.000 description 3
- PUPZLCDOIYMWBV-UHFFFAOYSA-N (+/-)-1,3-Butanediol Chemical compound CC(O)CCO PUPZLCDOIYMWBV-UHFFFAOYSA-N 0.000 description 2
- SVTBMSDMJJWYQN-UHFFFAOYSA-N 2-methylpentane-2,4-diol Chemical compound CC(O)CC(C)(C)O SVTBMSDMJJWYQN-UHFFFAOYSA-N 0.000 description 2
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 150000003961 organosilicon compounds Chemical class 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 235000013870 dimethyl polysiloxane Nutrition 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 229940051250 hexylene glycol Drugs 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- -1 that is Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、微粉であっても流動性が高く、従って取扱いやすい水酸化カルシウムを製造する方法に関する。
【0002】
【従来の技術】
水酸化カルシウムの工業的な製造は、よく知られているように、石灰石を仮焼して得た生石灰すなわち酸化カルシウムに、水を加えて消化させることにより行なわれている。 微粉末が要求されるときは、水酸化カルシウムを分級し、必要によっては粉砕した上で分級し、この要求にこたえている。
【0003】
ところが、このようにして提供される微粉の水酸化カルシウムは、一般に付着性や凝集性が強く、粉末の流動性が低いためにホッパーから落下しにくい等の問題があって、取扱いにくい。 水酸化カルシウムのような金属水酸化物を微粉末にしたときに流動性が悪くなることの要因としては、分子の極性が大きいため大気中の水分による影響を受けやすいことや、粒子間に静電気等による相互作用が働くことなどが考えられる。
【0004】
水酸化カルシウムの諸用途のうち、近年とくに拡大しつつある、ゴミ焼却炉などから出るHClやSOxを含む廃ガスを処理する分野では、とくに粉末が微粉であり、従って反応性に富むことが要求される。 一方で、粉末の流動性が高く取扱いやすいことは、この分野に限らず望ましい。
【0005】
比較的微粉末でありながら流動性の高い水酸化カルシウムを得る方策として、酸化カルシウムの消化に当って水和反応を抑制することが考えられ、その手段としてアルコールを含む消化水を使用することが試みられている。 たとえば、50〜70容量%のエタノールを含む水との混合液を使用し、高比表面積で噴流性にすぐれた水酸化カルシウムを製造する方法(特公平6−8194)や、アルコールに加えて界面活性剤を含む消化水を用い、流動性にすぐれた水酸化カルシウムを得る方法(特開平5−193997)などである。
【0006】
しかしこれらの方法は、アルコールを多量に使用するため、それを回収して再利用する必要があり、そのための工程が加わって複雑になる上、消費エネルギーが多いという欠点がある。 また、これらのアルコールは揮発性が高く燃えやすいことから、呼気障害や燃焼、爆発への対策も必要となる。
【0007】
【発明が解決しようとする課題】
本発明の目的は、工程を複雑にしたり消費エネルギーを増大させたりすることなく、高流動性の水酸化カルシウム、とくに分級して微粉としたときにも流動性を維持できるような水酸化カルシウムを製造する方法を提供することにある。
【0008】
【課題を解決するための手段および作用】
本発明の高流動性水酸化カルシウムを製造する方法は、酸化カルシウムに水を加えて消化することにより水酸化カルシウムを製造する方法において、消化水として、下記
(a)炭素数3〜8の水溶性多価アルコール
(b)ポリグリコール系界面活性剤
(c)アミノ変性ジメチルシリコンオイル
の(a)+(b)、(b)または(c)を0.05〜5%を含有する水を使用することを特徴とする。
【0010】
従来使用が試みられているエタノールのような水和反応抑制剤は、水よりも沸点が低いこと、および多量に使用しなければ効果がないことから、どうしてもその回収が必要であった。 少量で分子極性を抑制できるような物質であって、沸点が水よりも高く、従って製品水酸化カルシウムの表面に付着し、臭いや毒性等による支障のないものを使用すれば、エタノールのような低沸点のアルコールを使用した場合のように複雑な工程を経る必要なく、高流動性水酸化カルシウムを得ることができる、との着想の下に発明者らが研究を進め、有用であることを確認したのが、上記の消化水への添加剤である。
【0011】
これらの添加剤は、いずれも入手容易で経済的に使用でき、かつ装置に対する腐食性などの問題がないから、従来慣用の消化機や熟成機などの設備を、そのまま使用して本発明を実施することができる。
【0012】
炭素数3〜8の多価アルコールは、具体的には、グリセリン、プロピレングリコール、1,3−ブタンジオール、ヘキシレングリコールなどであり、とくにグリセリンおよびプロピレングリコールが、入手が容易でしかも低価格であるから有用である。 これらは、その効果および経済性からみて、消化水に2〜4%程度添加して使用するのが適切である。
【0013】
ポリグリコール系界面活性剤は、より少量の0.05〜1%程度の濃度で使用するのが適切である。
【0014】
有機珪素化合物は、分散剤や撥水剤として、種々の用途に使用されている。 有機珪素化合物を無機粉体に少量添加することにより粉末の流動性が向上することは知られているが、水酸化カルシウムに適用した場合、その粒子の化学的特性に大きな影響を及ぼすと考えられていた。 そのこともあって、酸化カルシウムの消化水に、または製品水酸化カルシウムに添加使用することは試みられなかったが、発明者らにより、アミノ変性ジメチルシリコンオイルが流動性を改善する上で有用なことがわかった。 これは、0.5〜2%の水溶液ないしエマルジョンとして使用するのが適当である。
【0015】
【実施例】
常用の消化機および熟成機を使用し、生石灰各100重量部に対し下記の消化水をいずれも60重量部使用して、水酸化カルシウムを製造した。No.1および2は参考例であり、No.3〜5が実施例である。
【0016】
No.1 4%グリセリン水溶液
No.2 2%プロピレングリコール水溶液
No.3 0.05%ポリグリコール誘導体界面活性剤水溶液
No.4 0.5%アミノ変性ジメチルポリシロキサンのエマルジョン
No.5 2%グリセリンと0.05%ポリグリコール誘導体界面活性剤併用。
【0017】
比較のため、JIS特号消石灰と、これを気流分級機により分級して微粉を集めたものとをサンプルに加えた。 前者をA、後者をBとする。 サンプルNo.1〜6、ならびにAおよびBの平均粒径を測定するとともに、流動性のめやすとしてホッパー試験および振動落下試験を行ない、また反応性の尺度として塩化水素ガス除去率を測定した。 それぞれの試験法は、つぎのとおりである。
【0018】
(ホッパー試験)
少なくとも1日密封静置したサンプル1kgを、特定の形状・寸法のホッパーモデルに入れ、下部のバルブを開くとともにバイブレータによりホッパー全体に振動を与え、サンプル全量が落下するまでの時間を測定する。 30秒間経過しても全量が落下しないときは、振動を止めてホッパーに残留した量を測定する。
【0019】
(振動落下試験)
サンプル100gを、円筒を通して目開き1mmのフルイ上にのせる。 このフルイをのせた台を一定の時間間隔で5回上下に振動させ、フルイを通過した量を測定する。
【0020】
(塩化水素ガス除去率)
内径8.5mmの管内にサンプル約50mgを充填し、そこへHClを0.4容量%と水蒸気を50容量%含む混合ガスを、200℃で、ガス流速4.4m/minとなる条件下に20分間流通させて、HClの除去率を測定する。
【0021】
各サンプルについて上記試験を行なって得た結果は、つぎの表に示すとおりである:
表
サンプル 平均粒径 ホッパー 振動落下 HC1除去率
No. ( μ m) ( 秒 ) ( % ) ( % )
参考例および実施例
1 2.9 3.9 75.2 94.4
2 3.5 6.0 63.9 89.0
3 3.5 3.7 49.5 92.4
4 3.4 8.1 55.6 94.0
5 3.3 2.5 77.2 92.8
比較例
A 6.0 4.8 45.6 79.0
B 3.3 370g残留 29.0 88.0
本発明の方法により製造した水酸化カルシウム( No. 3〜5)は、JIS特号消石灰から分級して得た微粉と同等またはそれ以上の反応性を有し、一方で遥かに高い流動性を示すことが、上のデータから明らかである。とくに添加剤(a)+(b)を併用した No. 5は、最良の流動性を示した。
【0022】
【発明の効果】
本発明の方法により、工程を複雑にしたりエネルギー消費を増したりすることなく、常用の消化機と熟成機からなる設備を使用して酸化カルシウムの消化を行ない、微粉であっても流動性の高い、従って反応性も高い水酸化カルシウムを製造することができる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing calcium hydroxide which is fine and has high fluidity and is therefore easy to handle.
[0002]
[Prior art]
As is well known, calcium hydroxide is industrially produced by adding water to digestion of quick lime obtained by calcining limestone, that is, calcium oxide. When a fine powder is required, calcium hydroxide is classified and, if necessary, ground and classified to meet this requirement.
[0003]
However, the finely powdered calcium hydroxide provided in this way is generally difficult to handle due to problems such as strong adhesion and cohesion and difficulty in dropping from the hopper due to low powder fluidity. Factors that cause poor fluidity when a metal hydroxide such as calcium hydroxide is made into a fine powder are that it is easily affected by moisture in the atmosphere due to its large molecular polarity, and static electricity between particles. It is conceivable that an interaction due to the above works.
[0004]
Among the various uses of calcium hydroxide, especially in the field of treating waste gas containing HCl and SOx from garbage incinerators, which are expanding in recent years, it is required that the powder is fine and therefore highly reactive. Is done. On the other hand, it is desirable that the powder has high fluidity and is easy to handle, not limited to this field.
[0005]
As a measure to obtain calcium hydroxide with high fluidity while being relatively fine powder, it is conceivable to suppress the hydration reaction in the digestion of calcium oxide, and the use of digested water containing alcohol as its means Has been tried. For example, a method of producing calcium hydroxide having a high specific surface area and excellent jet properties using a mixed solution with water containing 50 to 70% by volume of ethanol (Japanese Patent Publication No. 6-8194), an interface in addition to alcohol For example, a method of obtaining calcium hydroxide having excellent fluidity using digested water containing an activator (Japanese Patent Laid-Open No. 5-193997).
[0006]
However, since these methods use a large amount of alcohol, it is necessary to recover and reuse the alcohol, which is complicated by the addition of a process for that purpose, and has the disadvantages of high energy consumption. In addition, since these alcohols are highly volatile and flammable, it is necessary to take measures against breath problems, combustion, and explosion.
[0007]
[Problems to be solved by the invention]
It is an object of the present invention to provide a high fluidity calcium hydroxide, in particular, a calcium hydroxide that can maintain fluidity even when classified into fine powders without complicating the process or increasing energy consumption. It is to provide a method of manufacturing.
[0008]
[Means and Actions for Solving the Problems]
The method for producing high-fluidity calcium hydroxide of the present invention is a method for producing calcium hydroxide by adding water to calcium oxide for digestion, and the following (a) water solution having 3 to 8 carbon atoms as digestion water: Polyhydric alcohol (b) polyglycol surfactant (c) amino-modified dimethyl silicone oil
(A) + (b), (b) or (c) is characterized by using water containing 0.05 to 5%.
[0010]
A hydration inhibitor such as ethanol, which has been attempted to be used conventionally, has a boiling point lower than that of water, and has no effect unless used in a large amount. If you use a substance that can suppress the molecular polarity in a small amount and has a boiling point higher than that of water, and therefore adheres to the surface of the product calcium hydroxide and does not interfere with odor or toxicity, Based on the idea that high-fluidity calcium hydroxide can be obtained without having to go through a complicated process as in the case of using a low-boiling alcohol, the inventors have advanced research and are useful. What has been confirmed is the above-mentioned additive to digestion water.
[0011]
All of these additives are readily available and can be used economically, and there are no problems such as corrosiveness to the apparatus. Therefore, the present invention is carried out by using equipment such as conventional digesters and aging machines as they are. can do.
[0012]
Specific examples of the polyhydric alcohol having 3 to 8 carbon atoms include glycerin, propylene glycol, 1,3-butanediol, hexylene glycol and the like. In particular, glycerin and propylene glycol are easily available and inexpensive. It is useful because there is. From the viewpoint of the effect and economy, it is appropriate to add about 2 to 4% to digested water.
[0013]
It is appropriate to use the polyglycol-based surfactant in a smaller amount of about 0.05 to 1%.
[0014]
Organosilicon compounds are used in various applications as dispersants and water repellents. It is known that adding a small amount of an organosilicon compound to an inorganic powder improves the fluidity of the powder, but when applied to calcium hydroxide, it is thought to have a significant effect on the chemical properties of the particles. It was. For this reason, attempts have not been made to add it to the digested water of calcium oxide or the product calcium hydroxide, but the inventors have found that amino-modified dimethyl silicone oil is useful for improving fluidity. I understood it. This is suitably used as a 0.5-2% aqueous solution or emulsion.
[0015]
【Example】
Using a conventional digester and aging machine, calcium hydroxide was produced using 60 parts by weight of the following digested water for 100 parts by weight of quicklime. No. Nos. 1 and 2 are reference examples. 3 to 5 are examples.
[0016]
No. 14 4% glycerin aqueous solution
No. 2 2% aqueous propylene glycol solution
No. 3 0.05% polyglycol derivative surfactant aqueous solution
No. 4 0.5% amino-modified dimethylpolysiloxane emulsion
No. 5 Combined use of 2% glycerin and 0.05% polyglycol derivative surfactant.
[0017]
For comparison, a JIS special slaked lime and a powder obtained by classifying the JIS slaked lime with an air classifier were added to the sample. The former is A and the latter is B. Sample No. In addition to measuring the average particle diameters of 1 to 6 and A and B, a hopper test and a vibration drop test were performed as a measure of fluidity, and a hydrogen chloride gas removal rate was measured as a measure of reactivity. Each test method is as follows.
[0018]
(Hopper test)
A 1 kg sample that has been kept sealed for at least one day is placed in a hopper model of a specific shape and size, the lower valve is opened, the vibrator is vibrated by the vibrator, and the time until the entire sample falls is measured. If the total amount does not fall after 30 seconds, stop the vibration and measure the amount remaining in the hopper.
[0019]
(Vibration drop test)
A sample (100 g) is placed on a sieve having an opening of 1 mm through a cylinder. The platform on which the sieve is placed is vibrated up and down five times at regular time intervals, and the amount of passage through the sieve is measured.
[0020]
(Hydrogen chloride gas removal rate)
A tube with an inner diameter of 8.5 mm is filled with about 50 mg of sample, and a mixed gas containing 0.4% by volume of HCl and 50% by volume of water vapor is placed at 200 ° C. under a gas flow rate of 4.4 m / min. Circulate for 20 minutes and measure the removal rate of HCl.
[0021]
The results obtained by performing the above test on each sample are as shown in the following table:
Table sample Average particle size Hopper Vibration drop HC1 removal rate
No. ( μm ) ( Seconds ) ( % ) ( % )
Reference Examples and Examples 1 2.9 3.9 75.2 94.4
2 3.5 6.0 63.9 89.0
3 3.5 3.7 49.5 92.4
4 3.4 8.1 55.6 94.0
5 3.3 2.5 77.2 92.8
Comparative Example A 6.0 4.8 45.6 79.0
B 3.3 370 g residual 29.0 88.0
Calcium hydroxide ( No. 3-5) produced by the method of the present invention has a reactivity equivalent to or higher than fine powder obtained by classification from JIS special slaked lime, while having a much higher fluidity. This is evident from the data above. In particular, No. 5 in which the additives (a) + (b) were used in combination showed the best fluidity.
[0022]
【The invention's effect】
With the method of the present invention, the calcium oxide is digested using equipment consisting of a conventional digester and an aging machine without complicating the process or increasing energy consumption, and even if it is a fine powder, it has high fluidity Therefore, calcium hydroxide having high reactivity can be produced.
Claims (1)
(a)炭素数3〜8の水溶性多価アルコール
(b)ポリグリコール系界面活性剤
(c)アミノ変性ジメチルシリコンオイル
の(a)+(b)、(b)または(c)を0.05〜5%を含有する水を使用することを特徴とする、高流動性水酸化カルシウムの製造方法。In the method for producing calcium hydroxide by adding water to calcium oxide and digesting, the following (a) water-soluble polyhydric alcohol having 3 to 8 carbon atoms (b) polyglycol surfactant (c) ) Amino modified dimethyl silicone oil
(A) + (b), (b) or water containing 0.05 to 5% of (c) is used, A method for producing highly fluid calcium hydroxide,
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32927895A JP3864443B2 (en) | 1995-12-18 | 1995-12-18 | Method for producing high-fluidity calcium hydroxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32927895A JP3864443B2 (en) | 1995-12-18 | 1995-12-18 | Method for producing high-fluidity calcium hydroxide |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09165216A JPH09165216A (en) | 1997-06-24 |
| JP3864443B2 true JP3864443B2 (en) | 2006-12-27 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32927895A Expired - Fee Related JP3864443B2 (en) | 1995-12-18 | 1995-12-18 | Method for producing high-fluidity calcium hydroxide |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3864443B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6686623B2 (en) | 1997-11-18 | 2004-02-03 | Semiconductor Energy Laboratory Co., Ltd. | Nonvolatile memory and electronic apparatus |
| KR20020004916A (en) * | 2001-11-26 | 2002-01-16 | 김상봉 | Manufacturing method of slaked lime |
| BE1015841A3 (en) | 2003-12-24 | 2005-10-04 | Lhoist Rech & Dev Sa | POWDER COMPOSITION BASED COMPOUND CALCO-magnesium. |
| DE102008014893A1 (en) * | 2008-03-19 | 2009-09-24 | Fels-Werke Gmbh | Flue gas cleaning process and hydrated lime for flue gas cleaning processes |
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1995
- 1995-12-18 JP JP32927895A patent/JP3864443B2/en not_active Expired - Fee Related
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| Publication number | Publication date |
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| JPH09165216A (en) | 1997-06-24 |
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