JPH10265218A - Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity - Google Patents

Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity

Info

Publication number
JPH10265218A
JPH10265218A JP6865897A JP6865897A JPH10265218A JP H10265218 A JPH10265218 A JP H10265218A JP 6865897 A JP6865897 A JP 6865897A JP 6865897 A JP6865897 A JP 6865897A JP H10265218 A JPH10265218 A JP H10265218A
Authority
JP
Japan
Prior art keywords
carbon
ore
fine powder
limestone
impurities
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
JP6865897A
Other languages
Japanese (ja)
Inventor
Masaharu Katayama
正治 片山
Saburo Yashima
三郎 八嶋
Fumiyoshi Saito
文良 齋藤
Toyohisa Fujita
豊久 藤田
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.)
Fuaimatetsuku Kk
Original Assignee
Fuaimatetsuku Kk
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 Fuaimatetsuku Kk filed Critical Fuaimatetsuku Kk
Priority to JP6865897A priority Critical patent/JPH10265218A/en
Publication of JPH10265218A publication Critical patent/JPH10265218A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To efficiently remove carbonaceous particles of impurities and to obtain high purity powdery limestone stock having high whiteness by subjecting raw limestone ore pulverized to a specified particle size to flotation with a alcoholic frother and alkaline pulp and separating floated ore as impurities. SOLUTION: Raw limestone ore is pulverized to fine powder of <=100 mesh and sodium silicate as a dispersant, sodium carbonate, sodium hydrogencarbonate, >=3C alcohol as an active agent, kerosene as a capturing agent, an alcoholic frother and water are added to the fine powder to prepare an aq. dispersion. Air is introduced into the dispersion by stirring, flotation is carried out with alkaline pulp kept at >=60 deg.C and floated ore is separated as impurities. Precipitated ore is rapidly heated at 600-900 deg.C and the residual carbon-contg. org. matter is thermally decomposed, volatilized and removed. Impurities are removed from the gray raw ore and the whiteness and purity of the ore are increased.

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、炭素系不純物の浮
遊除去による石灰石微粉の高純度化方法、さらに詳しく
は、建築用材料、セメント原料、製鉄原料、砕石、公害
防止用材料、その他の工業用原料等に用いられているは
ん用石灰石の高純度化方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying limestone fine powder by floating removal of carbon-based impurities, and more particularly, to building materials, cement raw materials, iron-making raw materials, crushed stones, pollution control materials, and other industrial materials. The present invention relates to a method for purifying general-purpose limestone used as a raw material for use.

【0002】[0002]

【従来の技術】上述したはん用石灰石は、白色度を問題
とされることはなく、破砕、粉砕した石灰石がそのまま
の状態で用いられている。石灰石は種々の不純物を含ん
でおり、そのために灰色あるいは薄墨色等の色彩を呈す
るが、その色彩あるいは模様を美術工芸品あるいは建築
物の壁面用として珍重する場合を除いて、そのまま塊・
粒・粉として用いられている現状である。一方、製紙塗
工用の石灰石、フィラー、食品、薬品に用いられる石灰
石粉には白色度が高く高純度であることが要求される。
そのために従来は白色度が高く、高純度の原料鉱石を選
んで粉砕する方法が採られて来た。すなわち白色度、純
度の高いカルサイト、アラゴナイトの鉱床を選択的に採
掘して原料として用いる方法である。
2. Description of the Related Art The general-purpose limestone described above does not have a problem with whiteness, and crushed and pulverized limestone is used as it is. Limestone contains various impurities, and therefore presents a color such as gray or light black, but the color or pattern is directly used as a lump or solid except for the case where the color or pattern is prized for use as a wall for arts and crafts or buildings.
It is currently used as granules and powder. On the other hand, limestone powder used for limestone, filler, food, and medicine for papermaking application is required to have high whiteness and high purity.
For this reason, a method of selecting and grinding raw ore having high whiteness and high purity has conventionally been adopted. That is, this is a method of selectively mining ore deposits of calcite and aragonite having high whiteness and purity and using them as raw materials.

【0003】[0003]

【発明が解決しようとする課題】しかし自然界における
このような高品質原料鉱石は量的に限界があり、最近は
埋蔵鉱量も少なくなっており、ある程度灰色あるいは薄
墨色を呈する原料鉱石から不純物を除き、白色度、純度
を高めて使用する技術を開発する必要に迫られている。
このようにはん用石灰石が灰色あるいは薄墨色を呈する
のは、不純物としておもに炭素質粒子を含んでいること
によるもので、1μm 〜10μm 程度の粒子径の炭素が
含まれており、これが白色度、純度を低下させている。
この炭素質粒子にも無機質のものと有機質のものがある
However, such high-quality raw ores in the natural world are limited in quantity, and reserves are recently reduced, and impurities are removed from raw ores having a gray or black ink color to some extent. Except for this, it is necessary to develop a technique for increasing the whiteness and purity.
The reason that the general-purpose limestone exhibits a gray or light-black color is that it mainly contains carbonaceous particles as impurities, and contains carbon having a particle diameter of about 1 μm to 10 μm, which is a whiteness. , Lowering the purity.
There are also inorganic and organic carbonaceous particles

【0004】[0004]

【発明の目的】本発明は、従来のはん用石灰石の上述し
た問題点に鑑みなされたものであって、不純物の炭素質
粒子を効率良く除去し、高白色度を有する高純度の石灰
石原料粉を得ることができる方法を提供することを目的
とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems of the conventional general-purpose limestone, and it is an object of the present invention to efficiently remove carbonaceous particles as impurities and obtain a high-purity limestone raw material having high whiteness. It is an object to provide a method by which a powder can be obtained.

【0005】[0005]

【発明の実施の形態】本願の第1発明は、石灰石原料鉱
石を100メッシ以下の微粒状に粉砕し、アルコール系
の起泡剤を用いてアルカリ性パルプで浮選し、不純物を
浮鉱として分離することを特徴とする炭素系不純物の除
去による石灰石微粉の高純度化方法である。第2発明
は、石灰石原料鉱石を100メッシ以下の微粒状に粉砕
し、アルコール系の起泡剤を用いてアルカリ性パルプで
浮選し、不純物を浮鉱として分離し、沈鉱物を、乾燥の
うえ空気中で600℃以上900℃以下の温度で急速加
熱し、残余の含炭素有機物を熱分解して揮発除去するす
ることを特徴とする炭素系不純物の除去による石灰石微
粉の高純度化方法である。
BEST MODE FOR CARRYING OUT THE INVENTION The first invention of the present application is to grind limestone raw material ore into fine particles of 100 mesh or less, flotate with alkaline pulp using an alcohol-based foaming agent, and separate impurities as flotation. This is a method for purifying limestone fine powder by removing carbon-based impurities. In the second invention, limestone raw material ore is pulverized into fine particles of 100 Messi or less, flotated with alkaline pulp using an alcohol-based foaming agent, impurities are separated as flotation, and the precipitated mineral is dried and dried. A method for highly purifying limestone fine powder by removing carbon-based impurities, characterized by rapidly heating in air at a temperature of 600 ° C. or more and 900 ° C. or less and thermally decomposing and volatilizing and removing residual carbon-containing organic matter. .

【0006】第3発明は、石灰石原料鉱石を100メッ
シ以下の微粒状に粉砕し、アルコール系の起泡剤を用い
てアルカリ性パルプで浮選し、不純物を浮鉱として分離
し、沈鉱物を、空気中で600℃以上900℃以下の温
度で急速加熱し、含炭素有機物を熱分解して揮発除去す
ることを特徴とする炭素系不純物の除去による石灰石微
粉の高純度化方法である。本発明の実施態様は、以下の
通りである。上記方法において、さらに活剤として炭酸
ナトリウムたまたは重炭酸ナトリウムを用いることを特
徴とする。上記方法において、上記活剤がさらに炭素数
3以上のアルコールを含むことを特徴とする。上記方法
において、さらに捕集剤としてケロシンを用いることを
特徴とする。上記方法において、上記鉱石の分散剤とし
てケイ酸ソーダを用いることを特徴とする。上記方法に
おいて、さらに活剤として炭酸ナトリウムたまたは重炭
酸ナトリウム及び炭素数3以上のアルコールを用い、上
記鉱石の分散剤としてケイ酸ソーダを用いることを特徴
とする。上記アルカリ性パルプを、温度約60℃以上に
保持することを特徴とする。
In a third aspect of the present invention, a limestone raw material ore is pulverized into fine particles of 100 mesh or less, flotated with alkaline pulp using an alcohol-based foaming agent, impurities are separated as flotation, and precipitated minerals are separated. This is a method for purifying limestone fine powder by removing carbon-based impurities, which is characterized by rapidly heating in air at a temperature of 600 ° C. or more and 900 ° C. or less to thermally decompose and volatilize and remove carbon-containing organic matter. Embodiments of the present invention are as follows. The above method is characterized in that sodium carbonate or sodium bicarbonate is further used as an activator. The above method is characterized in that the activator further contains an alcohol having 3 or more carbon atoms. The above method is further characterized in that kerosene is used as a collecting agent. The above method is characterized in that sodium silicate is used as the ore dispersant. The above method is further characterized in that sodium carbonate or sodium bicarbonate and an alcohol having 3 or more carbon atoms are used as an activator, and sodium silicate is used as a dispersant for the ore. The alkaline pulp is maintained at a temperature of about 60 ° C. or higher.

【0007】本発明において、石灰石原料鉱石を100
メッシを超えて粒状に粉砕した場合、不純物あるいは不
純物を含む鉱石を効率的に浮遊させることができない問
題がある。上記鉱物を600℃未満の温度で加熱して
も、炭素系不純物は熱分解せず除去することができな
い。上記鉱物を900℃を超えた温度で加熱すると、石
灰石原料鉱石が変質するおそれがある。上記アルカリ性
パルプのパルプは、選鉱法の用語であって、水中に鉱石
微粉末を分散させた懸濁液を意味する。上記アルコール
系の起泡剤としては、 Dowfros(ジェチレン・グライコ
ール・カービノールの同族体混合物)、MIBC(メチ
ル・イソブチル・カービノール)、パイン油等が挙げら
れる。
In the present invention, the limestone raw material ore is 100
When pulverized beyond the mesh, impurities or ores containing the impurities cannot be efficiently suspended. Even if the above mineral is heated at a temperature lower than 600 ° C., carbon-based impurities cannot be removed without thermal decomposition. If the mineral is heated at a temperature exceeding 900 ° C., the limestone raw material ore may be altered. The pulp of the alkaline pulp is a term of the beneficiation method and means a suspension in which ore fine powder is dispersed in water. Examples of the alcohol-based foaming agent include Dowfros (a mixture of homologues of jetylene glycol glycol), MIBC (methyl isobutyl carbinol), and pine oil.

【0008】[0008]

【発明の効果】本発明によれば、不純物の炭素質粒子を
効率良く除去し、高白色度を有する高純度の石灰石原料
粉を得ることができる効果を有する。
According to the present invention, there is an effect that carbonaceous particles as impurities can be efficiently removed and a high-purity limestone raw material powder having high whiteness can be obtained.

【0009】[0009]

【実施例】浮選は、例えば、デンパー型FW浮選機を用
いる。石灰岩(カルサイト)試料は、尻屋産であり、図
1に示すように、ステンレス製乳鉢10、コーヒーミル
12、アルミナボールの容量が約4分の1で20g/l
の割合のボールミル14を使用して、乾式で4時間粉砕
したものを使用した。その後、100mesh、150mes
h、200mesh、270mesh、400meshによって湿式
でふるい分け16をし、乾燥18させた。この試料は、
有機炭素割合が0.015%、全炭素含有率が11.9
2%であった。浮選におけるパルプ濃度は約0.6%であ
る。浮選機のセルは、約350mlで、試料をセル内に入
れ、純水を加えて攪拌しながらpHを調整した。
DESCRIPTION OF THE PREFERRED EMBODIMENTS For flotation, for example, a denper type FW flotation machine is used. The limestone (calcite) sample is from Shiriya. As shown in FIG. 1, the capacity of the stainless steel mortar 10, the coffee mill 12, and the alumina balls is about 1/4 and 20 g / l.
Was milled in a dry system for 4 hours using a ball mill 14 having a ratio of After that, 100mesh, 150mes
h, 200 mesh, 270 mesh, 400 mesh, wet sieving 16 and drying 18. This sample is
Organic carbon ratio of 0.015%, total carbon content of 11.9
2%. The pulp concentration in flotation is about 0.6%. The cell of the flotation machine was about 350 ml, and the sample was placed in the cell, pure water was added, and the pH was adjusted while stirring.

【0010】その後、図2に示すように、分散剤30、
活剤32、捕集剤34、起泡剤36の順に添加して条件
付け後、インベラ回転数1500rpm (周速50cm/s
)で5分間攪拌することにより空気を約2 l/min 導
入して浮選40した。鉱石1kg当たり、分散剤としてケ
イ酸ソーダを0.5kg、活剤としてIAA(イソアミルア
ルコール、3ーメチルー1ーブタノール)40g、捕集
剤としてケロシンを1kg、起泡剤としてMIBC(メチ
ル・イソブチル・カービノール)20gを用いて浮選し
た。起泡剤としてジエチレン・グライコール・カービノ
ールの同族体混合物であるダウフロスを使用することも
できる。分散剤として、重炭酸ソーダ、炭酸ソーダ等を
使用することもできる。温度を変化させた場合の浮選結
果を、図3に示す。図3において、横軸にパルプ温度
(°C)、左縦軸に浮上物への不純物とカルサイトの分
布率(%)及び右縦軸に沈下物中の不純物の品位(%)
を示し、グラフに付いた左右向きの矢印はそれぞれの方
向の縦軸によることを示す。60℃以上の温水を用いる
と、石灰岩中の不純物は40%浮遊し、カルサイトの精
鉱となる沈下物中の不純物は、0.17%から0.10%に
低下した。また、沈下物としてのカルサイトの実収率
は、90%以上となり良好に黒色不純物をカルサイトか
ら除去できた。
[0010] Thereafter, as shown in FIG.
After adding the active agent 32, the collector 34, and the foaming agent 36 in this order and conditioning them, the rotation speed of the invera is 1500rpm (peripheral speed 50cm / s
), The mixture was flotated 40 by introducing air at about 2 l / min. For 1 kg of ore, 0.5 kg of sodium silicate as a dispersant, 40 g of IAA (isoamyl alcohol, 3-methyl-1-butanol) as an activator, 1 kg of kerosene as a collector, and MIBC (methyl isobutyl carbinol) as a foaming agent Flotation was performed using 20 g. Dauflors, a homologous mixture of diethylene glycol glycol carbinol, can also be used as a foaming agent. As a dispersant, sodium bicarbonate, sodium carbonate, or the like can also be used. FIG. 3 shows a flotation result when the temperature is changed. In FIG. 3, the horizontal axis represents the pulp temperature (° C.), the left vertical axis represents the distribution of impurities and calcite in the floating material (%), and the right vertical axis represents the impurity quality (%) in the sediment.
The left and right arrows attached to the graph indicate the vertical axes in each direction. Using warm water above 60 ° C., the impurities in the limestone were suspended by 40%, and the impurities in the sediment, which became calcite concentrate, were reduced from 0.17% to 0.10%. The actual yield of calcite as a sediment was 90% or more, and black impurities were successfully removed from calcite.

【0011】上記沈下物はさらに、電気炉(マッフル
炉)中に入れ、空気中雰囲気で5分間まで加熱しするこ
とによって、含炭素有機物を揮発除去する。
The above sediment is further placed in an electric furnace (muffle furnace) and heated in an air atmosphere for up to 5 minutes to volatilize and remove the carbon-containing organic matter.

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

【図1】本発明の実施例の炭素系不純物の浮遊除去によ
る石灰石微粉の高純度化方法における粉砕工程の工程図
である。
FIG. 1 is a process diagram of a pulverizing step in a method for purifying limestone fine powder by floating removal of carbon-based impurities according to an embodiment of the present invention.

【図2】本発明の実施例の炭素系不純物の浮遊除去によ
る石灰石微粉の高純度化方法における浮選工程の工程図
である。
FIG. 2 is a process diagram of a flotation step in a method for purifying limestone fine powder by floating removal of carbon-based impurities according to an embodiment of the present invention.

【図3】本発明の実施例の炭素系不純物の浮遊除去によ
る石灰石微粉の高純度化方法による浮選結果を示すグラ
フ説明図である。
FIG. 3 is a graph illustrating the results of flotation by a method for purifying limestone fine powder by floating removal of carbon-based impurities according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 ステンレス製乳鉢 12 コーヒーミル 14 ボールミル 16 ふるい分け 18 乾燥 30 分散剤 32 活剤 34 捕集剤 36 起泡剤 40 浮選 Reference Signs List 10 mortar made of stainless steel 12 coffee mill 14 ball mill 16 sieving 18 drying 30 dispersant 32 active agent 34 collecting agent 36 foaming agent 40 flotation

───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤田 豊久 秋田県秋田市広面高田13−4 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Toyohisa Fujita 13-4 Hiromotakada, Akita City, Akita Prefecture

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 石灰石原料鉱石を100メッシ以下の微
粒状に粉砕し、アルコール系の起泡剤を用いてアルカリ
性パルプで浮選し、不純物を浮鉱として分離することを
特徴とする炭素系不純物の浮遊除去による石灰石微粉の
高純度化方法。
1. A carbon-based impurity characterized in that limestone raw material ore is pulverized into fine particles of 100 mesh or less, flotated with alkaline pulp using an alcohol-based foaming agent, and impurities are separated as flotation. Method of purifying limestone fine powder by floating removal of water.
【請求項2】 上記方法において、さらに活剤として炭
酸ナトリウムたまたは重炭酸ナトリウムを用いることを
特徴とする請求項1に記載の炭素系不純物の浮遊除去に
よる石灰石微粉の高純度化方法。
2. The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 1, wherein sodium carbonate or sodium bicarbonate is further used as an active agent.
【請求項3】 上記方法において、上記活剤がさらに炭
素数3以上のアルコールを含むことを特徴とする請求項
2に記載の炭素系不純物の浮遊除去による石灰石微粉の
高純度化方法。
3. The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 2, wherein the active agent further contains an alcohol having 3 or more carbon atoms.
【請求項4】 上記方法において、さらに捕集剤として
ケロシンを用いることを特徴とする請求項1に記載の炭
素系不純物の浮遊除去による石灰石微粉の高純度化方
法。
4. The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 1, wherein kerosene is further used as a collector in the above method.
【請求項5】 上記方法において、上記鉱石の分散剤と
してケイ酸ソーダを用いることを特徴とする請求項1に
記載の炭素系不純物の浮遊除去による石灰石微粉の高純
度化方法。
5. The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 1, wherein in the method, sodium silicate is used as a dispersant for the ore.
【請求項6】 上記方法において、さらに活剤として炭
酸ナトリウムたまたは重炭酸ナトリウム及び炭素数3以
上のアルコールを用い、上記鉱石の分散剤としてケイ酸
ソーダを用いることを特徴とする請求項1に記載の炭素
系不純物の浮遊除去による石灰石微粉の高純度化方法。
6. The method according to claim 1, further comprising using sodium carbonate or sodium bicarbonate as the active agent and an alcohol having 3 or more carbon atoms, and using sodium silicate as a dispersant for the ore. A method for purifying limestone fine powder by floating removal of the carbon-based impurities described in the above.
【請求項7】 上記アルカリ性パルプを、温度約60℃
以上に保持することを特徴とする請求項1に記載の炭素
系不純物の浮遊除去による石灰石微粉の高純度化方法。
7. The alkaline pulp is heated to a temperature of about 60 ° C.
The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 1, wherein the limestone is held as described above.
【請求項8】 上記アルカリ性パルプを、温度約60℃
以上に保持することを特徴とする請求項1に記載の炭素
系不純物の浮遊除去による石灰石微粉の高純度化方法。
8. The alkaline pulp is heated to a temperature of about 60 ° C.
The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 1, wherein the limestone is held as described above.
【請求項9】 上記炭素数3以上のアルコールが、イソ
アミルアルコールであることを特徴とする請求項3また
は6に記載の炭素系不純物の浮遊除去による石灰石微粉
の高純度化方法。
9. The method for purifying limestone fine powder by floating removal of carbon-based impurities according to claim 3, wherein the alcohol having 3 or more carbon atoms is isoamyl alcohol.
【請求項10】 石灰石原料鉱石を100メッシ以下の
微粒状に粉砕し、アルコール系の起泡剤を用いてアルカ
リ性パルプで浮選し、不純物を浮鉱として分離し、沈鉱
物を、乾燥のうえ空気中で600℃以上900℃以下の
温度で急速加熱し、残余の含炭素有機物を熱分解して揮
発除去するすることを特徴とする炭素系不純物の浮遊除
去による石灰石微粉の高純度化方法。
10. A limestone raw material ore is pulverized into fine particles of 100 mesh or less, flotated with alkaline pulp using an alcohol-based foaming agent, impurities are separated as flotation, and the precipitated mineral is dried and dried. A method for highly purifying limestone fine powder by floating removal of carbon-based impurities, which comprises rapidly heating in air at a temperature of 600 ° C. to 900 ° C. to thermally decompose and volatilize and remove the remaining carbon-containing organic matter.
JP6865897A 1997-03-21 1997-03-21 Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity Pending JPH10265218A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6865897A JPH10265218A (en) 1997-03-21 1997-03-21 Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6865897A JPH10265218A (en) 1997-03-21 1997-03-21 Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity

Publications (1)

Publication Number Publication Date
JPH10265218A true JPH10265218A (en) 1998-10-06

Family

ID=13380032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6865897A Pending JPH10265218A (en) 1997-03-21 1997-03-21 Increase of purity of fine limestone powder by flotation and removal of carbonaceous impurity

Country Status (1)

Country Link
JP (1) JPH10265218A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006256893A (en) * 2005-03-16 2006-09-28 Taiheiyo Cement Corp High-quality crystalline limestone and its production method
JP2010163343A (en) * 2009-01-19 2010-07-29 Taiheiyo Cement Corp Method for removing impurity in limestone
JP2010228988A (en) * 2009-03-27 2010-10-14 Taiheiyo Cement Corp Method and system for removing impurities of limestone
JP2011046570A (en) * 2009-08-27 2011-03-10 Taiheiyo Cement Corp Method and system for removing impurity of limestone
KR101402643B1 (en) * 2012-12-20 2014-06-03 한국지질자원연구원 Method of impurity carbon removal included limestone

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006256893A (en) * 2005-03-16 2006-09-28 Taiheiyo Cement Corp High-quality crystalline limestone and its production method
JP2010163343A (en) * 2009-01-19 2010-07-29 Taiheiyo Cement Corp Method for removing impurity in limestone
JP2010228988A (en) * 2009-03-27 2010-10-14 Taiheiyo Cement Corp Method and system for removing impurities of limestone
JP2011046570A (en) * 2009-08-27 2011-03-10 Taiheiyo Cement Corp Method and system for removing impurity of limestone
KR101402643B1 (en) * 2012-12-20 2014-06-03 한국지질자원연구원 Method of impurity carbon removal included limestone

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