JPH07267698A - Method for solidifying caco3 - Google Patents

Method for solidifying caco3

Info

Publication number
JPH07267698A
JPH07267698A JP6235694A JP6235694A JPH07267698A JP H07267698 A JPH07267698 A JP H07267698A JP 6235694 A JP6235694 A JP 6235694A JP 6235694 A JP6235694 A JP 6235694A JP H07267698 A JPH07267698 A JP H07267698A
Authority
JP
Japan
Prior art keywords
caco
substance
caco3
solubility
silica
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.)
Granted
Application number
JP6235694A
Other languages
Japanese (ja)
Other versions
JP3309092B2 (en
Inventor
Yasuo Shibazaki
靖雄 芝崎
Keiichi Inukai
恵一 犬飼
Makoto Kigami
真 樹神
Hideki Ishida
秀輝 石田
Yasuo Goto
泰男 後藤
Tatsuya Nagata
達也 永田
Takayuki Yamamoto
剛之 山本
Hiroki Maenami
洋輝 前浪
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.)
Inax Corp
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
Inax 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 Agency of Industrial Science and Technology, Inax Corp filed Critical Agency of Industrial Science and Technology
Priority to JP06235694A priority Critical patent/JP3309092B2/en
Priority to NL9500594A priority patent/NL9500594A/en
Priority to DE1995112163 priority patent/DE19512163C2/en
Publication of JPH07267698A publication Critical patent/JPH07267698A/en
Application granted granted Critical
Publication of JP3309092B2 publication Critical patent/JP3309092B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

PURPOSE:To obtain a solidified CaCO3 form at reduced cost by making use of autoclave reaction of a mixture of CaCO3 or CaCO3-dominant material and a CaCO3 solubility-raising substance. CONSTITUTION:Firstly, CaCO3 or a material containing 250wt.% of CaCO3 such as dolomite is incorporated with a silica-based substance such as noncrystalline SiO2 at an amount so as to account for ca. <=50 (esp. 10-30)wt.% of the final mixture in terms of SiO2 and, if needed, a CaCO3 solubility-raising substance such as KOH, in the form of a ca. 5mol/l aqueous solution, at an amount so as to account for ca. <=10 (esp. ca. 0.5)wt.% of the final mixture in terms of an alkali metal ion. Subsequently, the resultant mixture is molded to a specified shape by e.g. press molding and then charged into an autoclave followed by addition of an appropriate amount of water and then conducting a treatment under the saturated vapor pressure at ca. 200-250 deg.C for 2-20hr or so, to obtain the objective high-strength CaCO3 solidified form.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はCaCO3 の固化方法に
係り、特に、CaCO3 又はCaCO3 を主成分とする
物質を緩やかな処理条件にて固化させる方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for solidifying CaCO 3 , and more particularly to a method for solidifying CaCO 3 or a substance containing CaCO 3 as a main component under mild treatment conditions.

【0002】[0002]

【従来の技術】各種産業分野で排出される排ガス中のC
2 は、地球の温暖化現象への影響が懸念されているこ
とから、大気中のCO2 の低減について検討が進められ
ている。
2. Description of the Related Art C in exhaust gas emitted from various industrial fields
Since it is feared that O 2 will affect the global warming phenomenon, studies are underway to reduce CO 2 in the atmosphere.

【0003】従来、大気中のCO2 の低減技術として、
燃焼排ガスなどのCO2 含有ガスを海水に吸収させて、
CO2 をCaCO3 又は(Ca・Mg)CO3 として固
定化する方法がある。
Conventionally, as a technique for reducing CO 2 in the atmosphere,
By absorbing CO 2 -containing gas such as combustion exhaust gas into seawater,
There is a method of immobilizing CO 2 as CaCO 3 or (Ca · Mg) CO 3 .

【0004】CaCO3 の固化方法として、特開平3−
252341号公報には、炭酸カルシウム、ガラス、N
aOH及び水の混合物を200℃以上かつ100kg/
cm2 以上の高温高圧で処理する方法が記載されてい
る。
As a method for solidifying CaCO 3 , Japanese Patent Laid-Open No.
No. 252341 discloses calcium carbonate, glass, N.
A mixture of aOH and water above 200 ° C and 100 kg /
A method of treating at high temperature and high pressure of cm 2 or more is described.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、上記の
CaCO3 の固化方法は、処理条件が高温、高圧の過酷
な条件であると共に、装置設備が複雑であることから、
大量処理には不向きである。また、消費エネルギーが大
きく、処理コストが高くつくという欠点がある。本発明
は上記従来の問題点を解決し、CaCO3 又はCaCO
3 を主成分とする物質を緩やかな条件で固化することが
できる方法を提供することを目的とする。
However, in the method for solidifying CaCO 3 described above, since the processing conditions are severe conditions of high temperature and high pressure, and the equipment is complicated,
Not suitable for large-scale processing. In addition, there are disadvantages that the energy consumption is large and the processing cost is high. The present invention solves the above-mentioned problems of the related art, and CaCO 3 or CaCO 3
An object is to provide a method capable of solidifying a substance containing 3 as a main component under mild conditions.

【0006】[0006]

【課題を解決するための手段】請求項1のCaCO3
固化方法は、CaCO3 又はCaCO3 を主成分とする
物質と、CaCO3 の溶解度を高める物質を混合した
後、オートクレーブ反応を利用して固化させることを特
徴とするものである。
The method for solidifying CaCO 3 according to claim 1 uses an autoclave reaction after mixing a substance containing CaCO 3 or CaCO 3 as a main component with a substance which enhances the solubility of CaCO 3. It is characterized in that it is solidified.

【0007】請求項2のCaCO3 の固化方法は、Ca
CO3 又はCaCO3 を主成分とする物質に、シリカ系
物質と、CaCO3 及び/又はシリカ系物質の溶解度を
高める物質とを混合した後、オートクレーブ反応を利用
して固化させることを特徴とするものである。
The method for solidifying CaCO 3 according to claim 2 is Ca
It is characterized in that a silica-based substance and a substance that enhances the solubility of CaCO 3 and / or the silica-based substance are mixed with a substance containing CO 3 or CaCO 3 as a main component, and then solidified by utilizing an autoclave reaction. It is a thing.

【0008】請求項3のCaCO3 の固化方法は、Ca
CO3 又はCaCO3 を主成分とする物質をオートクレ
ーブ反応を利用して固化させる方法であって、CaCO
3 の溶解度を高める物質の溶液をオートクレーブ処理溶
液として用いることを特徴とするものである。
The method for solidifying CaCO 3 according to claim 3 is Ca
A method of solidifying a substance containing CO 3 or CaCO 3 as a main component by using an autoclave reaction.
It is characterized in that a solution of a substance which enhances the solubility of 3 is used as an autoclave treatment solution.

【0009】請求項4のCaCO3 の固化方法は、Ca
CO3 又はCaCO3 を主成分とする物質に、シリカ系
物質を混合した後、オートクレーブ反応を利用して固化
させる方法であって、CaCO3 及び/又は該シリカ系
物質の溶解度を高める物質の溶液をオートクレーブ処理
溶液として用いることを特徴とするものである。
A method for solidifying CaCO 3 according to claim 4 is as follows.
A method in which a silica-based material is mixed with a material containing CO 3 or CaCO 3 as a main component and then solidified by using an autoclave reaction, which is a solution of CaCO 3 and / or a material that enhances the solubility of the silica-based material. Is used as an autoclave treatment solution.

【0010】以下に本発明を詳細に説明する。The present invention will be described in detail below.

【0011】本発明のCaCO3 の固化方法において、
原料となるCaCO3 又はCaCO3 を主成分とする物
質としては、例えば、燃焼排ガス中のCO2 を海水等に
吸収させて、CaCO3 又は(Ca・Mg)CO3 とし
て固定化して得られる物質が挙げられるが、何らこれら
の物質に制限されるものではなく、本発明はCaCO3
又はCaCO3 を主成分として50重量%以上含有する
物質(例えば、CaCO3 分が50%以上であるドロマ
イト)であれば有効に適用することができる。本発明に
おいては、CaCO3 又はCaCO3 を含む物質にシリ
カ系物質を混合して処理することもできる。シリカ系物
質としては、非晶質SiO2 ,結晶質SiO2 の他、ケ
イ砂、キラ微砂、ケイ藻土、粘土、シリカヒューム、ホ
ワイトカーボン、タイル屑、ガラス屑、レンガ屑、スラ
グ、セメント・コンクリート廃材、石炭灰、汚泥、釉汚
泥、汚泥焼却灰、Ca分を抽出後の産業廃棄物(例えば
セメント・コンクリート廃材、スラグ、釉汚泥、石炭
灰、汚泥焼却灰、ガラス屑のCa分を抽出したもの)等
を用いることができる。
In the method for solidifying CaCO 3 of the present invention,
Examples of the raw material CaCO 3 or a substance containing CaCO 3 as a main component include substances obtained by absorbing CO 2 in combustion exhaust gas into seawater or the like and fixing it as CaCO 3 or (Ca · Mg) CO 3. However, the present invention is not limited to these substances, and the present invention provides CaCO 3
Alternatively, a substance containing CaCO 3 as a main component in an amount of 50% by weight or more (for example, dolomite having a CaCO 3 content of 50% or more) can be effectively applied. In the present invention, CaCO 3 or a substance containing CaCO 3 may be mixed with a silica-based substance for treatment. Examples of the silica-based substance include amorphous SiO 2 , crystalline SiO 2 , silica sand, fine sand, diatomaceous earth, clay, silica fume, white carbon, tile scrap, glass scrap, brick scrap, slag, cement・ Concrete waste materials, coal ash, sludge, glaze sludge, sludge incineration ash, industrial waste after extraction of Ca content (for example, cement / concrete waste material, slag, glaze sludge, coal ash, sludge incineration ash, glass scrap Ca content (Extracted) and the like can be used.

【0012】シリカ系物質を混合した場合には、得られ
る固化体中にC−S−H(CaO−SiO2 −H2 O系
固形物質)が生成し、固化体の強度を高めることができ
る。
When a silica-based material is mixed, C--S--H (CaO--SiO 2 --H 2 O-based solid material) is produced in the solidified product obtained, and the strength of the solidified product can be increased. .

【0013】なお、シリカ系物質を用いる場合、その使
用割合は、多過ぎると相対的にCaCO3 又はCaCO
3 を主成分とする物質の割合が低減してCaCO3 の固
化による有効利用の面での効率が低下するため、シリカ
系物質の使用量は、混合後の原料中において占める割合
がSiO2 換算で50重量%以下、特に10〜30重量
%となるようにするのが好ましい。
When a silica-based material is used, if its usage rate is too high, CaCO 3 or CaCO 3
Since the ratio of the substance containing 3 as a main component is reduced and the efficiency of effective utilization due to solidification of CaCO 3 is reduced, the amount of the silica-based substance used is the ratio in the raw material after mixing converted to SiO 2. Is preferably 50% by weight or less, and particularly preferably 10 to 30% by weight.

【0014】本発明では、CaCO3 又はCaCO3
含む物質に、CaCO3 の溶解度を高める物質を混合し
ても良い。
In the present invention, the material containing CaCO 3 or CaCO 3, may be mixed substances which increase the solubility of CaCO 3.

【0015】また、本発明では、CaCO3 又はCaC
3 を含む物質に対し、上記のシリカ系物質と、CaC
3 及び/又は該シリカ系物質の溶解度を高める物質と
を混合しても良い。
Further, in the present invention, CaCO 3 or CaC
For the substances containing O 3 , the above-mentioned silica-based substances and CaC
O 3 and / or a substance that enhances the solubility of the silica-based substance may be mixed.

【0016】この溶解度を高める物質(以下、「溶解度
増大物質」ということがある。)は、固形物、ゲル状、
液状のいずれであっても良い。なお、溶解度増大物質
は、水などの溶媒に溶解又は希釈させて混合しても良
い。
The substance that enhances the solubility (hereinafter, may be referred to as “solubility-increasing substance”) is a solid substance, a gel-like substance,
It may be liquid. The solubility-enhancing substance may be dissolved or diluted in a solvent such as water and mixed.

【0017】この溶解度増大物質としては、LiOH,
NaOH,KOH,NH4 OH,Li2 CO3 ,Na2
CO3 ,K2 CO3 ,(NH42 CO3 ,LiHCO
3 ,NaHCO3 ,KHCO3 ,NH4 HCO3 ,Li
NO3 ,NaNO3 ,KNO3 ,NH4 NO3 ,Ca
(NO32 ,LiF,NaF,KF,NH4 F,Li
Cl,NaCl,KCl,NH4 Cl,LiBr,Na
Br,KBr,NH4 Brなどの水酸化アルカリ、アル
カリ塩、炭酸アルカリ、炭酸水素アルカリ、ハロゲン化
アルカリ等アルカリ系物質ならびにアンモニウム系物質
や、これらを含む物質が好適である。また、酸化アルカ
リを含む物質(例えばガラス、鉱物など)等も好適であ
る。この溶解度増大物質は、産業廃棄物を利用するのが
好適である。なお、これらの溶解度増大物質は、CaC
3 及び/又はシリカ系物質の溶解度を高める作用を有
する。
As the solubility-increasing substance, LiOH,
NaOH, KOH, NH 4 OH, Li 2 CO 3 , Na 2
CO 3 , K 2 CO 3 , (NH 4 ) 2 CO 3 , LiHCO
3 , NaHCO 3 , KHCO 3 , NH 4 HCO 3 , Li
NO 3 , NaNO 3 , KNO 3 , NH 4 NO 3 , Ca
(NO 3 ) 2 , LiF, NaF, KF, NH 4 F, Li
Cl, NaCl, KCl, NH 4 Cl, LiBr, Na
Alkaline hydroxides such as Br, KBr, NH 4 Br, alkali salts, alkali carbonates, alkali hydrogen carbonates, alkali halides and other alkali-based substances, ammonium-based substances, and substances containing these are preferable. In addition, substances containing alkali oxides (eg glass, minerals, etc.) are also suitable. It is preferable to use industrial waste as the solubility enhancing substance. In addition, these solubility-increasing substances are CaC.
It has the effect of increasing the solubility of O 3 and / or the silica-based substance.

【0018】このような溶解度増大物質は、混合後の原
料中においてアルカリ金属イオン又はアンモニウムイオ
ンの占める割合が10重量%以下、特に0.1〜5重量
%となるようにするのが好適である。又、このような溶
解度増大物質を、同時に複数種類混合しても良い。
It is preferable that such a solubility-increasing substance has an alkali metal ion or ammonium ion content of 10% by weight or less, particularly 0.1 to 5% by weight, in the raw materials after mixing. . Further, plural kinds of such solubility enhancing substances may be mixed at the same time.

【0019】CaCO3 又はCaCO3 を主成分とする
物質に、必要に応じてシリカ系物質や溶解度増大物質を
混合して得られる固化原料は、プレス成形、鋳込成形、
押出成形、流し込み成形等の成形法により所望の形状に
成形した後、オートクレーブ処理する。なお、固化原料
は特に成形を行なわず、そのままオートクレーブ処理し
た後、成形し、さらにオートクレーブ処理しても良い。
The solidification raw material obtained by mixing CaCO 3 or a substance containing CaCO 3 as a main component with a silica-based substance or a solubility-increasing substance, if necessary, is formed by press molding, cast molding,
After being molded into a desired shape by a molding method such as extrusion molding or cast molding, it is autoclaved. The solidified raw material may be autoclaved as it is without being molded, and then molded and further autoclaved.

【0020】本発明では、この固化原料が上記溶解度増
大物質を含む場合には、オートクレーブ処理液は、水で
あっても良く、上記溶解度増大物質の溶液であっても良
い。この固化原料が上記溶解度増大物質を含まないとき
には、オートクレーブ処理溶液として、この溶解度増大
物質の溶液を用いる。
In the present invention, when the solidification raw material contains the solubility-increasing substance, the autoclave treatment liquid may be water or a solution of the solubility-increasing substance. When the solidified material does not contain the solubility-increasing substance, the solution of the solubility-increasing substance is used as the autoclave treatment solution.

【0021】溶解度増大物質の溶液は、その中に含まれ
るアルカリ金属イオン又はアンモニウムイオンが5mo
l/l以下とりわけ0.01〜1mol/lとなるよう
にするのが好適である。
In the solution of the solubility-enhancing substance, the alkali metal ion or ammonium ion contained therein is 5 mo.
It is preferably 1 / l or less, particularly 0.01 to 1 mol / l.

【0022】オートクレーブ処理は、150〜300
℃、特に200〜250℃程度の飽和蒸気圧(40kg
f/cm2 以下)下という比較的緩やかな条件で行なう
ことができ、その処理時間は通常の場合、2〜20時
間、特に5〜10時間程度とされる。
The autoclave treatment is 150 to 300
Saturated vapor pressure (40kg)
f / cm 2 or less), which is a relatively mild condition, and the treatment time is usually 2 to 20 hours, particularly 5 to 10 hours.

【0023】得られた固化体は、必要に応じて適当な条
件で乾燥した後、各種建設・土木材料等として利用され
る。
The solidified product thus obtained is dried under appropriate conditions, if necessary, and then used as various construction and civil engineering materials.

【0024】本発明においては、CaCO3 又はCaC
3 を主成分とする物質を酸処理、イオン交換樹脂によ
る処理等により表面処理しておいても良い。
In the present invention, CaCO 3 or CaC
A substance containing O 3 as a main component may be surface-treated by acid treatment, treatment with an ion exchange resin, or the like.

【0025】[0025]

【作用】請求項1,3の方法においては、オートクレー
ブ処理により、CaCO3 の溶解と再析出反応が進行
し、CaCO3 等の固形粒子同志が結合する。これによ
り、従来法に比べて低温、低圧の緩やかな条件で、Ca
CO3 又はCaCO3 を主成分とする物質を固化させる
ことができる。
[Action] In the method according to claim 1 and 3, by autoclaving, proceeds dissolved and re-precipitation reaction of CaCO 3 are solid particles comrades like CaCO 3 are attached. As a result, compared to the conventional method, the Ca is
A substance containing CO 3 or CaCO 3 as a main component can be solidified.

【0026】請求項2,4の方法においては、CaCO
3 及びシリカ系物質の溶解及び反応によりC−S−H
(CaO−SiO2 −H2 O系物質)が生成し、このC
−S−Hによって固形粒子同志が強固に結合し、成形体
が固化される。
In the methods of claims 2 and 4, CaCO
C-S-H by dissolution and reaction of 3 and silica-based materials
(CaO-SiO 2 -H 2 O-based material) is generated, this C
Solid particles are firmly bound to each other by -SH, and the molded body is solidified.

【0027】請求項1,2においては、混合された溶解
度増大物質により、上記の溶解及び反応が促進される。
In the first and second aspects, the solubility and the reaction are promoted by the mixed solubility-enhancing substance.

【0028】請求項3,4においては、オートクレーブ
処理液中の溶解度増大物質が気相(例えば水蒸気)を介
して成形体中に入り込み、上記の溶解及び反応が促進さ
れる。
In the third and fourth aspects, the solubility-increasing substance in the autoclave treatment solution enters the molded body through the gas phase (for example, water vapor) to accelerate the above-mentioned dissolution and reaction.

【0029】[0029]

【実施例】以下に実施例を挙げて本発明をより具体的に
説明する。なお、実施例において用いた溶解度増大物質
以外の原料は下記表1の通りである。
EXAMPLES The present invention will be described in more detail with reference to the following examples. The raw materials other than the solubility-increasing substances used in the examples are shown in Table 1 below.

【0030】[0030]

【表1】 [Table 1]

【0031】また、各試料の曲げ強度の測定は、スパン
間距離30mm,クロスヘッドスピード0.5mm/m
inの3点曲げ強度測定条件で行なった。
The bending strength of each sample was measured with a span distance of 30 mm and a crosshead speed of 0.5 mm / m.
The in-point three-point bending strength was measured.

【0032】実施例1 溶解度増大物質として0.1mol/lのKOH水溶液
を用い、表2に示す配合にて原料を乳鉢で乾式混合し、
300kgf/cm2 で加圧成形して40mm×10m
m×約10mm厚さの成形体を得た。得られた成形体の
曲げ強度を表2に示す。各成形体をオートクレーブに入
れ、表2に示す条件で処理して固化させた。なお、オー
トクレーブの容器(2000cc容量)中には蒸留水を
290cc入れて飽和蒸気圧にて処理した。
Example 1 A 0.1 mol / l KOH aqueous solution was used as a solubility-increasing substance, and the raw materials were dry-mixed in a mortar in the composition shown in Table 2,
40 mm x 10 m after pressure molding at 300 kgf / cm 2.
A molded body with m × about 10 mm thickness was obtained. Table 2 shows the bending strength of the obtained molded body. Each molded body was put into an autoclave and treated under the conditions shown in Table 2 to be solidified. It should be noted that 290 cc of distilled water was put into a container (2000 cc capacity) of the autoclave and treated at a saturated vapor pressure.

【0033】得られた固化体を60℃で乾燥した後、曲
げ強度の測定を行ない結果を表2に示した。 実施例2 KOHの水溶液を原料に添加せず、その代わりにオート
クレーブ処理水として0.1mol/lのKOH水溶液
を用いたほかは実施例1と同様にして固化処理を行なっ
た。その結果を表2に併せて示す。
The resulting solidified product was dried at 60 ° C., and then the bending strength was measured. The results are shown in Table 2. Example 2 A solidification treatment was performed in the same manner as in Example 1 except that an aqueous solution of KOH was not added to the raw material and an aqueous solution of 0.1 mol / l KOH was used as the autoclaved water instead. The results are also shown in Table 2.

【0034】比較例1 実施例1において、KOH水溶液を全く添加しなかった
こと以外は全く同様にして固化処理を行なった。その曲
げ強度の測定結果を表2に併せて示す。
Comparative Example 1 A solidification treatment was carried out in the same manner as in Example 1, except that the KOH aqueous solution was not added at all. The measurement results of the bending strength are also shown in Table 2.

【0035】表2より、次のことが明らかである。即
ち、オートクレーブ処理によれば、280℃以下の温度
での飽和蒸気圧の処理で、CaCO3 又はCaCO3
SiO2 の混合物を容易に固化させることができる。特
に、SiO2 として非晶質SiO2 を用いた場合には、
固化体の強度を著しく高めることができる。
From Table 2, the following is clear. That is, according to the autoclave treatment, CaCO 3 or a mixture of CaCO 3 and SiO 2 can be easily solidified by the saturated vapor pressure treatment at a temperature of 280 ° C. or lower. Particularly, in the case of using an amorphous SiO 2 as SiO 2 is
The strength of the solidified body can be significantly increased.

【0036】また、KOH水溶液の添加や、KOH水溶
液をオートクレーブ処理液として用いることにより、成
形体の強度をさらに高めることができる。
The strength of the molded article can be further increased by adding an aqueous KOH solution or by using the aqueous KOH solution as an autoclave treating solution.

【0037】[0037]

【表2】 [Table 2]

【0038】実施例3 実施例1のNo. 2において、CaCO3 に混合する溶解
度増大物質としてKOH水溶液の代わりに表3のものを
用いたこと以外は全く同様にして固化処理を行ない、固
化体の曲げ強度を測定した。結果を表3に併せて示す。
Example 3 The solidification treatment was carried out in the same manner as in No. 2 of Example 1 except that the solubility increasing substance mixed with CaCO 3 was replaced with the KOH aqueous solution shown in Table 3. The bending strength of was measured. The results are also shown in Table 3.

【0039】実施例4 実施例2のNo. 2において、オートクレーブ処理水に溶
解させる溶解度増大物質としてKOH水溶液の代わりに
表3のものを用いたこと以外は全く同様にして固化処理
を行ない、固化体の曲げ強度を測定した。結果を表3に
併せて示す。
Example 4 No. 2 of Example 2 was subjected to solidification treatment and solidification in the same manner as in Example 2, except that the aqueous KOH solution was used as the solubility increasing substance to be dissolved in the autoclaved water. The bending strength of the body was measured. The results are also shown in Table 3.

【0040】[0040]

【表3】 [Table 3]

【0041】実施例5 実施例1のNo. 10において、CaCO3 に混合する溶
解度増大物質としてKOH水溶液の代わりに表4のもの
を用いたこと以外は全く同様にして固化処理を行ない、
固化体の曲げ強度を測定した。結果を表4に併せて示
す。
Example 5 Solidification treatment was carried out in the same manner as in No. 10 of Example 1, except that the solubility increasing substance mixed with CaCO 3 was replaced with the KOH aqueous solution shown in Table 4.
The bending strength of the solidified body was measured. The results are also shown in Table 4.

【0042】実施例6 実施例2のNo. 10において、オートクレーブ処理水に
溶解させる溶解度増大物質としてKOH水溶液の代わり
に表4のものを用いたこと以外は全く同様にして固化処
理を行ない、固化体の曲げ強度を測定した。結果を表4
に併せて示す。
Example 6 Solidification was carried out and solidified in the same manner as in No. 10 of Example 2 except that the KOH aqueous solution as shown in Table 4 was used as the solubility-increasing substance dissolved in the autoclaved water. The bending strength of the body was measured. The results are shown in Table 4.
Are also shown.

【0043】[0043]

【表4】 [Table 4]

【0044】実施例7 実施例1のNo. 10において、シリカ系物質として結晶
質SiO2 の代わりに表5のものを用いたこと以外は全
く同様にして固化処理を行ない、固化体の曲げ強度を測
定した。結果を表5に併せて示す。
Example 7 No. 10 of Example 1 was subjected to the solidification treatment in the same manner except that the silica-based material shown in Table 5 was used instead of the crystalline SiO 2 , and the bending strength of the solidified body was obtained. Was measured. The results are also shown in Table 5.

【0045】なお、表5には、各シリカ系物質の分析値
も併せて示す。水分を含んでいるものは乾燥後、添加し
た。No. 85の産廃(産業廃棄物)は、スラグからCa
分を抽出したものである。
Table 5 also shows the analytical values of each silica-based substance. Those containing water were added after drying. The industrial waste of No. 85 (industrial waste) is Ca from slag.
It is the extracted minutes.

【0046】[0046]

【表5】 [Table 5]

【0047】[0047]

【発明の効果】以上詳述した通り、本発明のCaCO3
の固化方法によれば、一般的な装置であるオートクレー
ブによる処理によりCaCO3 又はCaCO3 を主成分
とする物質を、比較的低温、低圧の緩やかな条件下で容
易かつ効率的に固化させることができ、CaCO3 固化
技術における省エネルギー、省コスト化を図ることがで
きる。
As described above in detail, the CaCO 3 of the present invention is used.
According to the solidification method of (1), CaCO 3 or a substance containing CaCO 3 as a main component can be easily and efficiently solidified under mild conditions of relatively low temperature and low pressure by treatment with an autoclave which is a general apparatus. Therefore, energy saving and cost saving in the CaCO 3 solidification technique can be achieved.

【0048】本発明によれば、燃焼排ガス中のCO2
CaCO3 又は(Ca・Mg)CO3 として固定化して
回収したものを低処理コストにて固化して、建設・土木
材料等への有効利用を図ることができる。
According to the present invention, CO 2 in combustion exhaust gas is fixed as CaCO 3 or (Ca.Mg) CO 3 and recovered, which is solidified at a low treatment cost to be used for construction and civil engineering materials. It can be effectively used.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 犬飼 恵一 愛知県名古屋市緑区万場山1−1208 フレ グランス万場山A−202 (72)発明者 樹神 真 愛知県知多市梅が丘1−285 ロイヤルハ イツB−203 (72)発明者 石田 秀輝 愛知県半田市堀崎町2−17 コープ野村半 田3棟 604号 (72)発明者 後藤 泰男 愛知県半田市仲田町1−38 (72)発明者 永田 達也 愛知県知多郡武豊町砂川1−29 (72)発明者 山本 剛之 愛知県常滑市字古道東割29−13 第7若竹 寮 (72)発明者 前浪 洋輝 愛知県常滑市港町1−29 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Keiichi Inukai 1-1208 Manbayama, Midori-ku, Nagoya-shi, Aichi Fregulance Manbayama A-202 (72) Inventor, Magami 1-285 Umegaoka, Chita-shi, Aichi Prefecture Royal Heights B-203 (72) Inventor Hideteru Ishida 2-17 Horizaki-cho, Handa-shi, Aichi Corp. Nomura Hanta 3 Building No. 604 (72) Inventor Yasuo Goto 1-38 Nakata-cho, Handa-shi, Aichi (72) Inventor Tatsuya Nagata 1-29 Sunagawa, Taketoyo-cho, Chita-gun, Aichi Prefecture (72) Inventor Takeyuki Yamamoto 29-13 Koto Higashiwari, Tokoname City, Aichi Prefecture 7th Wakatake Dormitory (72) Yoteru Maenami 1-29 Minatomachi, Tokoname City, Aichi Prefecture

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 CaCO3 又はCaCO3 を主成分とす
る物質と、CaCO3 の溶解度を高める物質を混合した
後、オートクレーブ反応を利用して固化させることを特
徴とするCaCO3 の固化方法。
1. A method for solidifying CaCO 3 , which comprises mixing CaCO 3 or a substance containing CaCO 3 as a main component with a substance which enhances the solubility of CaCO 3 , and then solidifying the mixture by using an autoclave reaction.
【請求項2】 CaCO3 又はCaCO3 を主成分とす
る物質に、シリカ系物質と、CaCO3 及び/又はシリ
カ系物質の溶解度を高める物質とを混合した後、オート
クレーブ反応を利用して固化させることを特徴とするC
aCO3 の固化方法。
2. A CaCO 3 or CaCO 3 -based substance is mixed with a silica-based substance and a substance that enhances the solubility of CaCO 3 and / or the silica-based substance, and then solidified by utilizing an autoclave reaction. C characterized by
Solidification method of aCO 3 .
【請求項3】 CaCO3 又はCaCO3 を主成分とす
る物質をオートクレーブ反応を利用して固化させる方法
であって、CaCO3 の溶解度を高める物質の溶液をオ
ートクレーブ処理溶液として用いることを特徴とするC
aCO3 の固化方法。
3. A method of solidifying CaCO 3 or a substance containing CaCO 3 as a main component by using an autoclave reaction, wherein a solution of a substance that enhances the solubility of CaCO 3 is used as an autoclave treatment solution. C
Solidification method of aCO 3 .
【請求項4】 CaCO3 又はCaCO3 を主成分とす
る物質に、シリカ系物質を混合した後、オートクレーブ
反応を利用して固化させる方法であって、CaCO3
び/又は該シリカ系物質の溶解度を高める物質の溶液を
オートクレーブ処理溶液として用いることを特徴とする
CaCO3 の固化方法。
4. A method of mixing CaCO 3 or a substance containing CaCO 3 as a main component with a silica-based substance and then solidifying the mixture by using an autoclave reaction, wherein the solubility of CaCO 3 and / or the silica-based substance is increased. A method of solidifying CaCO 3 , characterized in that a solution of a substance that enhances the use of CaCO 3 is used as an autoclaving solution.
JP06235694A 1994-03-31 1994-03-31 Method for solidifying CaCO3 Expired - Lifetime JP3309092B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP06235694A JP3309092B2 (en) 1994-03-31 1994-03-31 Method for solidifying CaCO3
NL9500594A NL9500594A (en) 1994-03-31 1995-03-28 Method for hardening CaCO3 and / or MgCO3.
DE1995112163 DE19512163C2 (en) 1994-03-31 1995-03-31 Process for the preparation of a solidified material containing CaCO¶3¶

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06235694A JP3309092B2 (en) 1994-03-31 1994-03-31 Method for solidifying CaCO3

Publications (2)

Publication Number Publication Date
JPH07267698A true JPH07267698A (en) 1995-10-17
JP3309092B2 JP3309092B2 (en) 2002-07-29

Family

ID=13197760

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06235694A Expired - Lifetime JP3309092B2 (en) 1994-03-31 1994-03-31 Method for solidifying CaCO3

Country Status (1)

Country Link
JP (1) JP3309092B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0881217A (en) * 1994-09-13 1996-03-26 Inax Corp Solidification of caco3
JP2006075717A (en) * 2004-09-09 2006-03-23 Nippon Steel Corp Utilization method of carbon dioxide
JP2014516023A (en) * 2011-06-09 2014-07-07 ラトガーズ, ザ ステイト ユニバーシティ オブ ニュー ジャージー Synthetic formulations and methods of making and using them
CN114591052A (en) * 2022-02-25 2022-06-07 碳达(深圳)新材料技术有限责任公司 Method for preparing building material by using high-temperature flue gas and alkaline solid waste

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0881217A (en) * 1994-09-13 1996-03-26 Inax Corp Solidification of caco3
JP2006075717A (en) * 2004-09-09 2006-03-23 Nippon Steel Corp Utilization method of carbon dioxide
JP2014516023A (en) * 2011-06-09 2014-07-07 ラトガーズ, ザ ステイト ユニバーシティ オブ ニュー ジャージー Synthetic formulations and methods of making and using them
CN114591052A (en) * 2022-02-25 2022-06-07 碳达(深圳)新材料技术有限责任公司 Method for preparing building material by using high-temperature flue gas and alkaline solid waste

Also Published As

Publication number Publication date
JP3309092B2 (en) 2002-07-29

Similar Documents

Publication Publication Date Title
CN106377867A (en) Curing agent and curing method for heavy metals in fly ash from mswi (municipal solid waste incineration)
JP3632222B2 (en) CaCO3 solidification method
CN110467368B (en) Active excitant for inorganic solid waste building material and preparation method thereof
CN105772483A (en) Incineration fly ash synchronous solidification/stabilization method based on geo-polymerization
JP2006075717A (en) Utilization method of carbon dioxide
KR100771490B1 (en) Manufacturing method of solidification agent for organic or inorganic waste resources
NL9500594A (en) Method for hardening CaCO3 and / or MgCO3.
CN115594429A (en) Method for building material utilization based on amino carbonation modification combined with cement solidification fly ash
JPH0761842A (en) Solidification of caco3
JPH07265688A (en) Method for fixing co2
CN113213498B (en) Cement-based material carbonization recycling method and calcium carbonate whisker material
JPH07267698A (en) Method for solidifying caco3
JP3274376B2 (en) Agglomerating agent for mud, solidifying agent using it
CN111499281A (en) Crystal sludge and water purifying agent waste residue geopolymer grouting material and preparation method thereof
JP2013086030A (en) Method for treating dolomite sludge and soil improving material
KR100472907B1 (en) Composition of material treating Sludge
JP3341009B2 (en) Method for solidifying MgCO3
JP3338828B2 (en) Method for solidifying CaCO3 and / or MgCO3
JP3685553B2 (en) Stabilized incineration ash-based solidification material
JPS62260753A (en) Neutral consolidating agent and manufacture
CN117185691B (en) Method for regenerating baking-free artificial lightweight aggregate by cooperatively disposing aluminum ash and garbage incineration fly ash
JP2000350976A (en) Method for solidifying granular steel-making slag
JPS6219798B2 (en)
JPS6158239B2 (en)
JPH0848549A (en) Slag curing material

Legal Events

Date Code Title Description
S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080524

Year of fee payment: 6

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100524

Year of fee payment: 8

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100524

Year of fee payment: 8

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313117

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 8

Free format text: PAYMENT UNTIL: 20100524

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

EXPY Cancellation because of completion of term