JPH0881217A - Solidification of caco3 - Google Patents
Solidification of caco3Info
- Publication number
- JPH0881217A JPH0881217A JP6218681A JP21868194A JPH0881217A JP H0881217 A JPH0881217 A JP H0881217A JP 6218681 A JP6218681 A JP 6218681A JP 21868194 A JP21868194 A JP 21868194A JP H0881217 A JPH0881217 A JP H0881217A
- Authority
- JP
- Japan
- Prior art keywords
- caco
- raw material
- caco3
- autoclave
- solidifying
- 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
Links
- 238000007711 solidification Methods 0.000 title claims abstract description 10
- 230000008023 solidification Effects 0.000 title claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 36
- 239000000126 substance Substances 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 238000000034 method Methods 0.000 claims description 23
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 22
- 239000000377 silicon dioxide Substances 0.000 claims description 9
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 230000009257 reactivity Effects 0.000 abstract description 3
- 239000013535 sea water Substances 0.000 abstract description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract 16
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract 8
- 235000010216 calcium carbonate Nutrition 0.000 abstract 8
- 238000001354 calcination Methods 0.000 description 9
- 238000000465 moulding Methods 0.000 description 7
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- 238000005452 bending Methods 0.000 description 4
- 239000011575 calcium Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- JLDKGEDPBONMDR-UHFFFAOYSA-N calcium;dioxido(oxo)silane;hydrate Chemical compound O.[Ca+2].[O-][Si]([O-])=O JLDKGEDPBONMDR-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000007731 hot pressing Methods 0.000 description 2
- 230000003100 immobilizing effect Effects 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000005909 Kieselgur Substances 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910021488 crystalline silicon dioxide Inorganic materials 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000004579 marble Substances 0.000 description 1
- 238000013001 point bending Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/18—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing mixtures of the silica-lime type
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/18—Carbonates
- C01F11/185—After-treatment, e.g. grinding, purification, conversion of crystal morphology
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
- C04B28/02—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
- C04B28/10—Lime cements or magnesium oxide cements
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/40—Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Description
【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 よりなる或いはCaCO3 を主
成分とする原料物質を緩やかな処理条件にて固化させ
て、高強度固化体を得る方法に関する。The present invention relates relates to a method of solidifying CaCO 3, in particular, a raw material whose main component is made or CaCO 3 from CaCO 3 and solidified by mild processing conditions, the high strength solidification body Regarding how to get.
【0002】[0002]
【従来の技術及び先行技術】各種産業分野で排出される
排ガス中のCO2 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 Since CO 2 in exhaust gas emitted from various industrial fields is concerned about the influence on global warming, reduction of CO 2 in the atmosphere is being studied. ing.
【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。しかして、固定化されたCaCO
3 や(Ca・Mg)CO3 を固化させて建設・土木材料
等に有効利用する試みがなされている。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 . Then, immobilized CaCO
Attempts have been made to solidify 3 and (Ca · Mg) CO 3 and use them effectively for construction and civil engineering materials.
【0004】CaCO3 の固化方法としては、従来、ホ
ットプレス法又は水熱ホットプレス法などが提案されて
いる。As a method for solidifying CaCO 3 , a hot pressing method, a hydrothermal hot pressing method, etc. have hitherto been proposed.
【0005】しかしながら、従来のCaCO3 の固化方
法は、いずれも天然のCaCO3 固化体である大理石や
石灰石の生成条件に準じた処理条件を必要とするため、
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
り、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。However, since the method of solidifying conventional CaCO 3 in need of treatment conditions both conforming to generate conditions of marble and limestone is CaCO 3 solidification of natural,
Since the processing conditions are severe conditions of high temperature and high pressure and the equipment is complicated, it is not suitable for large-scale processing, energy consumption is large, and processing cost is high.
【0006】上記従来の問題点を解決し、CaCO3 又
はCaCO3 を主成分とする物質を緩やかな条件で固化
する方法として、本出願人は、CaCO3 又はCaCO
3 を主成分とする物質をオートクレーブ反応を利用して
固化させる方法を見出し、先に特許出願をした(特願平
5−209399号。以下「先願」という。)。[0006] The above solves the conventional problems, a material mainly composed of CaCO 3 or CaCO 3 as a method of solidifying under mild conditions, the applicant, CaCO 3 or CaCO
A method for solidifying a substance containing 3 as a main component by utilizing an autoclave reaction was found, and a patent application was previously filed (Japanese Patent Application No. 5-209399, hereinafter referred to as "prior application").
【0007】上記先願のオートクレーブ処理を利用する
方法によれば、従来法に比べて低温、低圧の緩やかな条
件で、CaCO3 又はCaCO3 を主成分とする物質を
固化させることができる。According to the method utilizing the autoclave treatment of the above-mentioned prior application, CaCO 3 or a substance containing CaCO 3 as a main component can be solidified under mild conditions of low temperature and low pressure as compared with the conventional method.
【0008】[0008]
【発明が解決しようとする課題】ところで、このように
して得られる固化体の、各種建設・土木材料等としての
用途を考慮した場合、その強度がより一層高いことが望
まれる。By the way, in consideration of the use of the solidified body thus obtained as various construction and civil engineering materials, it is desired that its strength is much higher.
【0009】本発明は上記先願の方法に従って、CaC
O3 又はCaCO3 を主成分とする物質を固化させるに
当り、得られる固化体の強度を高め、各種用途に有用な
固化体を得る方法を提供することを目的とする。According to the method of the above-mentioned prior application, the present invention provides CaC
An object of the present invention is to provide a method for obtaining a solidified product useful for various purposes by increasing the strength of the solidified product obtained when solidifying a substance containing O 3 or CaCO 3 as a main component.
【0010】[0010]
【課題を解決するための手段】請求項1のCaCO3 の
固化方法は、CaCO3 よりなる或いはCaCO3 を主
成分とする原料物質をオートクレーブ処理することによ
り固化させる方法であって、オートクレーブ処理に先立
って、該原料物質中のCaCO3 の一部がCaOとなる
ように、該原料物質を仮焼しておくことを特徴とする。Means for Solving the Problems The method for solidifying CaCO 3 according to claim 1, consisting of CaCO 3 or raw material to the CaCO 3 as the main component a method of solidifying by autoclaving, autoclaving It is characterized in that the raw material is calcined in advance so that a part of CaCO 3 in the raw material becomes CaO.
【0011】請求項2のCaCO3 の固化方法は、請求
項1の方法において、前記原料物質を仮焼した後、シリ
カ系物質と混合し、その後、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。The method for solidifying CaCO 3 according to claim 2 is the method according to claim 1, wherein the raw material is calcined, mixed with a silica-based material, and then solidified by utilizing an autoclave reaction. And
【0012】以下に本発明を詳細に説明する。なお、以
下において、仮焼前の原料物質中のCaCO3 に対す
る、仮焼後、CaOに転換せずにCaCO3 として残留
するCaCO3 の割合(重量%)を、「CaCO3 残存
率」と称す。The present invention will be described in detail below. In the following, for CaCO 3 of before calcination of the raw materials in, after calcination, the ratio of CaCO 3 remaining as CaCO 3 without converted to CaO (% by weight), referred to as "CaCO 3 residual ratio" .
【0013】本発明のCaCO3 の固化方法において、
原料物質となる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CaC
O3 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 含有量が50%以上のドロ
マイト等)であれば有効に適用することができる。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 CaCO 3 or (Ca · Mg) CO 3 obtained by absorbing CO 2 in combustion exhaust gas into seawater or the like.
Examples thereof include substances obtained by immobilization, but the present invention is not limited to these substances.
A substance containing 50% by weight or more of O 3 or CaCO 3 as a main component (for example, dolomite having a CaCO 3 content of 50% or more) can be effectively applied.
【0014】本発明においては、このような原料物質
を、原料物質中のCaCO3 の一部がCaOとなるよう
に仮焼した後、オートクレーブ処理に供する。原料物質
を仮焼することにより、原料物質中のCaCO3 の一部
がCaCO3 →CaO+CO2の反応で、反応性に富む
CaOとなり、オートクレーブ反応時における反応性が
向上し、固化強度が高められる。In the present invention, such a raw material is calcined so that a part of CaCO 3 in the raw material becomes CaO, and then subjected to an autoclave treatment. By calcining the raw material, a part of CaCO 3 in the raw material reacts with CaCO 3 → CaO + CO 2 to become highly reactive CaO, and the reactivity in the autoclave reaction is improved and the solidification strength is increased. .
【0015】本発明において、原料物質の仮焼の程度
は、CaCO3 残存率が70%以上、特に80〜90%
となるような程度であることが好ましい。In the present invention, the degree of calcination of the raw material is such that the residual rate of CaCO 3 is 70% or more, particularly 80 to 90%.
It is preferable that it is such that
【0016】このCaCO3 残存率が過度に多いと本発
明による固化強度の向上効果が十分に得られず、逆にC
aCO3 残存率が過度に少ないと、CO2 の固定化とい
う所期の目的を達成し得ない。If the CaCO 3 residual rate is excessively high, the effect of improving the solidification strength according to the present invention cannot be sufficiently obtained, and conversely C
If the residual rate of aCO 3 is too small, the intended purpose of immobilizing CO 2 cannot be achieved.
【0017】原料物質をこのようなCaCO3 残存率と
なるように仮焼するには、通常の場合、原料物質を大気
中で700〜800℃の温度で0.1〜5時間程度焼成
すれば良い。In order to calcine the raw material so as to have such a CaCO 3 residual rate, in general, the raw material is calcined in the air at a temperature of 700 to 800 ° C. for about 0.1 to 5 hours. good.
【0018】ところで、本発明においては、このように
して仮焼した原料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SiO
2 ,結晶質SiO2 の他、ケイ砂、キラ微砂、ケイ藻
土、粘土等を用いることができ、この場合には、得られ
る固化体中にC−S−H(ケイ酸カルシウム水和物)が
生成し、固化体の強度を高めることができる。By the way, in the present invention, the silica-based substance may be mixed with the raw material thus calcined and treated. As the silica-based material, amorphous SiO
In addition to 2 , crystalline SiO 2 , silica sand, fine kira sand, diatomaceous earth, clay, etc. can be used. In this case, C--S--H (calcium silicate hydrate) is contained in the obtained solidified body. Substance) is produced, and the strength of the solidified body can be increased.
【0019】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原料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割合は、原料物質に対し
て50重量%以下、特に10〜30重量%とするのが好
ましい。When a silica-based substance is used, if the amount of the silica-based substance used is too large, the ratio of the raw material is relatively reduced and the efficiency of effective utilization due to solidification of CaCO 3 is reduced. The use ratio of the substance is preferably 50% by weight or less, particularly 10 to 30% by weight, based on the raw material.
【0020】本発明においては、原料物質を仮焼後、必
要に応じてシリカ系物質を混合して得られる固化原料
を、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ても良い。In the present invention, the solidified raw material obtained by calcining the raw material and then optionally mixing the silica-based material is desired by a molding method such as press molding, cast molding, extrusion molding or cast molding. After being molded into the shape of, it is autoclaved. The solidified raw material may be subjected to autoclave treatment as it is without performing molding.
【0021】オートクレーブ処理は、100〜300
℃、特に150〜200℃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 100 to 300.
Saturated vapor pressure (40 kg
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.
【0022】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.
【0023】[0023]
【作用】オートクレーブ処理によれば、従来法に比べて
低温、低圧の緩やかな条件で、CaCO3 よりなる或い
はCaCO3 を主成分とする原料物質を固化させること
ができるが、このオートクレーブ処理による固化に先立
ち、原料物質を仮焼してCaCO3 の一部を反応性の高
いCaOに転換しておくことにより、オートクレーブ反
応時の反応性が向上し、固化強度を高めることができ
る。SUMMARY OF According to autoclaving, the low temperature as compared with the conventional method, a low pressure of mild conditions, but the made or CaCO 3 from CaCO 3 can be solidified raw material whose main component, solidified by the autoclaving Prior to the above, by calcining the raw material and converting a part of CaCO 3 into highly reactive CaO, the reactivity during the autoclave reaction is improved and the solidification strength can be increased.
【0024】また、仮焼後の原料物質にシリカ系物質を
混合した場合には、C−S−Hが生成し、得られる固化
体の強度をより一層高めることができる。When a silica-based material is mixed with the raw material after calcination, C--S--H is produced, and the strength of the obtained solidified product can be further enhanced.
【0025】[0025]
【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。EXAMPLES The present invention will be described in more detail with reference to the following examples.
【0026】実施例1〜8 CaCO3 (平均粒径80μmの石灰石)を表1に示す
条件で表1に示すCaCO3 残存率となるように仮焼し
た後、この仮焼後のCaCO3 にSiO2 (平均粒径5
μmの石英)を、仮焼CaCO3 :SiO2 =80:2
0(重量%)の割合で乾式混合し、一軸加圧成形(10
%含水)して40mm×10mm×約10mm厚さの成
形体を得た。得られた成形体をオートクレーブに入れ、
表1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30
0cc入れて飽和蒸気圧にて処理した。Examples 1 to 8 CaCO 3 (limestone having an average particle size of 80 μm) was calcined under the conditions shown in Table 1 so that the CaCO 3 residual rate shown in Table 1 was obtained, and then the CaCO 3 after this calcination was changed. SiO 2 (average particle size 5
(μm quartz) is calcined CaCO 3 : SiO 2 = 80: 2
Dry mixing at a ratio of 0 (% by weight), uniaxial pressure molding (10
% Water) to obtain a molded product having a thickness of 40 mm × 10 mm × about 10 mm. Put the obtained molded body in an autoclave,
It was treated and solidified under the conditions shown in Table 1. Distilled water was added to the container (2000 cc capacity) of the autoclave.
It was charged with 0 cc and treated at a saturated vapor pressure.
【0027】得られた固化体を80℃で1日乾燥した
後、曲げ強度の測定を行ない結果を表1に示した。な
お、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/minの3点曲げ強度測定
条件で行なった。The obtained solidified product was dried at 80 ° C. for 1 day, and the bending strength was measured. The results are shown in Table 1. The bending strength was measured under three-point bending strength measurement conditions with a span distance of 30 mm and a crosshead speed of 0.5 mm / min.
【0028】比較例1 実施例1において、CaCO3 の仮焼を行わなかったこ
と以外は同様にして固化体を得、その曲げ強度の測定結
果を表1に示した。Comparative Example 1 A solidified body was obtained in the same manner as in Example 1 except that CaCO 3 was not calcined, and the bending strength measurement results are shown in Table 1.
【0029】比較例2 仮焼していないCaCO3 に、CaOとSiO2 を添加
混合することにより、実施例5における固化原料と同組
成のCaCO3 −CaO−SiO2 原料を調合し、この
原料を用いて、実施例5と同様にして固化体を得、その
曲げ強度の測定結果を表1に示した。Comparative Example 2 A CaCO 3 -CaO-SiO 2 raw material having the same composition as the solidified raw material in Example 5 was prepared by adding CaO and SiO 2 to CaCO 3 which was not calcined, and this raw material was mixed. Was used in the same manner as in Example 5 to obtain a solidified body, and the bending strength measurement results are shown in Table 1.
【0030】なお、成形圧は、実施例と比較例で成形体
の嵩密度が約1.95になるよう300〜900kgf
/cm2 で変化させた。The molding pressure is 300 to 900 kgf so that the bulk density of the molded body is about 1.95 in Examples and Comparative Examples.
/ Cm 2 It was changed.
【0031】[0031]
【表1】 [Table 1]
【0032】表1より明らかなように、本発明によれ
ば、CaCO3 をオートクレーブ処理して高強度固化体
を得ることができる。As is clear from Table 1, according to the present invention, CaCO 3 can be autoclaved to obtain a high-strength solidified body.
【0033】なお、本発明による強度向上効果は原料物
質を仮焼してCaCO3 の一部をCaOに転換すること
により達成されるものであり、実施例5と比較例2の結
果から明らかなように、CaCO3 にCaOを外部から
添加混合した場合以上の強度向上効果が達成される。The strength improving effect of the present invention is achieved by calcining the raw material and converting a part of CaCO 3 into CaO, which is clear from the results of Example 5 and Comparative Example 2. As described above, the strength improving effect more than the case of adding CaO to CaCO 3 from the outside and mixing is achieved.
【0034】[0034]
【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
ブによる処理のみで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て、高強度固化体を得ることが
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 only by treatment with an autoclave which is a general apparatus. A high-strength solidified body can be obtained, and energy saving and cost saving in the CaCO 3 solidifying technology can be achieved.
【0035】本発明によれば、燃焼排ガス中のCO2 を
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.
Claims (2)
主成分とする原料物質をオートクレーブ処理することに
より固化させる方法であって、 オートクレーブ処理に先立って、該原料物質中のCaC
O3 の一部がCaOとなるように、該原料物質を仮焼し
ておくことを特徴とするCaCO3 の固化方法。1. A consisting CaCO 3 or raw material to the CaCO 3 as the main component a method of solidifying by autoclaving, prior to autoclaving, CaC in raw material substance
A method for solidifying CaCO 3 , characterized in that the raw material is calcined so that a part of O 3 becomes CaO.
を仮焼した後、シリカ系物質と混合し、その後、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. The method according to claim 1, wherein the raw material is calcined, mixed with a silica-based material, and then solidified using an autoclave reaction.
Solidification method of aCO 3 .
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21868194A JP3632222B2 (en) | 1994-09-13 | 1994-09-13 | CaCO3 solidification method |
| DE19523324A DE19523324C2 (en) | 1994-09-13 | 1995-06-27 | Process for making a solidified product |
| NL1001134A NL1001134C2 (en) | 1994-09-13 | 1995-09-05 | Method for hardening CaCO3. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21868194A JP3632222B2 (en) | 1994-09-13 | 1994-09-13 | CaCO3 solidification method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0881217A true JPH0881217A (en) | 1996-03-26 |
| JP3632222B2 JP3632222B2 (en) | 2005-03-23 |
Family
ID=16723756
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21868194A Expired - Fee Related JP3632222B2 (en) | 1994-09-13 | 1994-09-13 | CaCO3 solidification method |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP3632222B2 (en) |
| DE (1) | DE19523324C2 (en) |
| NL (1) | NL1001134C2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006075717A (en) * | 2004-09-09 | 2006-03-23 | Nippon Steel Corp | How to use carbon dioxide |
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| DE19854768A1 (en) * | 1998-11-27 | 2000-05-31 | Wolff Walsrode Ag | Process for the production of mineral moldings |
| US7753618B2 (en) | 2007-06-28 | 2010-07-13 | Calera Corporation | Rocks and aggregate, and methods of making and using the same |
| AU2008270034B2 (en) | 2007-06-28 | 2009-07-16 | Arelac, Inc. | Desalination methods and systems that include carbonate compound precipitation |
| US7754169B2 (en) | 2007-12-28 | 2010-07-13 | Calera Corporation | Methods and systems for utilizing waste sources of metal oxides |
| CA2652803A1 (en) | 2007-12-28 | 2009-06-28 | Calera Corporation | Methods of sequestering co2 |
| US7749476B2 (en) | 2007-12-28 | 2010-07-06 | Calera Corporation | Production of carbonate-containing compositions from material comprising metal silicates |
| US20100239467A1 (en) | 2008-06-17 | 2010-09-23 | Brent Constantz | Methods and systems for utilizing waste sources of metal oxides |
| MX2010012947A (en) * | 2008-05-29 | 2011-04-27 | Calera Corp | Rocks and aggregate, and methods of making and using the same. |
| CN101910469A (en) | 2008-07-16 | 2010-12-08 | 卡勒拉公司 | Co2 utilization in electrochemical systems |
| JP2011528405A (en) | 2008-07-16 | 2011-11-17 | カレラ コーポレイション | Low energy 4-cell electrochemical system using carbon dioxide gas |
| US7993500B2 (en) | 2008-07-16 | 2011-08-09 | Calera Corporation | Gas diffusion anode and CO2 cathode electrolyte system |
| EP2338136A1 (en) | 2008-09-11 | 2011-06-29 | Calera Corporation | Co2 commodity trading system and method |
| US8869477B2 (en) | 2008-09-30 | 2014-10-28 | Calera Corporation | Formed building materials |
| US7939336B2 (en) | 2008-09-30 | 2011-05-10 | Calera Corporation | Compositions and methods using substances containing carbon |
| WO2010039903A1 (en) | 2008-09-30 | 2010-04-08 | Calera Corporation | Co2-sequestering formed building materials |
| US7815880B2 (en) | 2008-09-30 | 2010-10-19 | Calera Corporation | Reduced-carbon footprint concrete compositions |
| EP2203241A4 (en) | 2008-10-31 | 2011-01-12 | Calera Corp | NON-CEMENTIC COMPOSITIONS COMPRISING CO2-SEPARATING ADDITIVES |
| US9133581B2 (en) | 2008-10-31 | 2015-09-15 | Calera Corporation | Non-cementitious compositions comprising vaterite and methods thereof |
| BRPI0823394A2 (en) | 2008-12-23 | 2015-06-16 | Calera Corp | Low Energy Hydroxide Electrochemical System and Method |
| EP2245215A4 (en) | 2009-02-10 | 2011-04-27 | Calera Corp | Low-voltage alkaline production using hydrogen and electrocatlytic electrodes |
| EP2250127A4 (en) | 2009-03-02 | 2011-04-06 | Calera Corp | Gas stream multi-pollutants control systems and methods |
| WO2010104989A1 (en) | 2009-03-10 | 2010-09-16 | Calera Corporation | Systems and methods for processing co2 |
| US7993511B2 (en) | 2009-07-15 | 2011-08-09 | Calera Corporation | Electrochemical production of an alkaline solution using CO2 |
| EP2540684A1 (en) * | 2011-06-30 | 2013-01-02 | L'AIR LIQUIDE, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Porous silica and portlandite material for lining insulation bricks with controlled structure and associated manufacturing method |
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| JPH07267757A (en) * | 1994-03-31 | 1995-10-17 | Agency Of Ind Science & Technol | Method for solidifying calcium carbonate and/or magnesium carbonate |
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| FR563545A (en) * | 1922-06-08 | 1923-12-07 | Artificial limestone and its manufacturing process | |
| DE1646416B1 (en) * | 1967-08-25 | 1970-04-16 | Battelle Institut E V | Process for the production of hydrothermally hardened building materials and components |
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1994
- 1994-09-13 JP JP21868194A patent/JP3632222B2/en not_active Expired - Fee Related
-
1995
- 1995-06-27 DE DE19523324A patent/DE19523324C2/en not_active Expired - Fee Related
- 1995-09-05 NL NL1001134A patent/NL1001134C2/en not_active IP Right Cessation
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|---|---|---|---|---|
| JPS51102021A (en) * | 1975-03-05 | 1976-09-09 | Masayoshi Aoki | SETSUKAISEKIFUNGANJUDEIJOBUTSUSHORIHOHO |
| JPH03164459A (en) * | 1989-11-22 | 1991-07-16 | Denki Kagaku Kogyo Kk | Production of lined pipe |
| JPH0761842A (en) * | 1993-08-24 | 1995-03-07 | Inax Corp | Solidification of caco3 |
| JPH07267698A (en) * | 1994-03-31 | 1995-10-17 | Agency Of Ind Science & Technol | Method for solidifying caco3 |
| JPH07267757A (en) * | 1994-03-31 | 1995-10-17 | Agency Of Ind Science & Technol | Method for solidifying calcium carbonate and/or magnesium carbonate |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006075717A (en) * | 2004-09-09 | 2006-03-23 | Nippon Steel Corp | How to use carbon dioxide |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3632222B2 (en) | 2005-03-23 |
| NL1001134A1 (en) | 1996-03-13 |
| NL1001134C2 (en) | 1997-05-13 |
| DE19523324C2 (en) | 1999-07-01 |
| DE19523324A1 (en) | 1996-03-14 |
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