JPH06340417A - Production of zeolite composition - Google Patents
Production of zeolite compositionInfo
- Publication number
- JPH06340417A JPH06340417A JP12697193A JP12697193A JPH06340417A JP H06340417 A JPH06340417 A JP H06340417A JP 12697193 A JP12697193 A JP 12697193A JP 12697193 A JP12697193 A JP 12697193A JP H06340417 A JPH06340417 A JP H06340417A
- Authority
- JP
- Japan
- Prior art keywords
- coal ash
- zeolite
- mixture
- alkaline component
- composition
- 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
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、石炭を原料としたゼ
オライト組成物の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a zeolite composition using coal as a raw material.
【0002】[0002]
【従来の技術】電力需要の増大とエネルギーコスト低減
のため、石炭焚ボイラによる発電は今後増大していくこ
とが予想されている。石炭中には未燃の灰分が多少なり
とも含まれており、これが燃焼したあと石炭灰(フライ
アッシュ)として残る。石炭焚発電所の増加に伴って排
出される石炭灰も多量なものとなり、その処理が社会的
な問題となっている。2. Description of the Related Art Power generation by a coal-fired boiler is expected to increase in the future due to an increase in power demand and a reduction in energy cost. Coal contains some unburned ash, which remains as fly ash after burning. With the increase in the number of coal-fired power plants, the amount of coal ash emitted becomes large, and the treatment of the ash becomes a social problem.
【0003】石炭灰は現在海上あるいは陸上での埋立や
セメントの原料として主に用いられている。その他の利
用としては無水石コウとの配合による硬化体を得る方法
(特開昭53−27619号)も示されている。また、
特開昭64−24014号,特開平2−221114号
には、石炭灰を原料に、より付加価値の高いゼオライト
を合成する方法が示されている。At present, coal ash is mainly used as a raw material for landfill or cement at sea or on land. As another use, a method of obtaining a hardened product by blending with anhydrous gypsum (JP-A-53-27619) is also shown. Also,
Japanese Unexamined Patent Publication No. 64-24014 and Japanese Unexamined Patent Publication No. 2-221114 disclose methods for synthesizing zeolite having a higher added value using coal ash as a raw material.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、従来技
術によれば、石炭灰の組成によっては必ずしも十分なゼ
オライト化ができず、特に石炭灰中のAl2 O3 が結晶
質のムライトとして存在する場合にはゼオライト化が進
行しにくい。However, according to the prior art, depending on the composition of the coal ash, sufficient zeolite formation is not always possible, and particularly when Al 2 O 3 in the coal ash exists as crystalline mullite. It is difficult for zeolite to progress.
【0005】この発明はこうした事情を考慮してなされ
たもので、従来と比べ、ゼオライト化しにくい石炭灰も
十分なゼオライト化が可能であり、石炭灰の種類に関係
なく付加価値の高いゼオライトを合成することができる
ゼオライト組成物の製造方法を提供することを目的とす
る。The present invention has been made in view of these circumstances. Compared with the prior art, coal ash that is difficult to be made into zeolite can be sufficiently made into zeolite, and a zeolite with high added value can be synthesized regardless of the type of coal ash. It is an object of the present invention to provide a method for producing a zeolite composition that can be used.
【0006】[0006]
【課題を解決するための手段】この発明は、石炭灰とN
a2 CO3 ,NaOH,K2 CO3 ,KOHの中の少な
くとも一種以上のアルカリ成分を混合し、更にこの混合
物を加熱溶融させた後、加熱処理することを特徴とする
ゼオライト組成物の製造方法である。This invention is directed to coal ash and N
a 2 CO 3, NaOH, mixed K 2 CO 3, at least one kind of alkaline components in the KOH, after further heating and melting the mixture, the manufacturing method of the zeolite composition, characterized in that the heat treatment Is.
【0007】この発明において、アルカリ成分の混合量
は石炭灰中のSiO2 含有量に対してモル比で0.5〜
1.5が好ましく、加熱溶融温度が1000℃以上であ
ることが好ましい。In the present invention, the amount of the alkaline component mixed is 0.5 to 0.5 in terms of molar ratio with respect to the SiO 2 content in the coal ash.
1.5 is preferable, and the heating and melting temperature is preferably 1000 ° C. or higher.
【0008】[0008]
【作用】この発明によれば、石炭灰中のAl2 O3 ,S
iO2 がムライトやα−石英などの結晶としてどのよう
な割合で存在しても、十分なゼオライト化が進行する。
この理由は、予め石炭灰をNa2 O3 などのアルカリ成
分と混合溶融することによって、石炭灰中に存在するム
ライト,α−成分などの結晶が消失し、ゼオライト化が
進行し易い霞石,カーネギー石等の鉱物に変化するため
と思われる。According to the present invention, Al 2 O 3 , S in coal ash is
Regardless of the proportion of iO 2 present as crystals of mullite, α-quartz, etc., sufficient zeolite formation proceeds.
The reason for this is that by mixing and melting coal ash with an alkaline component such as Na 2 O 3 in advance, crystals such as mullite and α-component existing in the coal ash disappear, and nepheline which easily undergoes zeolite formation, It is thought to be due to the change to minerals such as Carnegie stone.
【0009】[0009]
【実施例】以下、この発明の実施例について説明する。 (実施例1〜3)石炭焚ボイラから採取した下記「表
1」の化学組成の石炭灰30gにNa2 CO3 を各々1
7.6g,35.2g,52.8g加えて混合し、電気
炉内で1000℃×1時間溶融した。その後、溶融物を
冷却粉砕し水をH2 O/Na2 Oモル比で50になるよ
うに加え、オートクレーブ内で100℃×24時間加熱
処理を行った。処理後の生成物を濾過,水洗,乾燥し、
ゼオライト組成物A(実施例1),ゼオライト組成物B
(実施例2),ゼオライト組成物C(実施例3)を得
た。Embodiments of the present invention will be described below. (Examples 1 to 3) 1 g of Na 2 CO 3 was added to 30 g of coal ash having the chemical composition shown in the following “Table 1” collected from a coal-fired boiler.
7.6g, 35.2g, 52.8g were added and mixed, and it melted at 1000 degreeC x 1 hour in an electric furnace. Then, the melt was cooled and ground, water was added so that the H 2 O / Na 2 O molar ratio was 50, and heat treatment was carried out at 100 ° C. for 24 hours in an autoclave. The product after the treatment is filtered, washed with water and dried,
Zeolite composition A (Example 1), zeolite composition B
(Example 2) and a zeolite composition C (Example 3) were obtained.
【0010】[0010]
【表1】 [Table 1]
【0011】(比較例)表1の石炭灰30gを3NのN
aOH300mlに投入し、オートクレーブ内で3Kg/
cm2 の圧力になるように加熱し5時間処理した。処理後
の生成物を濾過,水洗,乾燥し、ゼオライト組成物Dを
得た。(Comparative Example) 30 g of coal ash shown in Table 1 was mixed with 3N N
Add to 300ml aOH, 3kg / in autoclave
It was heated to a pressure of cm 2 and treated for 5 hours. The treated product was filtered, washed with water and dried to obtain a zeolite composition D.
【0012】実施例1〜3及び比較例1で得られたゼオ
ライト組成物A,B,C,Dについてその鉱物組成をX
線回折によって同定した。X線回折パターンを図1〜図
4に示した。ここで、図1〜図4において、横軸は回折
角2θ(゜)であり、縦軸は回折X線強度(cps:co
unt per second)である。また、図中のムライト,α−
SiO2 (石英)は石炭灰にもともと含まれる鉱物種で
ある。また、NH4 Cl水溶液を用いてNH4 + イオン
交換を行い、ゼオライト組成物A,B,C,Dのイオン
交換容量( meq/g )を求めた。その結果を、下記「表
2」に示す。The mineral compositions of the zeolite compositions A, B, C and D obtained in Examples 1 to 3 and Comparative Example 1 were X.
It was identified by line diffraction. The X-ray diffraction patterns are shown in FIGS. Here, in FIGS. 1 to 4, the horizontal axis represents the diffraction angle 2θ (°) and the vertical axis represents the diffraction X-ray intensity (cps: co).
unt per second). In addition, mullite in the figure, α-
SiO 2 (quartz) is a mineral species originally contained in coal ash. Also performs NH 4 + ion exchanged with aqueous NH 4 Cl, zeolite compositions A, B, C, an ion exchange capacity of D a (meq / g) was determined. The results are shown in "Table 2" below.
【0013】[0013]
【表2】 [Table 2]
【0014】図1〜図4により、比較例のゼオライト組
成物Dにはムライトやα−SiO2が残存しているが、
実施例1,2,3のゼオライト組成物A,B,Cにはそ
れは見られず、ガロナイト,アナルサイムなどのゼオラ
イトがよく生成している。また、表2より、実施例1,
2,3のゼオライト組成物A,B,Cは比較例のゼオラ
イト組成物に比べて大きなイオン交換容量があり、優れ
ていることが分かる。1 to 4, mullite and α-SiO 2 remain in the zeolite composition D of the comparative example.
This is not seen in the zeolite compositions A, B, and C of Examples 1, 2, and 3, and zeolites such as gallonite and analcime are often formed. In addition, from Table 2, Example 1,
It can be seen that the few zeolite compositions A, B, and C have a larger ion exchange capacity than the zeolite compositions of the comparative examples, and are excellent.
【0015】[0015]
【発明の効果】以上詳述したようにこの発明によれば、
従来と比べ、ゼオライト化しにくい石炭灰も十分なゼオ
ライト化が可能であり、石炭灰の種類に関係なく付加価
値の高いゼオライトを合成することができる有益なゼオ
ライト組成物の製造方法を提供できる。As described above in detail, according to the present invention,
It is possible to provide sufficient zeolite-forming for coal ash that is difficult to form into zeolite as compared with the conventional one, and it is possible to provide a method for producing a useful zeolite composition capable of synthesizing high-value-added zeolite regardless of the type of coal ash.
【図1】この発明の実施例1に係るゼオライト組成物の
X線回折パターンの特性図。FIG. 1 is a characteristic diagram of an X-ray diffraction pattern of a zeolite composition according to Example 1 of the present invention.
【図2】この発明の実施例2に係るゼオライト組成物の
X線回折パターンの特性図。FIG. 2 is a characteristic diagram of an X-ray diffraction pattern of the zeolite composition according to Example 2 of the present invention.
【図3】この発明の実施例3に係るゼオライト組成物の
X線回折パターンの特性図。FIG. 3 is a characteristic diagram of an X-ray diffraction pattern of the zeolite composition according to Example 3 of the present invention.
【図4】従来に係るゼオライト組成物のX線回折パター
ンの特性図。FIG. 4 is a characteristic diagram of an X-ray diffraction pattern of a conventional zeolite composition.
Claims (2)
CO3 ,KOHの中の少なくとも一種以上のアルカリ成
分を混合し、更にこの混合物を加熱溶融させた後、加熱
処理することを特徴とするゼオライト組成物の製造方
法。1. Coal ash and Na 2 CO 3 , NaOH, K 2
A method for producing a zeolite composition, which comprises mixing at least one alkaline component selected from CO 3 and KOH, heating and melting the mixture, and then heat-treating the mixture.
O2 含有量に対してモル比で0.5〜1.5であり、か
つ加熱溶融温度が1000℃以上である請求項1記載の
ゼオライト組成物の製造方法。2. The amount of alkali components mixed in the coal ash is Si.
The method for producing a zeolite composition according to claim 1, wherein the molar ratio to the O 2 content is 0.5 to 1.5, and the heating and melting temperature is 1000 ° C or higher.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12697193A JP3442817B2 (en) | 1993-05-28 | 1993-05-28 | Method for producing zeolite composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12697193A JP3442817B2 (en) | 1993-05-28 | 1993-05-28 | Method for producing zeolite composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06340417A true JPH06340417A (en) | 1994-12-13 |
JP3442817B2 JP3442817B2 (en) | 2003-09-02 |
Family
ID=14948432
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12697193A Expired - Fee Related JP3442817B2 (en) | 1993-05-28 | 1993-05-28 | Method for producing zeolite composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3442817B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6027708A (en) * | 1998-09-08 | 2000-02-22 | Council Of Scientific & Industrial Research | Process for the synthesis of flyash based zeolite-Y |
JP2007131502A (en) * | 2005-11-14 | 2007-05-31 | Takamasa Wajima | Method for manufacturing zeolite |
WO2019202933A1 (en) | 2018-04-16 | 2019-10-24 | 旭化成株式会社 | Gis-type zeolite |
US10646847B2 (en) | 2016-12-13 | 2020-05-12 | Asahi Kasei Kabushiki Kaisha | GIS-type zeolite |
WO2022025247A1 (en) | 2020-07-31 | 2022-02-03 | 旭化成株式会社 | Gis-type zeolite |
WO2023067841A1 (en) | 2021-10-22 | 2023-04-27 | 旭化成株式会社 | Gis-type zeolite, adsorbent, and separation method |
WO2023067840A1 (en) | 2021-10-22 | 2023-04-27 | 旭化成株式会社 | Gis-type zeolite, adsorbent, and separation method |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109705918B (en) * | 2017-10-25 | 2021-12-17 | 中国石油化工股份有限公司 | Composite fluxing agent for improving fusion characteristics of coal ash and preparation method and application thereof |
-
1993
- 1993-05-28 JP JP12697193A patent/JP3442817B2/en not_active Expired - Fee Related
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6027708A (en) * | 1998-09-08 | 2000-02-22 | Council Of Scientific & Industrial Research | Process for the synthesis of flyash based zeolite-Y |
JP2007131502A (en) * | 2005-11-14 | 2007-05-31 | Takamasa Wajima | Method for manufacturing zeolite |
US10646847B2 (en) | 2016-12-13 | 2020-05-12 | Asahi Kasei Kabushiki Kaisha | GIS-type zeolite |
WO2019202933A1 (en) | 2018-04-16 | 2019-10-24 | 旭化成株式会社 | Gis-type zeolite |
US10829383B2 (en) | 2018-04-16 | 2020-11-10 | Asahi Kasei Kabushiki Kaisha | GIS-type zeolite |
WO2022025247A1 (en) | 2020-07-31 | 2022-02-03 | 旭化成株式会社 | Gis-type zeolite |
WO2023067841A1 (en) | 2021-10-22 | 2023-04-27 | 旭化成株式会社 | Gis-type zeolite, adsorbent, and separation method |
WO2023067840A1 (en) | 2021-10-22 | 2023-04-27 | 旭化成株式会社 | Gis-type zeolite, adsorbent, and separation method |
KR20240037332A (en) | 2021-10-22 | 2024-03-21 | 아사히 가세이 가부시키가이샤 | GIS-type zeolite, adsorbent, and separation method |
KR20240052855A (en) | 2021-10-22 | 2024-04-23 | 아사히 가세이 가부시키가이샤 | GIS type zeolite, adsorbent and separation method |
Also Published As
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---|---|
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