JPH03252310A - Method for purifying natural zeolite - Google Patents
Method for purifying natural zeoliteInfo
- Publication number
- JPH03252310A JPH03252310A JP4887790A JP4887790A JPH03252310A JP H03252310 A JPH03252310 A JP H03252310A JP 4887790 A JP4887790 A JP 4887790A JP 4887790 A JP4887790 A JP 4887790A JP H03252310 A JPH03252310 A JP H03252310A
- Authority
- JP
- Japan
- Prior art keywords
- zeolite
- tuff
- swelling clay
- clay mineral
- ore
- 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
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 53
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 53
- 239000010457 zeolite Substances 0.000 title claims abstract description 53
- 238000000034 method Methods 0.000 title claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 230000008961 swelling Effects 0.000 claims abstract description 12
- 239000002734 clay mineral Substances 0.000 claims abstract description 11
- 239000013078 crystal Substances 0.000 claims abstract description 10
- 239000000843 powder Substances 0.000 claims abstract description 9
- 238000005065 mining Methods 0.000 claims abstract description 4
- 239000002245 particle Substances 0.000 claims description 21
- JYIBXUUINYLWLR-UHFFFAOYSA-N aluminum;calcium;potassium;silicon;sodium;trihydrate Chemical compound O.O.O.[Na].[Al].[Si].[K].[Ca] JYIBXUUINYLWLR-UHFFFAOYSA-N 0.000 claims description 7
- 229910001603 clinoptilolite Inorganic materials 0.000 claims description 7
- 238000007670 refining Methods 0.000 claims description 2
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 abstract description 9
- 229910052901 montmorillonite Inorganic materials 0.000 abstract description 9
- 238000010298 pulverizing process Methods 0.000 abstract description 6
- 230000002522 swelling effect Effects 0.000 abstract description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 2
- 239000011707 mineral Substances 0.000 abstract description 2
- 238000007598 dipping method Methods 0.000 abstract 1
- 239000012535 impurity Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 3
- 238000005341 cation exchange Methods 0.000 description 2
- 239000011362 coarse particle Substances 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001493 electron microscopy Methods 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Description
【発明の詳細な説明】 〈産業上の利用分野〉 この発明は天然ゼオライトの精製方法に関する。[Detailed description of the invention] <Industrial application field> This invention relates to a method for purifying natural zeolite.
〈従来の技術〉
一般にゼオライトは浄水作用、脱臭作用、ガス吸着作用
の他触媒等とし、でも用いられるが、コスト及び量産性
の面から人工ゼオライトよりも天然ゼオライトの使用が
望まれている。しかし天然ゼオライトは鉱物資源である
ため多量の不純物を含み、純度が低いので期待される各
種の作用が不十分という問題がある。<Prior Art> Generally, zeolite is used for water purification, deodorization, gas adsorption, and as a catalyst, but from the viewpoint of cost and mass production, the use of natural zeolite is preferred over artificial zeolite. However, since natural zeolite is a mineral resource, it contains a large amount of impurities and has a low purity, so there is a problem that various expected effects are insufficient.
一方、従来の天然ゼオライトの精製には乾式法と湿式法
があり、前者は採掘後粉砕分級して硬度の高い石英質等
の不純物の一部を除去するもので、その純度は原鉱の純
度(約60〜70%)と大差がない。On the other hand, there are two conventional methods for refining natural zeolite: a dry method and a wet method. (approximately 60-70%), there is not much difference.
また後者の湿式法においては、採鉱後のものを例えば1
5xx以下の粒度に粉砕したものをさらにボールミル等
を使って機械的に湿式粉砕し、粗分級、下流排出物の機
械的再粉砕、上流排出物遠心分級、粗粒の二次粉砕、二
次分級、極微粒子を不純物として除去、化学的処理を施
して再固化し、再砕解せしめて粉末状にする等の方法が
知られている。In the latter wet method, for example, 1
After being crushed to a particle size of 5xx or less, it is further mechanically wet-pulverized using a ball mill, etc., followed by coarse classification, mechanical re-grinding of downstream waste, centrifugal classification of upstream waste, secondary crushing of coarse particles, and secondary classification. There are known methods such as removing ultrafine particles as impurities, resolidifying them by chemical treatment, and crushing them again to form a powder.
〈発明が解決しようとする課題〉
しかし上記の方法中、乾式法では上述のように高純度の
ゼオライトは期待できず、一方の湿式法では原鉱純度7
0%のもので80%以上の純度のゼオライトが得られた
との報告があるが、これはX線分析によるピーク高の比
較による推定値であり、これより正確な測定が可能な陽
イオン交換容量に基く測定では、原鉱より僅かに良いか
殆ど変わらない程度の値しか得られない。また、上記方
法は極めて限定された実験精製の域を出ないだけでなく
、精製工程が多く且つ複雑で作業能率やコスト面でも実
用的ではない。特に原鉱中に含まれる長石その他ガラス
質のものをすべて微粉末に粉砕混合したものからゼオラ
イト分のみを機械的に分離回収することは極めて困難若
しくは不可能である。<Problem to be solved by the invention> However, among the above methods, the dry method cannot be expected to produce zeolite with high purity as mentioned above, while the wet method produces raw ore with a purity of 7.
There are reports that zeolite with a purity of 80% or more was obtained with 0% zeolite, but this is an estimate based on a comparison of peak heights by X-ray analysis, and the cation exchange capacity can be measured more accurately. Measurements based on this result in values that are only slightly better or almost the same as those of the raw ore. Moreover, the above method not only goes beyond the scope of extremely limited experimental purification, but also involves many purification steps and is complicated, making it impractical in terms of work efficiency and cost. In particular, it is extremely difficult or impossible to mechanically separate and recover only the zeolite component from a mixture of all the feldspar and other glassy substances contained in the raw ore that have been pulverized and mixed into fine powder.
〈課題を解決するための手段〉
上記問題点を解決するための本悌明の方法は、膨潤性粘
土鉱物を含有するゼオライト含凝灰岩を、採掘後にゼオ
ライトの結晶を破壊しない程度に粉砕した後水中に浸漬
し、上記膨潤性粘土鉱物を膨潤させることによって前記
凝灰岩を微粉状態に砕解せしめ、砕解した微粉を分級し
てゼオライト結晶粒が最も高密度に分布する所定範囲の
粒度のもののみを回収して高純度ゼオライトを得るもの
で、本方法ではゼオライト原鉱の粉砕工程における機械
的粉砕を必要最小限に留め、特に粉砕化の最終工程では
モンモリロナイトの膨潤作用だけでゼオライト鉱石粒の
粉砕化を行うことを特徴としている。<Means for solving the problem>Hontemei's method for solving the above problem is to crush zeolite-containing tuff containing swelling clay minerals to an extent that does not destroy the zeolite crystals after mining, and then submerge the zeolite-containing tuff in water. The tuff is pulverized into a fine powder by immersing it in water and swelling the swellable clay mineral, and the crushed tuff is classified to select only those with a particle size within a predetermined range in which zeolite crystal grains are most densely distributed. High-purity zeolite is obtained by recovering the zeolite, and in this method, the mechanical crushing in the pulverizing process of the zeolite ore is kept to the minimum necessary, and in particular, in the final process of pulverizing, the zeolite ore particles are crushed only by the swelling action of montmorillonite. It is characterized by doing the following.
また上記膨潤性粘土鉱物がモンモリロナイトであり、ゼ
オライト含凝灰岩がクリノプチロライト含凝灰岩である
ことを第2の特徴としている。The second feature is that the swelling clay mineral is montmorillonite, and the zeolite-containing tuff is clinoptilolite-containing tuff.
〈作 用〉
本発明においては、鉱石中にモンモリロナイト等の膨潤
性粘土鉱物を浸漬時の水分により膨潤させることによっ
て鉱石を砕解するので、ゼオライトはその結晶状態のま
ま水中に分散するとともに他の不純物も機械的な微破砕
を受けないので比較的大きい粒度のまま分散するものと
極小微粒子として分散するものとに分れる。その結果極
小微粒子と比較的大粒子の微粉体の中間にあって、ゼオ
ライト結晶粒が最も高密度に分布する粒径範囲を分級回
収すれば高純度の天然ゼオライトが得られる。<Function> In the present invention, the ore is crushed by swelling swelling clay minerals such as montmorillonite in the ore with water during immersion, so the zeolite is dispersed in water in its crystalline state and other Since impurities are not subjected to mechanical pulverization, they are divided into those that are dispersed as relatively large particles and those that are dispersed as extremely small particles. As a result, highly pure natural zeolite can be obtained by classifying and collecting the particle size range in which zeolite crystal grains are most densely distributed, which is between extremely small particles and relatively large particles.
〈実施例〉
以下本発明の実施例につき詳述すると、この例では島根
県産のゼオライト原鉱を使用し、クリノプチロライト含
有率約60%〜70%、モンモリロナイトが重量比約l
O%前後含まれているものを使用した。<Example> Hereinafter, an example of the present invention will be described in detail. In this example, zeolite raw ore from Shimane Prefecture is used, the clinoptilolite content is about 60% to 70%, and the weight ratio of montmorillonite is about 1
The one containing around 0% was used.
ゼオライト原鉱採掘後、含水率約3%位に乾燥し、クラ
ッシャー等により5xm以下の粒径に粉砕して3〜53
11の粒径のものを分級採取した。但し、粒径の分級は
実験の設定条件として定めたもので、処理自体には3m
m以下のものを含んでいてもよい。After mining the zeolite raw ore, it is dried to a moisture content of about 3% and crushed to a particle size of 5xm or less using a crusher etc.
Particles with a particle size of 11 were classified and collected. However, the particle size classification was determined as the experimental setting conditions, and the treatment itself
It may contain less than m.
次いでボールミル内には鉱石粒の機械的粉砕を避けるた
めにボールを混入しないで、鉱石量に対する重量比5倍
程度の水を加えて浸漬状態とし、上記ボールミルを約2
0時間前後駆動させる。この時使用したボールミルは容
量IQのもであるが、このボールミルの容量が大きい場
合は上記原鉱の粉砕粒径や分級粒度は5mm以下である
必要はない。Next, in order to avoid mechanical crushing of the ore grains, no balls were mixed into the ball mill, and water was added in an amount of about 5 times the weight of the ore to create an immersed state.
Drive around 0 hours. The ball mill used at this time has a capacity of IQ, but if the capacity of this ball mill is large, the crushed particle size and classified particle size of the raw ore need not be 5 mm or less.
上記処理によりゼオライト鉱石(#灰岩)は、含有され
るモンモリロナイトが多量の水を含んで膨潤し、粗粒を
含む微粉末に崩壊する。ちなみにモンモリロナイトは粘
土質であって水によって7〜IO倍の体積に膨潤するこ
とが知られており、クリノプチロライト含凝灰岩中にお
いて、モンモリロナイトは極めて広範囲且つ均一に分布
していることが電子顕微鏡により確認され、さらにクリ
ノプチロライト結晶は約5〜10μl角の板状結晶が群
を形成しているものが多く観測された。上記クリノプチ
ロライトの結晶の性状からみて水中に分散したクリノプ
チロライトは概ね5〜数十μlの範囲に製果されている
ものと推定された。By the above treatment, the montmorillonite contained in the zeolite ore (#graystone) swells with a large amount of water, and disintegrates into fine powder including coarse particles. Incidentally, montmorillonite is clayey and is known to swell to 7 to IO times its volume in water, and electron microscopy shows that montmorillonite is extremely widely and evenly distributed in clinoptilolite-containing tuff. Furthermore, many clinoptilolite crystals were observed in which plate-shaped crystals of about 5 to 10 μl square formed groups. Judging from the properties of the clinoptilolite crystals, it was estimated that the amount of clinoptilolite dispersed in water was approximately 5 to several tens of μl.
本実施例では上記の考察に基づいて水中に分散した微粉
から上記推定範囲に則し74μ肩を越える粒径のものを
ふるいで除去し、5μ1未満の微粒子を遠心分離機で分
離除去することによって分級した。In this example, based on the above consideration, from the fine powder dispersed in water, particles with a particle size exceeding 74 μm are removed using a sieve in accordance with the above estimated range, and fine particles smaller than 5 μ1 are separated and removed using a centrifuge. Classified.
その結果ゼオライト含有率92%と、従来の天然ゼオラ
イトからは得られなかった高純度のゼオライトを得るこ
とができた。この純度測定は陽イオン交換容量(CEC
値)によって行ったものである。As a result, it was possible to obtain zeolite with a zeolite content of 92% and a high purity that could not be obtained from conventional natural zeolite. This purity measurement is based on cation exchange capacity (CEC).
value).
〈発明の効果〉
本発明方法は以下の如く構成され、ゼオライト原鉱を微
粉化してゼオライトを回収する際、ゼオライト鉱石粒の
機械的粉砕をできるだけ避け、鉱石中のモンモリロナイ
トの水による膨潤作用で崩壊させるためゼオライトは限
られた粒径範囲で特有の結晶状態を維持し、他方長石等
の不純物も機械的な微小破壊を受けない結果、両者の粒
度分布が異なり、上記ゼオライトが集中的に分布する粒
径範囲だけを分級回収することにより、きわめて高純度
のゼオライトを得ることができる。またこの方法によれ
ば原鉱のゼオライト含有量が少ない場合でも処理時間は
多く要するものの、比較的安定して高純度の天然ゼオラ
イトが得られる利点がある。<Effects of the Invention> The method of the present invention is configured as follows. When pulverizing zeolite raw ore and recovering zeolite, mechanical crushing of zeolite ore grains is avoided as much as possible, and montmorillonite in the ore is disintegrated by the swelling action of water. As a result, zeolite maintains a unique crystalline state within a limited particle size range, and on the other hand, impurities such as feldspar are not subject to mechanical micro-destruction.As a result, the particle size distribution of the two is different, and the zeolite is concentratedly distributed. By classifying and collecting only the particle size range, extremely high purity zeolite can be obtained. Further, according to this method, even if the zeolite content of the raw ore is low, although it requires a long processing time, it has the advantage of being able to obtain relatively stable and highly pure natural zeolite.
Claims (1)
採掘後にゼオライトの結晶を破壊しない程度に粉砕した
後水中に浸漬し、上記膨潤性粘土鉱物を膨潤させること
によって前記凝灰岩を微粉状態に砕解せしめ、砕解した
微粉を分級してゼオライト結晶粒が最も高密度に分布す
る所定範囲の粒度のもののみを回収して高純度ゼオライ
トを得る天然ゼオライトの精製方法。 2)膨潤性粘土鉱物がモンモリノナイトであり、ゼオラ
イト含凝灰岩がクリノプチロライト含凝灰岩である特許
請求の範囲第1項に記載の天然ゼオライトの精製方法。[Claims] 1) Zeolite-containing tuff containing swelling clay minerals,
After mining, the tuff is crushed to the extent that it does not destroy the zeolite crystals, and then immersed in water to swell the swelling clay mineral to crush the tuff into a fine powder.The crushed fine powder is then classified to form zeolite crystal grains. A method for purifying natural zeolite to obtain high-purity zeolite by collecting only those particles with particle sizes within a predetermined range that are most densely distributed. 2) The method for refining natural zeolite according to claim 1, wherein the swelling clay mineral is montmorinonite and the zeolite-containing tuff is clinoptilolite-containing tuff.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4887790A JPH0674144B2 (en) | 1990-02-28 | 1990-02-28 | Purification method of natural zeolite |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4887790A JPH0674144B2 (en) | 1990-02-28 | 1990-02-28 | Purification method of natural zeolite |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03252310A true JPH03252310A (en) | 1991-11-11 |
JPH0674144B2 JPH0674144B2 (en) | 1994-09-21 |
Family
ID=12815514
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4887790A Expired - Fee Related JPH0674144B2 (en) | 1990-02-28 | 1990-02-28 | Purification method of natural zeolite |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0674144B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6299854B1 (en) | 1998-06-12 | 2001-10-09 | Teruo Henmi | Method of producing artificial zeolite |
EP1322426A4 (en) * | 2000-09-27 | 2006-07-26 | Basic Resources Inc | Process for extracting and purifying naturally occurring zeolite |
-
1990
- 1990-02-28 JP JP4887790A patent/JPH0674144B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6299854B1 (en) | 1998-06-12 | 2001-10-09 | Teruo Henmi | Method of producing artificial zeolite |
EP1322426A4 (en) * | 2000-09-27 | 2006-07-26 | Basic Resources Inc | Process for extracting and purifying naturally occurring zeolite |
Also Published As
Publication number | Publication date |
---|---|
JPH0674144B2 (en) | 1994-09-21 |
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