JPH0674144B2 - Purification method of natural zeolite - Google Patents
Purification method of natural zeoliteInfo
- Publication number
- JPH0674144B2 JPH0674144B2 JP4887790A JP4887790A JPH0674144B2 JP H0674144 B2 JPH0674144 B2 JP H0674144B2 JP 4887790 A JP4887790 A JP 4887790A JP 4887790 A JP4887790 A JP 4887790A JP H0674144 B2 JPH0674144 B2 JP H0674144B2
- Authority
- JP
- Japan
- Prior art keywords
- zeolite
- tuff
- clay mineral
- ore
- water
- 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.)
- Expired - Fee Related
Links
- 239000010457 zeolite Substances 0.000 title claims description 39
- 229910021536 Zeolite Inorganic materials 0.000 title claims description 36
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims description 36
- 238000000034 method Methods 0.000 title claims description 16
- 238000000746 purification Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 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 claims description 9
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 9
- 230000008961 swelling Effects 0.000 claims description 9
- 239000013078 crystal Substances 0.000 claims description 8
- 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
- 239000002734 clay mineral Substances 0.000 claims description 7
- 229910001603 clinoptilolite Inorganic materials 0.000 claims description 7
- 239000000843 powder Substances 0.000 claims description 7
- 238000005065 mining Methods 0.000 claims description 5
- 239000002245 particle Substances 0.000 description 13
- 239000012535 impurity Substances 0.000 description 5
- 238000005259 measurement 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
- 239000010419 fine particle Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000002522 swelling effect Effects 0.000 description 2
- 239000011882 ultra-fine particle Substances 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
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。TECHNICAL FIELD The present 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
の他触媒等としても用いられるが、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> In general, zeolite is used as a catalyst in addition to a water purifying action, a deodorizing action, a gas adsorbing action, but from the viewpoint of cost and mass productivity, it is desired to use a natural zeolite rather than an artificial zeolite. However, since natural zeolite is a mineral resource and contains a large amount of impurities, and its purity is low, various expected actions 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, conventional natural zeolites are refined by a dry method and a wet method.The former is to pulverize and classify after mining to remove a part of impurities such as quartz having high hardness. (Approximately 60-70%) is not much different.
また後者の湿式法においては、採鉱後のものを例えば15
mm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、科学的処理を施して
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, after mining, for example,
What was pulverized to a particle size of mm or less is further mechanically wet pulverized using a ball mill or the like, and coarse classification, mechanical re-pulverization of downstream discharge, upstream exhaust centrifugal classification, secondary pulverization of coarse particles, secondary classification It is known that ultrafine particles are removed as impurities, a chemical treatment is performed to re-solidify, and the mixture is re-crushed 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70
%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さないだけでなく、
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。<Problems to be Solved by the Invention> However, in the above method, a high purity zeolite cannot be expected in the dry method as described above.
%, A zeolite with a purity of 80% or more was reported, but this is an estimated value by comparing the peak heights by X-ray analysis, and the cation exchange capacity that allows more accurate measurement Based on the measurement, the value obtained is slightly better or almost unchanged from that of the raw ore. Moreover, the above-mentioned method not only puts out a very limited range of experimental purification,
It has many purification steps and is complicated, and it is not practical 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 pulverized feldspar or other glassy substance contained in the raw ore that is pulverized and mixed into a 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発明の方法は、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、粉砕した微粉を分級し
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 Problems> The method of the present invention for solving the above-mentioned problems is that zeolite-containing tuff containing a swelling clay mineral is ground in water after being crushed to the extent that zeolite crystals are not destroyed after mining. Immersion, swelling the swelling clay mineral to disintegrate the tuff into a fine powder state, classify the pulverized fine powder, and recover only those with a grain size within a predetermined range in which zeolite crystal grains are most densely distributed. In this method, the mechanical crushing in the crushing process of the zeolite ore is kept to the minimum necessary, and especially in the final process of crushing, the zeolite ore grains are crushed only by the swelling action of montmorillonite. It is characterized by that.
また上記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
ことを第2の特徴としている。The second characteristic is that the swelling clay mineral is montmorillonite and the zeolite tuff is clinoptilolite tuff.
<作 用> 本発明においては、鉱石中にモンモリノナイト等の膨潤
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。<Operation> In the present invention, since the ore is disintegrated by swelling the swelling clay mineral such as montmorillonite in the ore with the water at the time of immersion, the zeolite is dispersed in water in its crystalline state and Since other impurities do not undergo mechanical fine crushing, they are divided into those which are dispersed with a relatively large particle size and those which are dispersed as extremely small particles. As a result, high-purity natural zeolite can be obtained by classifying and recovering the particle size range in which the zeolite crystal particles are most densely distributed and located between the ultrafine particles and the relatively fine 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%、モンモリノナイトが重量比約10%前
後含まれているものを使用した。<Examples> In the following, examples of the present invention will be described in detail. In this example, a zeolite ore from Shimane Prefecture is used, and the clinoptilolite content is about 60% to 70%, and the montmorillonite is about 10% by weight. I used the one included around%.
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5mm以下の粒径に粉砕して3〜5mmの粒
径のものを分級採取した。但し、粒計の分級は実験の設
定条件として定めたもので、処理自体には3mm以下のも
のを含んでいてもよい。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のボール混入しないで、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20時間前後駆動させる。この時使用
したボールミルは容量1のものであるが、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。After mining the zeolite ore, it was dried to a water content of about 3%, crushed with a crusher or the like to a particle size of 5 mm or less, and classified to a particle size of 3 to 5 mm. However, the classification of the granulometer is set as a setting condition of the experiment, and the treatment itself may include 3 mm or less. Next, do not mix balls in the ball mill to avoid mechanical crushing of ore grains, and add water in a weight ratio of about 5 times the amount of ore to make it immersed.
The ball mill is driven for about 20 hours. The ball mill used at this time has a capacity of 1. However, when the capacity of the ball mill is large, it is not necessary that the crushed particle size or classified particle size of the raw ore be 5 mm or less.
上記処理によりゼオライト鉱石(凝灰岩)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7〜10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5〜10μm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μmの範囲に濃集されているもの
と推定された。By the above treatment, the zeolite ore (tuff) contains montmorillonite containing a large amount of water and swells, and is disintegrated into a fine powder containing coarse particles. By the way, it is known that montmorillonite is clay-like and swells to 7 to 10 times its volume by water, and that montmorillonite is extremely widely and uniformly distributed in clinoptilolite-bearing tuff. In addition, many clinoptilolite crystals were observed in which plate-like crystals of about 5 to 10 μm square formed a group. Considering the properties of the clinoptilolite crystals, it was estimated that the clinoptilolite dispersed in water was concentrated in the range of approximately 5 to several tens of μm.
本実施例では上記の考案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74μmを越える粒径のものをふ
るいで除去し、5μm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 the present embodiment, based on the above idea, fine powder dispersed in water having a particle size of more than 74 μm is removed by sieving according to the above estimated range, and fine particles of less than 5 μm are separated and removed by a centrifuge. did.
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 a high-purity zeolite with a zeolite content of 92%, which was not possible with conventional natural zeolites. This purity measurement is cation exchange capacity (CEC value)
It was done by.
<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。<Effect of the Invention> The method of the present invention is configured as follows, and when the zeolite ore is pulverized to recover the zeolite, mechanical crushing of the zeolite ore grains is avoided as much as possible, and the montmorillonite in the ore is disintegrated by the swelling action of water. In order to do so, the zeolite maintains a unique crystalline state in a limited particle size range, while impurities such as feldspar are not subject to mechanical microdestruction, and as a result, the particle size distributions of the two are different and the above zeolites are concentrated. By classifying and recovering only the particle size range, extremely high-purity zeolite can be obtained. Further, according to this method, although the processing time is long even if the content of zeolite in the raw ore is small, there is an advantage that natural zeolite of high purity can be obtained relatively stably.
Claims (2)
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
ゼオライトを得る天然ゼオライトの精製方法。1. A zeolitic tuff containing a swelling clay mineral is crushed after mining to the extent that zeolite crystals are not destroyed and then immersed in water to swell the swelling clay mineral, whereby the tuff is finely divided. Disintegrate into
A method for purifying natural zeolite, in which high-purity zeolite is obtained by classifying fine powder that has been disintegrated and recovering only those having a grain size within a predetermined range in which zeolite crystal grains are distributed in the highest density.
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。2. The method for purifying natural zeolite according to claim 1, wherein the swelling clay mineral is montmorillonite and the zeolite tuff is clinoptilolite 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 JPH03252310A (en) | 1991-11-11 |
| JPH0674144B2 true 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) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6299854B1 (en) | 1998-06-12 | 2001-10-09 | Teruo Henmi | Method of producing artificial zeolite |
| US6662951B1 (en) * | 2000-09-27 | 2003-12-16 | Basic Resources, Inc. | Process for extracting and purifying naturally occurring zeolite |
| CN116571347A (en) * | 2023-06-30 | 2023-08-11 | 黑龙江龙兴国际资源开发集团有限公司 | Mineral separation process for impurity removal and purification of natural clinoptilolite |
-
1990
- 1990-02-28 JP JP4887790A patent/JPH0674144B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03252310A (en) | 1991-11-11 |
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