JPH07144129A - Adsorbent consisting of carbide-containing calcined zeolite particles and its production - Google Patents

Adsorbent consisting of carbide-containing calcined zeolite particles and its production

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Publication number
JPH07144129A
JPH07144129A JP32137293A JP32137293A JPH07144129A JP H07144129 A JPH07144129 A JP H07144129A JP 32137293 A JP32137293 A JP 32137293A JP 32137293 A JP32137293 A JP 32137293A JP H07144129 A JPH07144129 A JP H07144129A
Authority
JP
Japan
Prior art keywords
natural
adsorbent
powdery mixture
powder
less
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.)
Pending
Application number
JP32137293A
Other languages
Japanese (ja)
Inventor
Sueo Sato
藤 末 雄 佐
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.)
JIIKURAITO KK
Original Assignee
JIIKURAITO KK
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 JIIKURAITO KK filed Critical JIIKURAITO KK
Priority to JP32137293A priority Critical patent/JPH07144129A/en
Publication of JPH07144129A publication Critical patent/JPH07144129A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To produce an improved adsorbent which is adopted for an object to increase a manuring effect on a paddy field, etc., and to adsorb and remove a harmful substance incorporated in a plant waste water, etc., consisting of carbide-containing calcined zeolite particles especially having a versatility to an adsorption effect, favorable from the view of handling property as a material and to provide a production method therefor. CONSTITUTION:A wet powdery mixture obtained by injecting and mixing a binder consisting of an org. of an inorg. binder aq. soln. adjusted to 0.01-0.05% to a powdery mixture consisting of powder of a natural org. matter ground to <=2mm and a natural zeolite powder ground to <=250mum and having about 30% moisture content is granulated, then the obtained granules are calcined at a calcining temp. of an order of about 500-1000 deg.C to obtain the adsorbent consisting of the carbide-containing calcined zeolite particles.

Description

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

【0001】[0001]

【発明の目的】この発明は、圃場等の施肥効果を高めた
り、工場排水等に含まれる有害物質を吸着、除去する等
の目的で採用される吸着材に関するものであり、特に、
吸着効果に汎用性があり、資材としての取り扱い性の面
でも有利な特徴を有する、改良された炭化物包含焼成ゼ
オライト粒からなる吸着材、およびその製造方法を提供
しようとするものである。
OBJECT OF THE INVENTION The present invention relates to an adsorbent used for the purpose of enhancing the fertilizing effect in fields, adsorbing and removing harmful substances contained in factory wastewater, and the like.
It is intended to provide an adsorbent comprising improved carbide-containing calcined zeolite particles, which has a versatile adsorption effect and is advantageous in terms of handleability as a material, and a method for producing the same.

【0002】[0002]

【従来技術】世界でも類を見ない経済的発展を遂げ続け
ている我が国に対し、諸外国から貿易の不均衡に対する
積極的な施策が求められている。農産物の自由化もその
中の一つとして強い要求があり、ミカンやサクランボ、
牛肉等を始めとして幾つかの品目は既に実行に移され、
様々な波紋を国内に投じているが、未だ解決されていな
い大きな課題が、我が国の主食である米の自由化に対す
る対応策である。米の自由化は、消費者側では価格の選
択上で有利になるという理由等から賛成の声も強いが、
稲作中心の農業政策を進めてきた我が国の特殊な農業事
情もあって、どのような施策に落ち着くのか内外で注目
を集めている。
2. Description of the Related Art Japan, which has continued to achieve unprecedented economic development in the world, is required by various countries to take positive measures against trade imbalances. There is a strong demand for liberalization of agricultural products, including mandarin oranges, cherries,
Some items such as beef have already been put into practice,
Although various ripples have been thrown into the country, a major issue that has yet to be resolved is how to deal with the liberalization of rice, which is our staple food. There is a strong support for the liberalization of rice because consumers will have an advantage in price selection.
Due to the special agricultural circumstances in Japan, which has promoted agricultural policies centered on rice cultivation, what kind of measures will be settled down is attracting attention both inside and outside Japan.

【0003】これまでに無いこのような厳しい情勢を受
けて、比較的安泰な農業経営に終始してきた稲作農家
も、趨勢として最終的には米も競争の市場へ移行するで
あろうとの予測から、規模の拡大による栽培の効率化と
高品質化、および増収対策に対する関心が高く、また、
政府としても食料管理制度の見直しをする中、国内の米
流通政策を手直しして自主流通米制度を導入する等、稲
作農家の意欲を駆り立たせる施策を打ち出し、既にそれ
なりの実効を上げ始めている。こうした経営内容の効率
化の問題で稲作農家個々の自助努力を必要とする事項
が、高収益、高品質化のための栽培技術の確立について
であろう。
In response to such a severe situation that has never existed before, it is predicted that rice farms, who have started to maintain relatively stable agricultural management, will eventually move to a competitive market for rice as a trend. , Interest in improving efficiency and quality of cultivation due to expansion of scale, and measures to increase revenue,
While the government is also reviewing the food management system, it has begun to implement measures to motivate rice farmers, such as revising domestic rice distribution policy and introducing a voluntary rice distribution system. . The issue that requires the self-help efforts of each rice farmer in order to improve management efficiency is the establishment of cultivation techniques for high profitability and high quality.

【0004】最近では、人体あるいは自然環境への悪影
響に対する高い関心から、新農薬の開発、農薬使用量の
自粛、農薬に頼らない丈夫な苗作りのための施肥対策、
圃場管理の検討等といった栽培技術が多くの稲作農家で
真剣に検討され、次第に実行に移されてきている。特
に、米の高品質化という時代の要請に対する栽培技術と
しては、単に新品種の栽培に頼るだけではなく、肥料の
選択、施肥対策といった対応が重要であるという認識か
ら、有機肥料(堆肥、ぼかし)が積極的に取り入れられ
ると共に、施肥効率を高めるための様々な技術が検討さ
れている。
[0004] Recently, due to the great interest in adverse effects on the human body or the natural environment, development of new pesticides, self-restraint of pesticide use, fertilizer application measures for the production of sturdy seedlings that do not rely on pesticides,
Many rice farmers are seriously studying cultivation techniques such as studying field management, and gradually implementing them. In particular, as a cultivation technique to meet the demands of high quality rice, it is important not only to cultivate new varieties but also to select fertilizers and measures for fertilizer application. ) Is being actively introduced, and various techniques for increasing fertilization efficiency are being studied.

【0005】施肥効率を高める技術として採用されてき
た従来技術としては、活性炭を圃場に積極的に散布、混
入し、肥料が簡単に圃場から流出してしまわないように
すると共に、微生物の繁殖環境を確保して肥料分の分
解、吸収効率を高めるようにした方法がある。この従前
までの活性炭による施肥効率を高める対策は、活性炭の
吸着性能の高さを利用するものであることから、それ自
体有効であって導入する稲作農家も少なくはないが、活
性炭が比較的高価であって、大量に採用する上で経済的
負担が大き過ぎるという難点と、圃場に引き入れる水や
雨水による増水で流出し易いという取り扱い管理上の問
題等から、最近では、それら欠点のある活性炭に代え、
その顕微鏡的微細孔を有する性状から、水分やガス、塩
基等の吸着作用が極めて強い天然ゼオライト(含水アル
ミノ珪酸塩)が、国内に略無尽蔵に産出していて比較的
安価に入手できること、圃場に馴染み易く、流出の虞が
少ないこと等の理由で、市場に出回り始め、稲作農家の
関心を集めている。
As a conventional technique which has been adopted as a technique for improving fertilization efficiency, active carbon is actively sprayed and mixed in a field to prevent fertilizer from easily flowing out from the field and a microbial breeding environment. There is a method of ensuring the efficiency of decomposition of fertilizer and improving the absorption efficiency. The conventional measures to increase fertilizer application efficiency with activated carbon are to use the high adsorption performance of activated carbon, so it is effective in itself and many rice farmers introduce it, but activated carbon is relatively expensive. However, due to the difficulty that the economic burden is too large for large-scale adoption and the problem of handling and management that water easily flows out due to the increase in water drawn into the field or rainwater, activated carbon with these defects has recently been selected. Instead of
Due to its microscopic microscopic properties, natural zeolite (hydrous aluminosilicate), which has an extremely strong adsorption action for water, gas, bases, etc., is produced in Japan almost inexhaustibly and can be obtained at relatively low cost, in the field. It has begun to appear in the market and is attracting the attention of rice farmers because it is easy to get used to and there is little risk of outflow.

【0006】こうして登場した天然ゼオライトを利用し
た吸着材としては、単に天然ゼオライトを破砕粒状とし
て適度な粒度にしたものや、それらを高温で焼成して焼
成ゼオライト粒とするか、あるいは、天然ゼオライト粉
末体に加水、混練したものを円柱状に押し出し成形して
から焼成したものとするか、あるいはまた、天然ゼオラ
イト粉末体に加水、混練したものを球形状に造粒してか
ら焼成したもの等であり、何れも天然ゼオライト単体で
ある点で、基本的な特性に変わりのないものである。
[0006] The adsorbents using the natural zeolite that have been introduced in this way are those obtained by simply crushing the natural zeolite into a proper particle size, firing them at a high temperature to obtain calcined zeolite particles, or natural zeolite powder. It may be obtained by adding water to the body, kneading and extruding into a cylindrical shape and then firing, or alternatively, by adding water to the natural zeolite powder body, kneading it into a spherical shape and then firing. However, all of them are natural zeolite alone, and their basic characteristics are the same.

【0007】ところで、吸着特性で比較した場合、天然
ゼオライト単体からなるものについては、生活排水処理
能力や重金属処理能力、有機塩素化合物処理能力、ガス
吸着能力等の項目の中、例えばMEP(スミチオン)や
一部の重金属、即ち、銅、亜鉛、カドミウムに対する吸
着特性等を除けば、殆どの項目で先の活性炭の能力に劣
るか精々同等の能力を有する程度のものであり、その意
味では、天然ゼオライト単体で完全に活性炭の代替物と
なり得ない弱みがある。しかし、活性炭に比較されれば
性能的に劣る〒ではあっても、他の物質との比較におい
て桁外れに優れた吸着特性を有している事実に変りはな
く、したがって、その値をいかに補い得るかによって
は、経済性、取扱性の有利さが手伝って、十分活性炭に
代わる吸着材として通用し得るものとなる筈である。
By the way, when comparing the adsorption characteristics, for the natural zeolite alone, among the items such as domestic wastewater treatment capacity, heavy metal processing capacity, organic chlorine compound processing capacity, gas adsorption capacity, etc., for example, MEP (Sumithion). Except for the adsorption characteristics for some heavy metals, such as copper, zinc, and cadmium, most of the items have inferior or almost equivalent capabilities to the above-mentioned activated carbon. There is a weakness that zeolite alone cannot completely substitute for activated carbon. However, even if it is inferior in performance when compared to activated carbon, it still has the fact that it has exceptionally excellent adsorption properties in comparison with other substances, and therefore it can be supplemented by that value. Depending on the situation, it should be possible to use it as an adsorbent that sufficiently replaces the activated carbon due to the advantages of economy and handleability.

【0008】この発明は、上記した認識に立脚し、天然
ゼオライトに深く関わる者として鋭意開発、研究を継続
してきた結果、天然ゼオライト粉末体から焼成ゼオライ
ト粒を造粒、焼成する過程で効率的に炭化物を含有させ
てゼオライトの吸着特性を改善するようにした炭化物包
含焼成ゼオライト粒およびその新規な製造方法の実現化
に成功したものであり、以下で、その構成を詳述するも
のである。
Based on the above recognition, the present invention has been earnestly developed and researched as a person who is deeply involved in natural zeolite, and as a result, in the process of granulating and calcining calcined zeolite particles from a natural zeolite powder body. The present invention has succeeded in realizing a charcoal-containing calcined zeolite particle in which a charcoal-containing material is contained so as to improve the adsorption property of the zeolite and a novel method for producing the same, and the constitution thereof will be described in detail below.

【0009】この発明の吸着材の構成の要旨は、2mm以
下に粉砕した籾殻、オガ屑等の天然有機物粉状体と25
0μm以下に粉砕した天然ゼオライト粉末体とからなる
粉状混合体に、0.01〜0.05%に調整したカルボ
キシメチルセルロースナトリウム水溶液、その他無機ま
たは有機バインダー等を粘結剤として注入、混合した、
含水率約30%前後の天然ゼオライト湿潤体から、造粒
後、約500〜1000℃程度の焼成温度で焼成して形
成した活性炭混入焼成ゼオライト粒からなる吸着材とす
るものである。
The gist of the constitution of the adsorbent of the present invention is to use a natural organic substance powder such as rice husk and sawdust scraped to 2 mm or less and 25
Into a powdery mixture consisting of a natural zeolite powder pulverized to 0 μm or less, 0.01-0.05% sodium carboxymethyl cellulose aqueous solution, other inorganic or organic binder, etc. were injected and mixed as a binder,
The adsorbent is composed of activated carbon-mixed calcined zeolite particles formed by granulating a moistened natural zeolite having a water content of about 30% and calcining at a calcining temperature of about 500 to 1000 ° C.

【0010】また、上記吸着材を製造する製造方法の要
旨は、250μm以下に粉砕した天然ゼオライト粉末体
に、2mm以下に粉砕した籾殻、オガ屑等の天然有機物粉
状体を6:4重量部の割合で均質に混合して粉状混合体
を形成した上、0.01〜0.05%に調整したカルボ
キシメチルセルロースナトリウム水溶液、その他無機ま
たは有機バインダー等の粘結剤を加え、含水率約30%
前後の天然ゼオライト湿潤体としたものから、造粒後、
約800〜1000℃程度の温度に加熱したロータリー
キルンで約5〜6分間前後焼成してから冷却した上、分
級機を経由して粒度0.1〜10mm前後で不定形の粒状
体としてなる、炭化物包含ゼオライト粒からなる吸着材
の製造方法である。
Further, the gist of the manufacturing method for manufacturing the above-mentioned adsorbent is as follows: 6: 4 parts by weight of a natural zeolite powder body crushed to 250 μm or less and a natural organic substance powder such as rice husk and sawdust scraped to 2 mm or less. To form a powdery mixture, and then add a sodium carboxymethylcellulose aqueous solution adjusted to 0.01 to 0.05% and other binder such as an inorganic or organic binder to obtain a water content of about 30%. %
After granulating from the natural zeolite wet body before and after,
Carbide that becomes an amorphous granular material with a particle size of 0.1 to 10 mm through a classifier after being baked for about 5 to 6 minutes in a rotary kiln heated to a temperature of about 800 to 1000 ° C. and then cooled. It is a method for producing an adsorbent composed of included zeolite particles.

【0011】天然有機物粉状体としては、籾殻、オガ
屑、樹皮等のように燻炭化可能なものであれば全て対象
となり得るものであり、それらを2mm以下のサイズに粉
砕して採用する。天然ゼオライトは、例えば商品名で
「イタヤゼオライト」と称されて福島県と山形県との県
境当たりから産出する天然のゼオライト等であって、純
度約70〜80%前後の極めて良質のものを採用すると
好適である。
Any natural organic matter powder can be used as long as it can be smoked and carbonized, such as rice husks, sawdust, and bark, and these are crushed to a size of 2 mm or less before use. The natural zeolite is, for example, a natural zeolite called "Itaya Zeolite" under the trade name and is produced from the border between Fukushima prefecture and Yamagata prefecture, and has an extremely high quality of about 70-80% purity. It is suitable if it is.

【0012】この天然ゼオライトを250μm以下の粉
末体に粉砕した上、上記2mm以下に粉砕した天然有機物
粉状体が、重量百分率で同量以下、例えば8割相当量前
後となる割合等、その後の造粒工程に支障を来すことが
なく、且つまた、焼成工程あるいはそれ以降の取り扱い
段階における粒状体としての形状保持に支障を来す虞の
ない最適な比率が選択され、均質な状態に攪拌、混合さ
れて粉状混合体とするものであり、その粉状混合体は、
天然ゼオライト粉末粒子間に満遍なく天然有機物粉状体
が散在するような状態、天然有機物粉状体側からみれ
ば、その表面に細かい〒粉末が振り掛けられ、それら相
互間に天然ゼオライト粉末が充填されたような状態のも
のとなる。
This natural zeolite is ground to a powder body of 250 μm or less, and the powdered natural organic substance ground to 2 mm or less is equal to or less than the same amount by weight percentage, for example, about 80% or so. An optimum ratio is selected that does not hinder the granulation process and that does not hinder the shape retention as granules in the firing process or the subsequent handling stages, and agitates in a homogeneous state. , Which is mixed into a powdery mixture, and the powdery mixture is
In a state where the natural organic matter powder is evenly distributed among the particles of the natural zeolite powder, when viewed from the side of the natural organic matter powder, fine powder is sprinkled on the surface and the natural zeolite powder is filled between them. It will be in a state of.

【0013】粘結剤としては、例えば有機バインダーと
して汎用されるカルボキシメチルセルロースナトリウム
(通称CMC)等、有機または無機の各種バインダーが
採用可能であり、これを0.01〜0.05%水溶液、
望ましくは、0.03%水溶液として採用するように
し、この範囲以下の濃度の水溶液では、以下の工程であ
る造粒およびハンドリング段階で崩壊し易くなる。ま
た、この範囲以上の濃度では、焼成されて形成された天
然ゼオライトが、焼成過程でCMCに災いされて天然ゼ
オライト本来の秀れた機能に支障を来す虞が懸念される
ことから、可能な限りこの範囲の温度を保つようにする
のが望ましい。
As the binder, various organic or inorganic binders such as sodium carboxymethyl cellulose (commonly known as CMC) commonly used as an organic binder can be adopted.
Desirably, it is adopted as a 0.03% aqueous solution, and an aqueous solution having a concentration below this range is likely to be disintegrated in the following steps of granulation and handling. Further, at a concentration higher than this range, there is a concern that the natural zeolite formed by firing may be damaged by CMC during the firing process and hinder the excellent function of the natural zeolite. It is desirable to keep the temperature in this range as long as possible.

【0014】上記のような濃度のCMC水溶液等を粘結
剤として、この発明で目的とする炭化物包含焼成ゼオラ
イト粒を造粒するには、上記混合粉状体の水分含有量が
略30%前後のものに調整され、造粒する上で理想的な
湿潤状の混合粉状体となし、天然ゼオライト粉末間に満
遍なく天然有機物粉状体が散在するような状態、逆に天
然有機物粉状体側から見れば、その周囲に細かな天然ゼ
オライト粉末が介在すると共に、それら相互間に天然ゼ
オライト粉末が充填された状態で、0.1〜10mm前後
の粒状物が確実に形成されるようにしなければならな
い。この水分含有量を実現する際、天然ゼオライト粉末
体自体の含水率(通常6〜7%前後)を考慮した上でC
MC水溶液その他水溶液からなる粘結剤の注入量が決定
されるようにする必要がある。なお、この造粒工程に
は、回転容器型造粒機あるいは遠心拡散造粒機、例えば
レーディゲミキサー(商品名。西独レーディゲ社)等公
知の造粒機の採用が可能であり、前者は連続式、後者は
バッチシステムで造粒される。
In order to granulate the calcined zeolite particles containing carbide which is the object of the present invention using the CMC aqueous solution or the like having the above concentration as a binder, the water content of the mixed powder is about 30%. It is adjusted to the one of the above, and it becomes an ideal wet mixed powder for granulation, the state that the natural organic substance powder is evenly distributed among the natural zeolite powders, conversely from the natural organic substance powder side. Obviously, it must be ensured that fine natural zeolite powder is present around it and that the granular particles of about 0.1 to 10 mm are formed with the natural zeolite powder filled between them. . When realizing this water content, the water content (usually around 6 to 7%) of the natural zeolite powder itself is taken into consideration and C
It is necessary to determine the injection amount of the binder containing the MC aqueous solution and other aqueous solutions. In this granulation step, a known granulator such as a rotary container granulator or a centrifugal diffusion granulator, for example, a Reedige mixer (trade name; West Germany Reedige Co.) can be used, and the former is Continuous, the latter is granulated in a batch system.

【0015】焼成キルン内での焼成温度は、約500〜
1000℃程度の範囲に設定されるべきであり、最適に
は700℃前後の焼成温度が選択されるのが理想的であ
って、この焼成温度範囲を下回り過ぎると、天然有機物
粉状体の燻炭化が完全に進行しない虞があり、また、こ
の範囲を上回り過ぎてしまうと、今度は天然有機物粉状
体が燃え尽きてしまって、焼成天然ゼオライトの中に炭
化物が存在しない焼成天然ゼオライト粒を製造してしま
う危険性も出てくるため、最適な温度範囲での燃焼調整
が必要である。
The firing temperature in the firing kiln is about 500-
It should be set in a range of about 1000 ° C., and ideally, a firing temperature of around 700 ° C. is ideally selected. If the firing temperature range is too low, the smoke of the natural organic matter powder is smoked. There is a possibility that carbonization will not progress completely, and if it exceeds this range, the natural organic matter powder will burn out this time, producing calcined natural zeolite particles with no carbides in the calcined natural zeolite. Since there is a risk that it will occur, it is necessary to adjust the combustion within the optimum temperature range.

【0016】一方、この範囲内で焼成された天然ゼオラ
イトは、脱水、部分的に焼結されて含水アルミノ珪酸塩
から一種の異性縮合酸化物系多孔性セラミックスに変性
し、そのまま元の秀れた性状を維持し続けるものとする
ことができ、しかも、粘結材であるCMCによる天然ゼ
オライトの性状の劣化も殆ど無視できる範囲のものとす
ることが可能であり、この範囲以下で焼成されてしまう
と、不定形粒状体としての保形性や硬度の点で問題を生
じるだけではなく、CMCが天然ゼオライトの顕微鏡的
微細孔に残留する虞が大きくなって、本来天然ゼオライ
トに備わっていた秀れた性能に支障を来し、望ましい吸
着材を得る上で不利になり、また、その範囲を大きく越
えた焼成がなされると、天然ゼオライトの有していた微
細孔壁が溶融して微細孔を崩壊、減少させてしまう虞が
生じ、これまたこの発明の目的とする天然ゼオライト本
来の性状を生かした理想的な吸着材の製造が不可能にな
る。
On the other hand, the natural zeolite calcined within this range is dehydrated and partially sintered to be modified from hydrous aluminosilicate into a kind of isomer condensed polycondensate porous ceramics, which is excellent as it is. The properties can be maintained, and the deterioration of the properties of the natural zeolite due to the CMC, which is a binder, can be set to a level that can be almost ignored, and firing will occur below this range. In addition to causing problems in shape retention and hardness as an irregularly shaped granular material, there is a greater risk that CMC will remain in the microscopic microscopic pores of natural zeolite, and the excellent nature of natural zeolite Performance is impaired, it is disadvantageous in obtaining a desirable adsorbent, and if the firing is far exceeding that range, the fine pore walls of natural zeolite will melt. Collapse pores, cause fear that is reduced, which also impossible to manufacture an ideal adsorbent utilizing the natural zeolite natural cast is an object of the present invention.

【0017】[0017]

【実施例1】以上のような構成を基本とするこの発明の
炭化物包含焼成ゼオライト粒の具体例を示すと以下のと
おりとなる。即ち、250μm以下に粉砕した天然ゼオ
ライト粉末体に、2mm以下に粉砕した籾殻、オガ屑等の
天然有機物粉状体を重量部で6:4の割合となる如く均
質に混合して粉状混合体を形成した上、0.01〜0.
05%に調整したカルボキシメチルセルロースナトリウ
ム水溶液からなる粘結剤を加え、含水率約30%前後の
湿潤粉状混合体としたものから、造粒後、約900℃前
後の温度に加熱したロータリーキルンに連続投入して焼
成し、冷却機で冷却した上、粒度で0.1〜10mm前後
の粒状体に篩分けしてなる、炭化物包含焼成ゼオライト
粒からなる吸着材とするものである。
Example 1 A specific example of the carbide-containing calcined zeolite particles of the present invention based on the above-mentioned constitution is as follows. That is, a natural zeolite powder body pulverized to 250 μm or less and a natural organic matter powder body pulverized to 2 mm or less such as rice husk and sawdust are homogeneously mixed at a ratio of 6: 4 by weight to form a powder mixture. 0.01 to 0.
Add a binder consisting of sodium carboxymethyl cellulose solution adjusted to 05% to make a wet powdery mixture with a water content of about 30%, and after granulation, continue to a rotary kiln heated to a temperature of about 900 ° C. The adsorbent is composed of calcined zeolite particles containing carbide, which is charged and calcined, cooled with a cooler, and then sieved into granules having a particle size of about 0.1 to 10 mm.

【0018】[0018]

【実施例2】次ぎに、炭化物含有焼成ゼオライト粒から
なる吸着材の製造方法の具体的な実施例を示す。先ず、
250μm以下に粉砕した天然ゼオライト粉末体、およ
び2mm以下に粉砕した籾殻を定量フィーダーに掛けて計
量し、夫々の混合割合が、重量部で略6:4となるよう
にして、回転容器型転動造粒機、例えばレーディゲミキ
サー造粒機(商品名)に投入し、十分に混合、攪拌して
均質な粉状混合体を形成すると共に、濃度を略0.03
%としたCMC水溶液を注入し、水分含有量約30%程
度の湿潤粉状混合体としながら前記造粒機の作動で0.
1〜10mm程度の大きさの粒状体を形成する。CMC水
溶液の注入量は、天然ゼオライト粉末体自体の含水率
(通常6〜7%前後)を考慮した上で適量が決定される
ようにしなければならないことは、前述のとおりであ
る。
[Embodiment 2] Next, a concrete embodiment of a method for producing an adsorbent made of calcined zeolite particles containing a carbide will be described. First,
The natural zeolite powder pulverized to 250 μm or less and the chaff pulverized to 2 mm or less are hung on a quantitative feeder and weighed so that the mixing ratio of each is about 6: 4 in parts by weight, and rolling container type rolling The mixture is put into a granulating machine, for example, a Loedige mixer granulating machine (trade name), sufficiently mixed and stirred to form a homogeneous powdery mixture, and the concentration is about 0.03.
% CMC aqueous solution was injected to obtain a wet powdery mixture having a water content of about 30%, and the granulator was operated to give a density of 0.
A granular material having a size of about 1 to 10 mm is formed. As described above, the injection amount of the CMC aqueous solution must be determined in consideration of the water content of the natural zeolite powder itself (usually around 6 to 7%).

【0019】所定量の粒状体がストックされた段階でベ
ルトコンベアによりロータリーキルンに送り込み、約8
00〜1000℃前後の燃焼温度(製品温度では500
〜800℃前後)で約5〜15分程度焼成した上、自然
放冷もしくは冷却機によって約60〜100℃前後、望
ましくはなるべく低い60℃辺りまで冷却してしまう。
冷却して取り出した焼成粒状体は、内部に炭化物を包含
した焼成天然ゼオライトとなり、、それらを篩分け装置
で0.1〜10mm程度前後の粒サイズのものに揃え、所
定量毎に計量して袋詰めされる。
When a predetermined amount of granular material is stocked, it is sent to a rotary kiln by a belt conveyor, and about 8
Combustion temperature around 00-1000 ° C (500 at product temperature)
Approximately about 800 ° C.) for about 5 to 15 minutes, and then naturally cooling or cooling to about 60 to 100 ° C., preferably about 60 ° C. which is as low as possible.
The calcined granules taken out after cooling become calcined natural zeolite containing carbides inside, and they are made to have a particle size of about 0.1 to 10 mm with a sieving device, and weighed in predetermined amounts. Will be packed in bags.

【0020】[0020]

【作用効果】以上のようにして製造されたこの発明の炭
化物包含焼成ゼオライト粒からなる吸着材の特性を、活
性炭のそれと比較して実験した結果を示すと次のとおり
となる。先ず、生活排水処理試験結果では、表1に示す
とおりであり、この発明の吸着材は、代表的な農薬であ
るMEPの除去率で活性炭のそれを凌ぎ、その他生物化
学的酸素要求量や化学的酸素要求量、ノルマルヘキサン
抽出物、窒素、燐の除去率で、活性炭のそれに比してや
や劣るか略同等の値を示していて、これらの項目に関す
る限り、十分活性炭に代替するものとなり得ることが解
る。
[Advantages] The characteristics of the adsorbent composed of the calcined zeolite particles containing carbide of the present invention produced as described above are compared with those of activated carbon, and the results of experiments are shown as follows. First, the results of the domestic wastewater treatment test are as shown in Table 1. The adsorbent of the present invention surpasses that of activated carbon in the removal rate of MEP, which is a typical pesticide, and other biochemical oxygen demands and chemicals. The oxygen demand, normal hexane extract, nitrogen and phosphorus removal rates are slightly inferior to or equivalent to those of activated carbon, and as far as these items are concerned, it can be a sufficient substitute for activated carbon. Understand.

【0021】[0021]

【表 1】[Table 1]

【0022】上記試験に使用した試験水は、宮城県栗原
郡瀬峰町内家庭雑廃排水路で採取した水にスミチオンを
約10ppmになるように添加した試料を原水としたも
のである。また、試料の調整方法は、容器(0.1立方
m)に試験材料4.5kgを入れ、その中に4.5リット
ルの前記試験水(原水)を入れ、10時間試験材料と接
触、放置し、その後、試験水(処理水)を回収した方法
によるものである。
The test water used in the above-mentioned test was a sample obtained by adding Sumithion to about 10 ppm to the water collected in the domestic wastewater drainage channel in Semine-cho, Kurihara-gun, Miyagi Prefecture. The sample preparation method is as follows: 4.5 kg of the test material is placed in a container (0.1 cubic meter), 4.5 liters of the test water (raw water) is placed therein, and the test material is left in contact for 10 hours. However, the test water (treated water) was then collected.

【0023】次に、有機塩素化合物処理試験の試験結果
を、表2に示す。上記試験に使用した試験水は、仙台市
の水道水を使用し、各物質を約5mg/lに調整した試料を
原水とし、試験は、単一成分毎に実施したものである。
また、試料液の調整方法は、容器(0.1立方m)に試
験材料4.5kgを入れ、その中に4.5リットルの前記
試験水(原水)を入れ、10時間試験材料と接触、放置
し、その後、試験水(処理水)を回収した方法によるも
のである。これらの試験項目の結果からは、この発明の
吸着材が、全ての項目で略活性炭の除去率に匹敵する高
い除去性能値を示している。
Next, Table 2 shows the test results of the organic chlorine compound treatment test. The test water used in the above test was tap water from Sendai City, and a sample prepared by adjusting each substance to about 5 mg / l was used as raw water. The test was conducted for each single component.
In addition, the method for preparing the sample liquid is to put 4.5 kg of the test material in a container (0.1 cubic m), put 4.5 liters of the test water (raw water) therein, and contact with the test material for 10 hours, This is due to a method in which the test water (treated water) is recovered after being left standing. From the results of these test items, the adsorbent of the present invention shows a high removal performance value which is almost equal to the removal rate of activated carbon in all items.

【0024】[0024]

【表 2】[Table 2]

【0025】表3には、重金属処理試験の結果が示され
ている。このデーターからは、この発明の吸着材は、水
銀の除去率で活性炭のそれを凌ぎ、その他の項目の重金
属の除去率では活性炭のそれに略匹敵している。上記試
験に使用した試験水は、仙台市の水道水を使用し、所定
の試薬を用いて各物質約100mg/lに調整した試料を原
水とし、試験は、単一成分毎に実施したものである。ま
た、試料液の調整方法は、三角フラスコ(300ml)に
試験水を100ml入れ、その中に試験材料1gを添加
し、常温で24時間放置した上、濾過して処理水とする
方法によるものである。
Table 3 shows the results of the heavy metal treatment test. From this data, the adsorbent of the present invention surpasses that of activated carbon in the removal rate of mercury, and is almost comparable to that of activated carbon in the removal rates of other heavy metals. The test water used in the above test was tap water from Sendai City, and the sample was adjusted to about 100 mg / l of each substance using the specified reagents as raw water. The test was conducted for each single component. is there. The sample solution is prepared by putting 100 ml of test water in an Erlenmeyer flask (300 ml), adding 1 g of the test material therein, leaving it at room temperature for 24 hours, and filtering it to obtain treated water. is there.

【0026】[0026]

【表 3】[Table 3]

【0027】以上のとおり、この発明の炭化物包含焼成
ゼオライト粒からなる吸着材は、本来天然ゼオライトが
有する特性をそのままか、あるいは更に強化して持続さ
せているだけではなく、その内部に炭化物を一体的に包
含させていて、この炭化物が活性炭としての機能を果た
し、天然ゼオライトの特性で弱い部分を補完する作用を
及ぼす構造としているため、単なる天然ゼオライトある
いはそれを焼成した焼成ゼオライト単品からなる吸着材
に比較して、その性能は大巾に改善されていて、殆ど活
性炭単品のそれに互するだけのものとなっている。
As described above, the adsorbent composed of the calcined zeolite particles containing carbide according to the present invention not only retains the characteristics originally possessed by natural zeolite, or further strengthens and maintains them, but also integrates the carbide therein. Since this carbide functions as activated carbon and has a function of complementing the weak part in the characteristics of natural zeolite, it is an adsorbent consisting of only natural zeolite or a calcined zeolite alone obtained by firing it. Compared to, the performance is greatly improved, and it is almost the same as that of the activated carbon alone.

【0028】また、その製造方法においても、粉状混合
体の段階で天然有機物粉状体が天然ゼオライト粉末粒子
間に満遍なく散在した状態から、所定の範囲に水分調整
されて湿潤状として造粒される段階に、天然有機物粉状
体の周囲に天然ゼオライト粉末体がどんどん付着、充填
する結果、天然ゼオライト粉末体の中に自然に天然有機
物粉状体が内包され、それを所定温度で焼成することに
より、天然ゼオライト焼成段階で同時に天然有機物粉状
体の炭化が実施されるという簡便な手段となっていて大
量生産可能となるものである。
Also in the production method, the natural organic material powder is uniformly dispersed between the natural zeolite powder particles in the powder mixture stage, and the water content is adjusted to a predetermined range to form a wet granulation. As a result of the natural zeolite powder being adhered and filled around the natural organic powder in the step, the natural organic powder is naturally included in the natural zeolite powder, and it is fired at a predetermined temperature. According to this, carbonization of the natural organic matter powder is simultaneously performed in the natural zeolite firing step, and mass production is possible.

【0029】したがって、その吸着特性として性能的に
十分活性炭に匹敵し得る値を示すだけのものとなってい
る以上、経済的に活性炭単品からなる吸着材に比較して
遥かに安価なこの発明の吸着材は、極めて実用的な吸着
材として使用可能であり、大量に使用しなければならな
い圃場用吸着材としては勿論のこと、水質汚濁防止材、
地下水汚染防止材、脱臭等環境浄化材、あるいは生ゴミ
処理材等用の吸着材としての利用に大いに寄与すること
が可能になるという極めて秀れた特徴を発揮することが
できるものである。これらの特徴は、実施例に示す具体
的な構成のものでより一層助長されることになる。
Therefore, as far as the adsorption characteristics are such that the performance thereof is sufficiently comparable to that of activated carbon, it is economically far less expensive than the adsorbent made of activated carbon alone. The adsorbent can be used as an extremely practical adsorbent, and as a field adsorbent that must be used in a large amount, of course, a water pollution control material,
It is possible to exert an extremely excellent feature that it can greatly contribute to use as a groundwater pollution prevention material, an environmental purification material such as deodorant, or an adsorbent material for raw garbage treatment material and the like. These features will be further promoted by the concrete configuration shown in the embodiment.

【0030】叙上の如く、この発明の炭化物包含ゼオラ
イト粒からなる吸着材、およびその製造方法は、天然ゼ
オライト本来の特性を更に強化し、且つ安定して発揮す
るようにしたものであって、簡便に製造可能とするもの
であることから、その取扱性、経済性、安全性等の点
で、天然ゼオライトあるいはそれを焼成した焼成天然ゼ
オライト単品からなる吸着材は勿論のこと、活性炭単品
からなるものをも凌ぐ秀れた特徴を発揮し得るものであ
り、各種用途の吸着材およびその製造方法として高い評
価がなされるものと予想される。 │
As described above, the adsorbent comprising the carbide-containing zeolite particles and the method for producing the same according to the present invention are intended to further enhance the original properties of natural zeolite and to stably exhibit them. Since it can be easily produced, in terms of its handleability, economical efficiency, safety, etc., it is not only an adsorbent consisting of natural zeolite or a calcined natural zeolite obtained by calcining it, but it is also composed of activated carbon alone. It can exhibit excellent characteristics that surpass those of other materials, and is expected to be highly evaluated as an adsorbent for various applications and a method for producing the same. │

【表 2】 [Table 2]

【表 3】 [Table 3]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 2mm以下に粉砕した籾殻、オガ屑等の天
然有機物粉状体と250μm以下に粉砕した天然ゼオラ
イト粉末体とからなる粉状混合体に、0.01〜0.0
5%に調整したカルボキシメチルセルロースナトリウム
水溶液等、有機または無機バインダー水溶液からなる粘
結剤を注入、混合した、含水率約30%前後の湿潤粉状
混合体から造粒後、約500〜1000℃程度の焼成温
度で焼成して形成した炭化物包含焼成ゼオライト粒から
なる吸着材。
1. A powdery mixture comprising a natural organic matter powder such as rice husk and sawdust scraped to 2 mm or less and a natural zeolite powder ground to 250 μm or less, 0.01 to 0.0
About 500-1000 ° C after granulation from a wet powdery mixture having a water content of about 30%, which is prepared by injecting and mixing a binder made of an organic or inorganic binder aqueous solution such as sodium carboxymethylcellulose solution adjusted to 5%. An adsorbent material comprising carbide-containing calcined zeolite particles calcined at the calcining temperature of.
【請求項2】 250μm以下に粉砕した天然ゼオライ
ト粉末体に、2mm以下に粉砕した籾殻、オガ屑等の天然
有機物粉状体を重量部で6:4の割合の均質に混合され
た粉状混合体を形成した上、0.01〜0.05%に調
整したカルボキシメチルセルロースナトリウム水溶液
等、有機または無機バインダー水溶液からなる粘結剤を
加え、含水率約30%前後の湿潤粉状混合体としたもの
から、造粒後、約800〜1000℃程度の温度に加熱
したロータリーキルンに連続投入して焼成し、冷却した
上、粒度0.1〜10mm前後の粒状体に篩分けしてな
る、炭化物包含焼成ゼオライト粒からなる吸着材。
2. A powdery mixture in which a natural zeolite powder body crushed to 250 μm or less and a natural organic matter powder body crushed to 2 mm or less such as rice husks and sawdust is uniformly mixed in a ratio of 6: 4 by weight. After forming the body, a binder made of an organic or inorganic binder aqueous solution such as sodium carboxymethyl cellulose aqueous solution adjusted to 0.01 to 0.05% was added to obtain a wet powdery mixture having a water content of about 30%. After granulation, the powder is continuously charged into a rotary kiln heated to a temperature of about 800 to 1000 ° C., fired, cooled, and then sieved into granules having a grain size of 0.1 to 10 mm. An adsorbent consisting of calcined zeolite particles.
【請求項3】 250μm以下に粉砕した天然ゼオライ
ト粉末体に、2mm以下に粉砕した籾殻、オガ屑等の天然
有機物粉状体を重量部で6:4の割合の均質に混合され
た粉状混合体を形成した上、0.01〜0.05%に調
整したカルボキシメチルセルロースナトリウム水溶液
等、有機または無機バインダー水溶液からなる粘結剤を
加え、含水率約30%前後の湿潤粉状混合体としたもの
から、造粒後、約800〜1000℃程度の温度に加熱
したロータリーキルンで約5〜15分間前後焼成してか
ら冷却した上、分級機を経由して粒度0.1〜10mm前
後の粒状体に篩分けして製造する、炭化物包含焼成ゼオ
ライト粒からなる吸着材の製造方法。
3. A powdery mixture in which a natural zeolite powder body pulverized to 250 μm or less and a natural organic matter powder body pulverized to 2 mm or less such as rice husks and sawdust are uniformly mixed in a ratio of 6: 4 by weight. After forming the body, a binder made of an organic or inorganic binder aqueous solution such as sodium carboxymethyl cellulose aqueous solution adjusted to 0.01 to 0.05% was added to obtain a wet powdery mixture having a water content of about 30%. After granulating, granules are fired in a rotary kiln heated to a temperature of about 800 to 1000 ° C. for about 5 to 15 minutes and then cooled, and then granulated through a classifier to have a particle size of about 0.1 to 10 mm. 1. A method for producing an adsorbent comprising carbide-containing calcined zeolite particles, which is produced by sieving.
JP32137293A 1993-11-24 1993-11-24 Adsorbent consisting of carbide-containing calcined zeolite particles and its production Pending JPH07144129A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32137293A JPH07144129A (en) 1993-11-24 1993-11-24 Adsorbent consisting of carbide-containing calcined zeolite particles and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32137293A JPH07144129A (en) 1993-11-24 1993-11-24 Adsorbent consisting of carbide-containing calcined zeolite particles and its production

Publications (1)

Publication Number Publication Date
JPH07144129A true JPH07144129A (en) 1995-06-06

Family

ID=18131833

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH07144129A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013034950A (en) * 2011-08-09 2013-02-21 Mitsunori Ueda Method for producing charcoal ph buffering adjusting mixing particulate material having air permeability, water retaining property, adsorbability, ph adjusting function and method for using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013034950A (en) * 2011-08-09 2013-02-21 Mitsunori Ueda Method for producing charcoal ph buffering adjusting mixing particulate material having air permeability, water retaining property, adsorbability, ph adjusting function and method for using the same

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