JP2733889B2 - Method for producing porous ceramic-based remover for pesticides and phosphate ions - Google Patents

Method for producing porous ceramic-based remover for pesticides and phosphate ions

Info

Publication number
JP2733889B2
JP2733889B2 JP5100200A JP10020093A JP2733889B2 JP 2733889 B2 JP2733889 B2 JP 2733889B2 JP 5100200 A JP5100200 A JP 5100200A JP 10020093 A JP10020093 A JP 10020093A JP 2733889 B2 JP2733889 B2 JP 2733889B2
Authority
JP
Japan
Prior art keywords
porous ceramic
pesticides
pesticide
remover
zeolite
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
Application number
JP5100200A
Other languages
Japanese (ja)
Other versions
JPH06285366A (en
Inventor
令治 加藤
憲人 渡辺
章夫 大江
邦雄 野村
哲志 岩下
克己 上村
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.)
GIFUKEN
Yahashi Kogyo KK
Original Assignee
GIFUKEN
Yahashi Kogyo 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 GIFUKEN, Yahashi Kogyo KK filed Critical GIFUKEN
Priority to JP5100200A priority Critical patent/JP2733889B2/en
Publication of JPH06285366A publication Critical patent/JPH06285366A/en
Application granted granted Critical
Publication of JP2733889B2 publication Critical patent/JP2733889B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05GMIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
    • C05G3/00Mixtures of one or more fertilisers with additives not having a specially fertilising activity
    • C05G3/80Soil conditioners

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Soil Sciences (AREA)
  • Pest Control & Pesticides (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、ゴルフ場等で用いられ
ている農薬と肥料の流出防止などを目的とした多孔質セ
ラミック系除去剤に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a porous ceramic remover for preventing outflow of pesticides and fertilizers used in golf courses and the like.

【0002】[0002]

【従来の技術】従来、ゴルフ場の芝を病虫害から守り、
育成するために多量の殺虫剤、除草剤、および殺菌剤な
らびに肥料が使用されている。都道府県の行政機関で
は、農薬による環境汚染を防止するために農薬の適正使
用と農薬の総量規制を指導している。一方、民間企業で
は、各種の農薬対策商品や除去システムを販売してい
る。このうち対策商品については、多種類の農薬を直ち
に除去でき、しかも永年にわたり除去効果を維持できる
ものは少ない。最近、二酸化珪素、酸化カルシウム、酸
化アルミニウム、酸化鉄、酸化マンガン、酸化マグネシ
ウム、酸化カリウムからなる金属酸化物を焼成してなる
多孔質焼結体に活性炭等の吸着物質を配合した農薬吸着
分解剤が見られる(特開平4−110035号公報)
が、多種類の農薬について必ずしも長期間にわたり除去
効果を期待することはできそうにない。また、農薬、栄
養塩類の同時除去については全く対策商品がないのが現
状である。さらに、除去システムについては、システム
の導入とその維持管理に経済的な負荷も大きいのが現状
である。
2. Description of the Related Art Conventionally, golf course turf has been protected from pests and insects,
Large amounts of insecticides, herbicides, and fungicides and fertilizers are used to grow. Prefectural governments provide guidance on the proper use of pesticides and the total amount of pesticides to prevent environmental pollution from pesticides. On the other hand, private companies sell a variety of pesticide products and removal systems. Among them, few of the countermeasure products can remove many kinds of pesticides immediately and can maintain the removal effect for many years. Recently, a pesticide adsorbing and decomposing agent in which an adsorbing substance such as activated carbon is blended into a porous sintered body obtained by firing a metal oxide composed of silicon dioxide, calcium oxide, aluminum oxide, iron oxide, manganese oxide, magnesium oxide, and potassium oxide (Japanese Patent Laid-Open No. 4-10035)
However, it is unlikely that many kinds of pesticides can be expected to have long-term removal effects. At the present time, there is no countermeasure product for simultaneous removal of pesticides and nutrients. Furthermore, with regard to the removal system, the introduction of the system and the maintenance and management thereof have a large economic load at present.

【0003】[0003]

【発明が解決しようとする課題】現在、多種類の農薬を
永年にわたり除去できる対策商品は、市販されていな
い。本発明は、ゴルフ場等からの農薬および肥料の流出
を未然に防止し環境を保全するために、農薬およびリン
の除去機能に優れ、しかも農薬については永年にわたり
除去効果を発揮する多孔質セラミック系除去剤を提供す
るものである。
At present, there is no commercially available countermeasure product capable of removing many kinds of pesticides for many years. The present invention is a porous ceramic system which is excellent in the function of removing pesticides and phosphorus in order to prevent the outflow of pesticides and fertilizers from golf courses and the like and to preserve the environment, and which exhibits an effect of removing pesticides for many years. It provides a remover.

【0004】[0004]

【課題を解決するための手段】本発明の多孔質セラミッ
ク系除去剤の製造方法は、下記の(A)過程あるいは更
に(B)および(C)成分を配合する過程を含むことを
特徴とする。 (A) 炭酸カルシウムと粘土を含む石灰石水洗ケーキ
を母体とし、これに真珠岩、黒曜石、松脂岩、バーミュ
キュライト等の鉱物系発泡材、さらにフライアッシュ、
ゼオライト等のシリカ系粉体を配合し、成形後に前記発
泡材の発泡温度以上で焼成して多孔質ヤラミックを得る
過程 (B) 顆粒状ゼオライトと、 (C) 活性炭または木炭とを前記多孔質セラミックに
配合する過程
Porous method for producing a ceramic-based scavengers SUMMARY OF THE INVENTION The present invention is characterized in that it comprises the step of mixing the (A) process, or even (B) and (C) the following components . (A) A limestone washed cake containing calcium carbonate and clay is used as a base, and mineral-based foaming materials such as perlite, obsidian, pine stone, vermiculite, and fly ash,
A silica-based powder such as zeolite is blended, and fired at a foaming temperature or higher of the foamed material after molding to obtain a porous yaramic.
Process (B) Granular zeolite and (C) activated carbon or charcoal are added to the porous ceramic.
Mixing process

【0005】[0005]

【発明の作用】本発明の多孔質セラミック系除去剤は、
農薬およびリン酸イオンあるいは更に硝酸イオンを選択
的に吸着・除去する機能を有しており、吸着された農薬
については生分解機能と加水分解機能があいまって、簡
便な施工により多種類の農薬を効果的に除去するもので
ある。とりわけ、本発明の(A)多孔質セラミックは、
農薬およびリン酸イオンの除去機能に優れており、吸着
された農薬は分解・除去されるため、通常の使用におい
ては、吸着された農薬が破過容量に達することは希であ
るので、永年にわたり除去効果を発揮することが可能に
なった。また、(B)顆粒状ゼオライトはリン酸イオン
の固定と農薬の加水分解機能に優れており、一方、
(C)活性炭は硝酸イオンの吸着に優れている。
The porous ceramic-based remover of the present invention comprises:
It has the function of selectively adsorbing and removing pesticides and phosphate ions or nitrate ions.The adsorbed pesticides have a biodegradation function and a hydrolysis function. It effectively removes them. In particular, the (A) porous ceramic of the present invention comprises:
It is excellent in removing pesticides and phosphate ions.Adsorbed pesticides are decomposed and removed.In normal use, adsorbed pesticides rarely reach breakthrough capacity. The removal effect can be exhibited. In addition, (B) granular zeolite is excellent in phosphate ion fixation and pesticide hydrolysis functions.
(C) Activated carbon is excellent in adsorbing nitrate ions.

【0006】[0006]

【発明の実施態様】DESCRIPTION OF THE PREFERRED EMBODIMENTS

(A)多孔質セラミックの原材料の母材をなす石灰石水
洗ケーキは、石灰石採掘後の水洗選鉱工程より発生する
ものである。即ち、石灰石を水洗すると、微細粒の粘
土、石灰石粉を含んだスラリーが発生する。これをシッ
クナー(沈澱槽)で沈澱させた後、フィルタープレス
(加圧脱水装置)等で脱水したものであり、約70%以
上の石灰石粉と約30%以下の粘土粉を含んでいる。
(A) The limestone washed cake which is a base material of the raw material of the porous ceramic is generated from the washing and beneficiation process after limestone mining. That is, when limestone is washed with water, a slurry containing fine-grained clay and limestone powder is generated. This is precipitated in a thickener (precipitation tank) and then dehydrated by a filter press (pressure dehydrator) or the like, and contains about 70% or more of limestone powder and about 30% or less of clay powder.

【0007】一方、鉱物系発泡材としては、鉱物系であ
って、焼結温度で発泡して多孔質セラミックを形成する
ものであればいずれも用いられるが、真珠岩、黒曜岩、
松脂岩等の真珠岩類、バーミュキュライトなどが好適に
用いられる。真珠岩類は、火山岩の一種でガラス質より
成り、800〜1000℃に加熱すると発泡する特性を
もっている。
On the other hand, any mineral-based foaming material may be used as long as it is a mineral-based material and foams at a sintering temperature to form a porous ceramic.
Pearlites such as pine resin, vermiculite, and the like are preferably used. Pearlites are a kind of volcanic rock, made of glass, and have the property of foaming when heated to 800 to 1000 ° C.

【0008】シリカ系粉体としては、フライアッシュ、
ゼオライトなどが挙げられる。フライアッシュとして
は、火力発電所等より発生する石炭系の普通のフライア
ッシュでよい。ゼオライトは天然ゼオライトでも合成ゼ
オライトでもよい。
[0008] As the silica-based powder, fly ash,
Zeolite and the like can be mentioned. As fly ash, ordinary coal-based fly ash generated from a thermal power plant or the like may be used. The zeolite may be a natural zeolite or a synthetic zeolite.

【0009】石灰石水洗ケーキ(A−1)、発泡材(A
−2)およびシリカ系粉体(A−3)の配合重量比は、
(A−1):(A−2):(A−3)=40〜60:1
0〜30:10〜40が好適であり、より好ましくは4
5〜55:15〜25:25〜35である。
[0009] Limestone washed cake (A-1), foamed material (A
-2) and the silica-based powder (A-3) are:
(A-1): (A-2): (A-3) = 40-60: 1.
0 to 30:10 to 40 are preferable, and 4 is more preferable.
5-55: 15-25: 25-35.

【0010】上記の石灰石水洗ケーキ、発泡材およびシ
リカ系粉体の各成分は混合された後、造粒される。造粒
には特にバインダーを必要とせず、適切量の水分があれ
ば普通の造粒機で造粒できる。
The components of the limestone washed cake, the foaming material, and the silica-based powder are mixed and then granulated. No particular binder is required for granulation, and granulation can be performed with an ordinary granulator if there is an appropriate amount of water.

【0011】造粒物を、発泡材の発泡温度以上、例えば
1100〜1300℃位の温度で焼成すると多孔質セラ
ミックとなり、農薬およびリン酸イオンに優れた除去機
能を持つセラミック系除去剤が得られる。
When the granulated material is fired at a temperature equal to or higher than the foaming temperature of the foaming material, for example, at a temperature of about 1100 to 1300 ° C., a porous ceramic is obtained, and a ceramic-based remover having an excellent removing function for pesticides and phosphate ions can be obtained. .

【0012】本発明の多孔質セラミックの粒径は、その
使用場所に応じて適宜選定され、例えば、芝土中に添加
する場合は透水性を考慮して1.5〜5mm径のものが
好ましく、集水マンホールなどで用いられる場合は5〜
15mm径のものが好ましい。
The particle size of the porous ceramic of the present invention is appropriately selected according to the place of use. For example, when added to turf soil, the particle size is preferably 1.5 to 5 mm in consideration of water permeability. , 5 for water collection manholes
Those having a diameter of 15 mm are preferred.

【0013】(B)成分の顆粒状ゼオライトとしては、
フライアッシュを原料としカセイソーダを使用して水熱
合成されたゼオライトを塩化カルシウム水溶液で処理し
た低アルカリの合成ゼオライト造粒品が適しているが、
他の合成ゼオライトあるいは天然ゼオライト造粒物ない
しは顆粒品を用いてもよい。
As the granular zeolite of the component (B),
Low alkali synthetic zeolite granules obtained by treating zeolite hydrothermally synthesized with fly ash as raw material and using caustic soda with an aqueous solution of calcium chloride are suitable,
Other synthetic or natural zeolite granules or granules may be used.

【0014】(C)成分としては、椰子ガラ類や、コー
クス等の石炭類を原料とした活性炭類が用いられる。ま
た、バーク材、ひのき等を原料とした木炭を用いてもよ
い。
As the component (C), activated charcoal made from coconut palms or coals such as coke is used. Alternatively, charcoal made of bark, hinoki, or the like may be used.

【0015】本発明の(B)顆粒状ゼオライトおよび
(C)活性炭の粒径は、その使用場所に応じて適宜選定
され、例えば、芝土中に添加する場合は透水性を考慮し
て1.5〜5mm径のものが好ましく、集水マンホール
などで用いられる場合は5〜15mm径のものが好まし
い。
The particle size of the granular zeolite (B) and the activated carbon (C) of the present invention is appropriately selected according to the place of use. Those having a diameter of 5 to 5 mm are preferable, and those having a diameter of 5 to 15 mm when used in a water collecting manhole or the like are preferable.

【0016】(A)多孔質セラミック、(B)粒状ゼオ
ライトおよび(C)活性炭または木炭は、要求される機
能・使用目的に応じて適宜配合比率を決定すればよい
が、重量比で(A):(B):(C)=10〜30:3
0〜50:30〜50の範囲が好適である。
The mixing ratio of (A) the porous ceramic, (B) the granular zeolite, and (C) the activated carbon or charcoal may be appropriately determined according to the required function and purpose of use. : (B): (C) = 10 to 30: 3
A range of 0 to 50:30 to 50 is preferred.

【0017】本発明の多孔質セラミック系除去剤の施工
方法としては、床土中に添加する方法、床土中に層状に
設置する方法、集水管や集水ピットに設置する方法およ
び調整池に設置する方法などがあり、これらの方法はい
ずれも簡便である。
The method for applying the porous ceramic-based remover of the present invention includes a method of adding it to floor soil, a method of installing it in a layer in floor soil, a method of installing it in a water collecting pipe and a water collecting pit, and a method of adjusting a pond. There are methods for installation, and all of these methods are simple.

【0018】[0018]

【発明の効果】本発明の多孔質セラミック系除去剤は農
薬およびリン酸イオンを除去する機能を併せ有している
が、特に加水分解機能に優れており、吸着された多種類
の農薬を速やかに分解・除去する効果を有している。ま
た、農薬を長期にわたり生分解する機能を有するもので
ある。したがって、当初より農薬除去効果の変動がな
く、長期にわたり効果が期待できるものである。
The porous ceramic-based remover of the present invention has both the function of removing pesticides and phosphate ions, but is particularly excellent in the hydrolysis function, and can quickly remove many kinds of adsorbed pesticides. It has the effect of decomposing and removing. It also has a function of biodegrading pesticides for a long period of time. Therefore, there is no change in the pesticide removal effect from the beginning, and the effect can be expected for a long time.

【0019】特に、本発明の多孔質セラミック系除去剤
は後述の実施例1,2に示すように、農薬分解能が優れ
ており、吸着を主体とする市販品よりもはるかに長期に
わたり、その除去効能を維持できるものである。また、
実施例3に示すように、リン酸イオンに対して非常に優
れた除去機能を示す。
In particular, as shown in Examples 1 and 2 below, the porous ceramic-based remover of the present invention has excellent pesticide decomposability, and its removal is much longer than a commercial product mainly comprising adsorption. The effect can be maintained. Also,
As shown in Example 3, it shows a very excellent removal function for phosphate ions.

【0020】さらに、顆粒状ゼオライトおよび活性炭を
併用することにより、農薬およびリン酸イオンの除去機
能がいっそう助長されるとともに、硝酸イオン等の窒素
の除去機能が改善され、栄養塩類を総合的に除去するこ
とができる。
Further, the combined use of granular zeolite and activated carbon further promotes the function of removing pesticides and phosphate ions, improves the function of removing nitrogen such as nitrate ions, and comprehensively removes nutrients. can do.

【0021】また、保水力、通気性、透水性、保肥力等
の物理的、化学的性質に優れているので、床土の改良に
も効果があり、また、施工も簡便である。以下に本発明
の実施例を挙げて具体的に説明するが、本発明は、その
主旨を超えない限りにおいて、以下の実施例に限定され
るものではない。
Further, since it is excellent in physical and chemical properties such as water retention, air permeability, water permeability, fertilization, etc., it is effective for improving the floor soil and the construction is simple. Hereinafter, the present invention will be described specifically with reference to Examples, but the present invention is not limited to the following Examples as long as the gist of the present invention is not exceeded.

【0022】[0022]

【実施例】【Example】

実施例1 石灰石水洗フィルターケーキ60重量部、黒曜石20重
量部およびフライアッシュ20重量部を混合造粒したの
ち、1200℃で焼成して粒径0.7〜1.0mmの本
発明の多孔質セラミック系除去剤を得た。
Example 1 After mixing and granulating 60 parts by weight of a limestone-washed filter cake, 20 parts by weight of obsidian and 20 parts by weight of fly ash, the porous ceramic of the present invention having a particle size of 0.7 to 1.0 mm was fired at 1200 ° C. A system remover was obtained.

【0023】実施例2 石灰石水洗フィルターケーキ50重量部、黒曜石30重
量部およびフライアッシュ20重量部を混合造粒したの
ち、1200℃で焼成して粒径0.7〜1.0mmの本
発明の多孔質セラミック系除去剤を得た。
Example 2 A mixture of 50 parts by weight of a limestone-washed filter cake, 30 parts by weight of obsidian and 20 parts by weight of fly ash was mixed and granulated, and then calcined at 1200 ° C. to obtain a particle having a particle size of 0.7 to 1.0 mm. A porous ceramic-based remover was obtained.

【0024】実施例3 フライアッシュをアルカリ熱水加工して得られたゼオラ
イトを塩化カルシウム水溶液を用いてカルシウム置換
し、さらにセメントをバインダーに用いて造粒し、平均
粒径1.5〜5mmの顆粒状ゼオライトを製造した。こ
の顆粒状ゼオライト30重量部、排水処理に用いられる
活性炭(平均粒径3〜5mm)30重量部および実施例
2と同様にして得た粒径3〜5mmの多孔質セラミック
30重量部を均一混合して本発明の多孔質セラミック系
除去剤(実施例3品)を得た。
Example 3 Zeolite obtained by subjecting fly ash to alkaline hot water processing was replaced with calcium using an aqueous solution of calcium chloride, and further granulated using cement as a binder to give an average particle size of 1.5 to 5 mm. A granular zeolite was produced. 30 parts by weight of this granular zeolite, 30 parts by weight of activated carbon (average particle size 3 to 5 mm) used for wastewater treatment and 30 parts by weight of a porous ceramic having a particle size of 3 to 5 mm obtained in the same manner as in Example 2 are uniformly mixed. Thus, a porous ceramic-based remover of the present invention (Example 3 product) was obtained.

【0025】実験例1:農薬除去機能(室内カラム試
験) ゴルフ場で汎用されている農薬を用いた。即ち、殺菌剤
としてクロロネブ、イソプロチオラン、フルトラニル、
イプロジオン、TPN、除草剤としてプロピザミド、シ
マジン(CAT)、殺虫剤としてフェニトロチオン(M
EP)、イソキサチオン、ダイアジノンを選定した。
Experimental Example 1: Pesticide removal function (indoor column test) A pesticide commonly used in golf courses was used. That is, as a fungicide chloroneb, isoprothiolane, flutranil,
Iprodione, TPN, propizamide, simazine (CAT) as herbicide, fenitrothion (M
EP), isoxathion, and diazinon were selected.

【0026】断面積0.78cm2 のカラムに本発明の
実施例1の多孔質セラミック系除去剤あるいは比較対照
としての活性炭を3g積層し、表1に示した流入液濃度
の溶液を1時間当たり25mlの速度で約520mlを
連続的に流し、20.75時間後に流出液中の平均農薬
濃度を測定し、その結果を表1に示した。
3 g of the porous ceramic-based remover of Example 1 of the present invention or activated carbon as a control was laminated on a column having a cross-sectional area of 0.78 cm 2 , and a solution having an influent concentration shown in Table 1 was added per hour. About 520 ml was continuously flowed at a speed of 25 ml, and after 20.75 hours, the average pesticide concentration in the effluent was measured. The results are shown in Table 1.

【0027】[0027]

【表1】表1:農薬除去効果 流出液濃度(mg/l) 調査対象農薬名 流入液濃度(mg/l) 実施例1品 活 性 炭 クロロネブ 94.0 8.52 8.59 イソプラチオラン 328 7.11 31.2 フルトラニル 223 7.01 21.2 イプロジオン 2020 6.42 187 TPN 789 23.3 78.0 CAT 1325 23.6 127 プロピザミド 287 14.5 27.4 MEP 1040 20.3 100 イソキサチオン 1040 7.03 98.6 ダイアジノン 650 16.8 60.1 Table 1 Table 1: Pesticide removal effect effluent concentration (mg / l) Name of pesticide to be investigated Influent concentration (mg / l) Example 1 product Active chloroneb charcoal 94.0 8.52 8.59 Isoplatiolan 328 7.11 31.2 Flutolanil 223 7.01 21.2 Iprodione 2020 6.42 187 TPN 789 23.3 78.0 CAT 1325 23.6 127 Propisamide 287 14.5 27.4 MEP 1040 20.3 100 Isoxathion 1040 7.03 98.6 Diazinon 650 16.8 60.1

【0028】以上の実験結果を見ても、本発明による多
孔質セラミック系除去剤は汎用されている活性炭に比べ
農薬除去に優れていることが分かる。
From the above experimental results, it can be seen that the porous ceramic-based remover according to the present invention is superior to the widely used activated carbon in removing pesticides.

【0029】実験例2:農薬除去機能(室内カラム試
験) 断面積0.78cm2 のカラムに本発明の実施例2の多
孔質セラミック系除去剤あるいは比較対照としての市販
農薬吸着剤を3g積層し、表2に示した流入液濃度の溶
液を1時間当たり32mlの速度で約720mlを連続
的に流し、22.5時間後に流出液中の平均農薬濃度を
測定し、その結果を表2に示した。
Experimental Example 2: Pesticide removal function (indoor column test) 3 g of the porous ceramic-based remover of Example 2 of the present invention or a commercially available pesticide adsorbent as a control was laminated on a column having a sectional area of 0.78 cm 2. Approximately 720 ml of the solution having the influent concentration shown in Table 2 was flowed continuously at a rate of 32 ml per hour, and the average pesticide concentration in the effluent was measured after 22.5 hours. The results are shown in Table 2. Was.

【0030】[0030]

【表2】表2:農薬除去効果 流出液濃度(mg/l) 調査対象農薬名 流入液濃度(mg/l) 実施例2品 市販農薬吸着剤 クロロネブ 2.98 0.587 0.551 イソプラチオラン 2.67 0.398 0.429 フルトラニル 2.12 0.478 0.559 イプロジオン 1.50 0.293 0.391 TPN 5.26 1.02 1.86 CAT 11.1 4.26 4.12 プロピザミド 4.86 1.76 1.89 MEP 3.03 0.292 0.348 イソキサチオン 1.83 0.306 0.461 ダイアジノン 2.71 0.445 0.347 [Table 2] Table 2: Pesticide removal effect effluent concentration (mg / l) Name of pesticide to be surveyed Influent concentration (mg / l) Example 2 product Commercially available pesticide adsorbent chloroneb 2.98 0.587 0.551 isoprathiolane 2.67 0.398 0.429 Flutolanil 2.12 0.478 0.559 Iprodione 1.50 0.293 0.391 TPN 5.26 1.02 1.86 CAT 11.1 4.26 4.12 Propisamide 4.86 1.76 1.89 MEP 3.03 0.292 0.348 Isoxathion 1.83 0.306 0.461 Diazinon 2.71 0.445 0.347

【0031】以上の実験結果を見ても、本発明による多
孔質セラミック系除去剤は市販の農薬吸着剤に比べ農薬
除去に優れていることが分かる。
From the above experimental results, it can be seen that the porous ceramic-based remover of the present invention is superior in removing pesticides as compared with a commercially available pesticide adsorbent.

【0032】実験例3:リン吸着能 断面積0.78cm2 のカラムに表3に示したそれぞれ
の試料を3g積層し、肥料成分としてPO4−P (リン
酸態リン)を含む肥料(芝グリーンP,大塚化学(株)
製)の溶液を891μg/cm2 の量で添加し、30m
mの降雨に相当する量の水を流し、流出液中の肥料成分
を測定して肥料成分の流出量を求め、その結果を表3に
示した。
Experimental Example 3: Phosphorus adsorbing ability 3 g of each of the samples shown in Table 3 were stacked on a column having a cross-sectional area of 0.78 cm 2 , and fertilizer (turf) containing PO 4 -P (phosphate phosphorus) as a fertilizer component Green P, Otsuka Chemical Co., Ltd.
Was added in an amount of 891 μg / cm 2 , and 30 m
The amount of fertilizer outflow was determined by measuring the amount of fertilizer component in the effluent by flowing water in an amount corresponding to m rainfall. The results are shown in Table 3.

【0033】[0033]

【表3】表3:リン吸着能 流出量(μg/cm2 試 料 肥 料 成 分 実施例2品 市販農薬吸着剤 活 性 炭 PO4−P <1 134 378 TABLE 3: Phosphor adsorption capacity runoff ([mu] g / cm 2) specimen fertilizer Ingredient Example 2 dishes commercial pesticide adsorbent activated carbon PO 4 -P <1 134 378

【0034】以上の実験結果を見ても、本発明の多孔質
セラミック系除去剤によるリン酸イオン吸着能は、市販
の農薬吸着剤および活性炭に比べ非常に優れていること
が分かる。
From the above experimental results, it can be understood that the phosphate ion-adsorbing ability of the porous ceramic-based remover of the present invention is much superior to the commercially available agricultural chemical adsorbent and activated carbon.

【0035】実験例4:農薬除去能(圃場実験) 幅2m×奥行2mの実験圃場の底部に配水管を設け、厚
さ5cmの除去剤を敷設しその上部に中部地方のゴルフ
場で汎用されているサバ土と木曽砂の混合されたものを
30cm敷き芝を植生した後、農薬の除去実験を行なっ
た。
Experimental Example 4: Pesticide removal ability (field experiment) A water pipe is provided at the bottom of an experimental field having a width of 2 m and a depth of 2 m, a remover having a thickness of 5 cm is laid, and the upper part thereof is widely used in golf courses in the Chubu region. After mixing a mixture of mackerel soil and Kiso sand, the grass was spread 30 cm and vegetated, and an experiment on removing pesticides was performed.

【0036】農薬の散布は表4に示す農薬濃度で1m2
当たり1リットルの割合で散布し、1日後に時間降雨3
0mmに相当する水を実験圃場に均一に散布し、配水管
より排出された水を分析した。除去剤として、本発明の
実施例3の多孔質セラミック系除去剤および市販農薬吸
着剤を用い、流出液中の農薬濃度を測定し、その結果を
表4に示した。
The spraying of the pesticide was performed at the pesticide concentration shown in Table 4 at 1 m 2.
Spray at a rate of 1 liter per hour.
Water equivalent to 0 mm was evenly sprayed on the experimental field, and the water discharged from the water distribution pipe was analyzed. Using the porous ceramic-based remover of Example 3 of the present invention and a commercially available pesticide adsorbent as the remover, the concentration of the pesticide in the effluent was measured, and the results are shown in Table 4.

【0037】[0037]

【表4】表4:農薬除去実験結果(実験圃場) 散布濃度 市販農薬吸着剤 農 薬 名 (mg/l) 実施例3品 市販農薬吸着剤 フルトラニル 212 1.3 16.3 イプロジオン 299 <0.0 16.2 CAT 802 0.7 31.0 プロピザミド 453 0.4 19.2 MEP 350 <0.0 <0.0 ダイアジノン 305 <0.0 0.1 Table 4: Pesticide removal experiment results (experimental field) Spray concentration Commercial pesticide adsorbent Pesticide name (mg / l) Example 3 product Commercial pesticide adsorbent Flutranil 212 1.3 16.3 Iprodione 299 <0.0 16.2 CAT 802 0.7 31.0 Propizamide 453 0.4 19.2 MEP 350 <0.0 <0.0 Diazinon 305 <0.0 0.1

【0038】以上の実験結果を見ても、本発明による多
孔質セラミック系除去剤は、市販の農薬吸着剤に比べ農
薬の除去にいかに優れているかが分かる。
From the above experimental results, it can be seen how the porous ceramic-based remover according to the present invention is superior in removing pesticides as compared with a commercially available pesticide adsorbent.

【0039】実験例5:肥料成分除去能(カラム実験) 本発明の多孔質セラミック系除去剤として実施例3で調
製したものを用いる他は、実験例3と同様にして肥料成
分の除去能力を試験し、その結果を表5に示す。
Experimental Example 5: Ability to remove fertilizer components (column experiment) Except that the porous ceramic-based remover of the present invention prepared in Example 3 was used, the ability to remove fertilizer components was the same as in Experimental Example 3. The test was performed and the results are shown in Table 5.

【0040】[0040]

【表5】表5:肥料除去実験結果 添加量 除去率(%) 肥 料 成 分 (μg/cm2) 実施例3品 市販農薬吸着剤 NH4−N 692 67.4 66.7 NO3−N 647 96.8 97.0 PO4−P 891 99.3 84.9 Table 5: Fertilizer removal experiment results Addition removal rate (%) Fertilizer component (μg / cm 2 ) Example 3 product Commercially available agricultural chemical adsorbent NH 4 -N 692 67.4 66.7 NO 3 -N 647 96.8 97.0 PO 4 -P 891 99.3 84.9

【0041】以上の実験結果を見ても、本発明による多
孔質セラミック系除去剤は、市販の農薬吸着剤に比べ栄
養塩類の除去にいかに優れているかが分かる。
From the above experimental results, it can be seen how the porous ceramic-based remover of the present invention is superior in removing nutrients as compared with a commercially available agricultural chemical adsorbent.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 岩下 哲志 岐阜県大垣市青墓町3−410−20 (72)発明者 上村 克己 岐阜県大垣市昼飯町377−17 (56)参考文献 特開 昭61−263636(JP,A) ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Tetsushi Iwashita 3-410-20, Aoto-machi, Ogaki City, Gifu Prefecture (72) Katsumi Uemura 377-17, Lunch Town, Ogaki City, Gifu Prefecture (56) References JP 61 -263636 (JP, A)

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 炭酸カルシウムと粘土を含む石灰石水洗
ケーキを母体とし、これに真珠岩、黒曜石、松脂岩、バ
ーミュキュライト等の鉱物系発泡材、さらにフライアッ
シュ、ゼオライト等のシリカ系粉体を配合し、成形後に
前記発泡材の発泡温度以上で焼成して多孔質セラミック
を得る過程を含むことを特徴とする農薬およびリン酸イ
オンの多孔質セラミック系除去剤の製造方法
1. A limestone washing cake containing calcium carbonate and clay is used as a base material, and mineral-based foaming materials such as perlite, obsidian, pine stone, and vermiculite, and silica-based powders such as fly ash and zeolite are used. Is mixed and fired at a foaming temperature or higher of the foamed material after molding to form a porous ceramic.
A process for producing a porous ceramic-based remover for pesticides and phosphate ions , comprising the step of obtaining
【請求項2】 (A) 炭酸カルシウムと粘土を含む石
灰石水洗ケーキを母体とし、これに真珠岩、黒曜石、松
脂岩、バーミュキュライト等の鉱物系発泡材、さらにフ
ライアッシュ、ゼオライト等のシリカ系粉体を配合し、
成形後に前記発泡材の発泡温度以上で焼成して多孔質セ
ラミックを得る過程と、 (B) 顆粒状ゼオライトと、 (C) 活性炭または木炭とを 前記多孔質セラミックに配合する過程とを含む ことを特
徴とする農薬およびリン酸イオンの多孔質セラミック系
除去剤の製造方法
(A) A limestone washing cake containing calcium carbonate and clay is used as a base material, and mineral-based foaming materials such as perlite, obsidian, pine stone, vermiculite, etc., and silica such as fly ash, zeolite, etc. System powder
After molding, the porous material is fired at a temperature equal to or higher than the foaming temperature of the foamed material.
A step of obtaining a lamic; and a step of blending (B) granular zeolite ; and (C) activated carbon or charcoal into the porous ceramic, wherein the porous ceramic-based remover for pesticides and phosphate ions is provided. Manufacturing method .
JP5100200A 1993-04-01 1993-04-01 Method for producing porous ceramic-based remover for pesticides and phosphate ions Expired - Fee Related JP2733889B2 (en)

Priority Applications (1)

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Applications Claiming Priority (1)

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JP2733889B2 true JP2733889B2 (en) 1998-03-30

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KR100330255B1 (en) * 2000-02-26 2002-03-25 서현숙 Composition of inorganic coagulant for water treatment
US7514002B1 (en) * 2007-11-09 2009-04-07 Hokuriku Electric Power Company Method for removing phosphorus and method for reutilizing recovered phosphorus
KR101297642B1 (en) * 2011-05-23 2013-08-19 주식회사 부강테크 Media with Calcium Carbonate, and Wastewater Processing Applicance employing the same

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JPS61263636A (en) * 1985-05-17 1986-11-21 Ube Ind Ltd Calcium silicate series water treating agent
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