JPH10165733A - Filter media - Google Patents
Filter mediaInfo
- Publication number
- JPH10165733A JPH10165733A JP8335345A JP33534596A JPH10165733A JP H10165733 A JPH10165733 A JP H10165733A JP 8335345 A JP8335345 A JP 8335345A JP 33534596 A JP33534596 A JP 33534596A JP H10165733 A JPH10165733 A JP H10165733A
- Authority
- JP
- Japan
- Prior art keywords
- filter medium
- nitrogen
- filter material
- synthetic resin
- acid
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Biological Depolymerization Polymers (AREA)
- Farming Of Fish And Shellfish (AREA)
- Biological Treatment Of Waste Water (AREA)
- Filtering Materials (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は主として鑑賞魚用水
槽、活魚保存用水槽等の循環濾過装置に用いる濾材に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter medium used for a circulating filtration device such as an aquarium for aquarium fish and an aquarium for storing live fish.
【0002】[0002]
【従来の技術】従来これらの濾材は、たとえば特開平4
−200788号公報に記載されているように珪酸カル
シウムやマグネシウム化合物、活性炭やアルミナーシリ
カ系粘土鉱物、ガラス質等の無機系多孔体およびそれら
の造粒物を一定量水槽内に投入したものである。2. Description of the Related Art Conventionally, these filter media are disclosed in
As described in -200788, a fixed amount of calcium silicate or magnesium compound, activated carbon, alumina-silica clay mineral, inorganic porous material such as vitreous, and granules thereof are charged into a water tank. is there.
【0003】[0003]
【発明が解決しようとする課題】上記従来の濾材におい
ては、水中の窒素化合物を窒素ガスに変換し水中から除
去する脱窒作用を得ようとする場合は、シュードモナス
属やバチルス属の脱窒作用を有する微生物(以下脱窒菌
とする)の水素供与体となるメタノール等(以下脱窒菌
の栄養の栄養源とする)を別途水中に添加する必要があ
った。In the above-mentioned conventional filter media, in order to obtain a denitrification effect of converting a nitrogen compound in water into nitrogen gas and removing it from water, a denitrification effect of Pseudomonas or Bacillus is required. It has been necessary to separately add methanol or the like (hereinafter, referred to as a nutrient source of the denitrifying bacteria) serving as a hydrogen donor of a microorganism having the following (hereinafter, referred to as a denitrifying bacterium) to water.
【0004】また濾材自身に水質汚染の原因となるアン
モニウムイオンやリン酸イオンを除去する機能がなかっ
た。Further, the filter medium itself has no function of removing ammonium ions and phosphate ions which cause water pollution.
【0005】本発明はこれら従来の課題を解決するもの
であり、脱窒菌の栄養源を添加する必要なく脱窒作用を
得ることができ、同時にアンモニウムイオンやリン酸イ
オンの除去性能に優れた濾材を提供することを目的とす
る。[0005] The present invention solves these conventional problems and provides a denitrifying effect without the need to add a nutrient source of denitrifying bacteria, and at the same time, a filter medium having excellent ammonium ion and phosphate ion removal performance. The purpose is to provide.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に、本発明の第1手段は、ポリビニルアルコールと澱粉
とのアロイ、乳酸重合体、ヒドロキシ酪酸とヒドロキシ
吉草酸との共重合体、ポリオール類と脂肪属ジカルボン
酸との縮合重合物、ポリ(γ−メチル−Lグルタメー
ト)、ポリ(ε−カプロラクトン)のうち少なくとも1
種類以上の合成樹脂を成形して濾材を構成するものであ
る。In order to achieve the above object, a first means of the present invention is to provide an alloy of polyvinyl alcohol and starch, a lactic acid polymer, a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a polyol, At least one selected from the group consisting of polycondensation products of fatty acids and aliphatic dicarboxylic acids, poly (γ-methyl-L-glutamate) and poly (ε-caprolactone)
More than one kind of synthetic resin is molded to constitute a filter medium.
【0007】また、本発明の第2手段は、ポリビニルア
ルコールと澱粉とのアロイ、乳酸重合体、ヒドロキシ酪
酸とヒドロキシ吉草酸との共重合体、ポリオール類と脂
肪属ジカルボン酸との縮合重合物、ポリ(γ−メチル−
Lグルタメート)、ポリ(ε−カプロラクトン)のうち
少なくとも1種類以上の合成樹脂に、ゼオライト、活性
アルミナから選ばれる少なくとも1種類以上の粉末を添
加した合成樹脂を成形して濾材を構成したものである。The second means of the present invention is an alloy of polyvinyl alcohol and starch, a lactic acid polymer, a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a condensation polymer of polyols and aliphatic dicarboxylic acid, Poly (γ-methyl-
L-glutamate), poly (ε-caprolactone) and at least one synthetic resin to which at least one powder selected from zeolite and activated alumina is added to form a synthetic resin to form a filter material. .
【0008】[0008]
【発明の実施の形態】上記各構成により、本発明の実施
の形態を以下順を追って説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described in the following order with the above-described respective configurations.
【0009】本発明の各手段を構成するポリビニルアル
コールと澱粉とのアロイは、微生物による分解性(以下
生分解性とする)を有する一般式(化1)なる構造を持
つポリビニルアルコールと[0009] The alloy of polyvinyl alcohol and starch constituting each means of the present invention comprises polyvinyl alcohol having a structure represented by the general formula (Chemical Formula 1), which is degradable by microorganisms (hereinafter referred to as biodegradable).
【0010】[0010]
【化1】 Embedded image
【0011】同じく生分解性を有する澱粉とのアロイで
あり、アロイ化することで生分解性がさらに高まり、脱
窒菌の良好な栄養源となる。[0011] Similarly, it is an alloy with starch having biodegradability. When the alloy is formed into an alloy, the biodegradability is further increased, and it is a good nutrient source for denitrifying bacteria.
【0012】さらにはアロイ化することで良好な流動性
を生み出し溶融成形加工が容易となり、濾材の形状が自
由に選択でき好ましい。[0012] Further, by forming an alloy, good fluidity is produced, and the melt forming process is facilitated, and the shape of the filter medium can be freely selected, which is preferable.
【0013】ポリビニルアルコール単体自身も生分解性
を有するが水溶性であり且つ界面活性が高いため、単体
での使用は本発明の用途からは好ましくない。Polyvinyl alcohol itself has biodegradability itself, but is water-soluble and has a high surface activity, so that use of the polyvinyl alcohol alone is not preferred for use in the present invention.
【0014】本発明の各手段を構成する乳酸重合体は、
一般式(化2)なる構造を持つ乳酸を環化反応、開環重
合を経て合成される合成樹脂であり、The lactic acid polymer constituting each means of the present invention comprises:
A synthetic resin synthesized through a cyclization reaction and ring-opening polymerization of lactic acid having a structure represented by the general formula (Formula 2),
【0015】[0015]
【化2】 Embedded image
【0016】生分解性が高く脱窒菌の良好な栄養源とな
る。さらには溶融成形加工が容易であり、濾材の形状が
自由に選択でき好ましい。It is highly biodegradable and is a good nutrient source for denitrifying bacteria. Further, the melt molding process is easy, and the shape of the filter medium can be freely selected, which is preferable.
【0017】本発明の各手段を構成するヒドロキシ酪酸
とヒドロキシ吉草酸をの共重合体は、一般式(化3)な
る構造を持つヒドロキシ酪酸と、The copolymer of hydroxybutyric acid and hydroxyvaleric acid constituting each means of the present invention comprises hydroxybutyric acid having a structure represented by the general formula (Formula 3):
【0018】[0018]
【化3】 Embedded image
【0019】一般式(化4)なる構造を持つヒドロキシ
吉草酸との共重合体であり、A copolymer with hydroxyvaleric acid having a structure represented by the general formula (4):
【0020】[0020]
【化4】 Embedded image
【0021】生分解性が高く、脱窒菌の良好な栄養源と
なる。さらには溶融成形加工が容易であり、濾材の形状
が自由に選択でき好ましい。It has high biodegradability and is a good nutrient source for denitrifying bacteria. Further, the melt molding process is easy, and the shape of the filter medium can be freely selected, which is preferable.
【0022】本発明の各手段を構成するポリオール類と
脂肪族ジカルボン酸との縮合重合物は、1.4−ブタジ
オール等のポリオール類と、コハク酸、アジピン酸等の
脂肪族ジカルボン酸との縮合重合により得られる脂肪属
ポリステルであり、生分解性が高く、脱窒菌の良好な栄
養源となる。The condensation polymer of a polyol and an aliphatic dicarboxylic acid constituting each means of the present invention is obtained by condensation of a polyol such as 1.4-butadiol with an aliphatic dicarboxylic acid such as succinic acid or adipic acid. It is an aliphatic polyester obtained by polymerization, has high biodegradability, and is a good nutrient source for denitrifying bacteria.
【0023】さらには溶融成形加工が容易であり、濾材
の形状が自由に選択でき好ましい。本発明の各手段を構
成するポリ(γ−メチル−Lグルタメート)は、一般式
(化5)なる構造を持ち、生分解性が高く、脱窒菌の良
好な栄養源となる。Further, the melt molding process is easy, and the shape of the filter medium can be freely selected, which is preferable. The poly (γ-methyl-L-glutamate) constituting each means of the present invention has a structure represented by the general formula (Formula 5), has high biodegradability, and is a good nutrient source for denitrifying bacteria.
【0024】[0024]
【化5】 Embedded image
【0025】さらには溶融成形加工が容易であり、濾材
の形状が自由に選択でき好ましい。本発明の各手段を構
成するポリ(ε−カプロラクトン)は、一般式(化6)
なる構造を持ち、生分解性が高く、脱窒菌の良好な栄養
源となる。Further, the melt molding process is easy, and the shape of the filter medium can be freely selected, which is preferable. The poly (ε-caprolactone) constituting each means of the present invention has the general formula (Chem. 6)
It is highly biodegradable and is a good source of nutrients for denitrifying bacteria.
【0026】[0026]
【化6】 Embedded image
【0027】さらには溶融成形加工が容易であり、濾材
の形状が自由に選択でき好ましい。つぎに、本発明の第
2手段を構成するゼオライトは、三次元骨格構造を有す
る結晶性アルミノケイ酸塩であり、天然ゼオライト及び
合成ゼオライトのいずれも用いることができる。代表的
はゼオライトの例としては,A−型ゼオライト,X−型
ゼオライト,Y−型ゼオライト,P−型ゼオライト,高
シリカゼオライト,ソーダライト,モルデナイト,アナ
ルサイム,クリノブチロライト,チャバサイト,エリオ
ナイト等を挙げることができる。Further, the melt molding process is easy, and the shape of the filter medium can be freely selected, which is preferable. Next, the zeolite constituting the second means of the present invention is a crystalline aluminosilicate having a three-dimensional skeleton structure, and either a natural zeolite or a synthetic zeolite can be used. Representative examples of zeolites include A-type zeolite, X-type zeolite, Y-type zeolite, P-type zeolite, high silica zeolite, sodalite, mordenite, analcyme, clinobutyrolite, chabazite, erionite. And the like.
【0028】これらゼオライトは特に水中のアンモニウ
ムイオンをイオン交換により効果的に除去できる。These zeolites can particularly effectively remove ammonium ions in water by ion exchange.
【0029】また、本発明の第2手段を構成する活性ア
ルミナとは、酸化アルミニウムを700゜C以下の温度
において三水和物を脱水して得られるγ−アルミナを主
成分とし、飽和の炭化水素を除くほとんどあらゆる化合
物を吸着し、特に水中のリン酸イオンを効果的に吸着除
去できる。The activated alumina constituting the second means of the present invention is mainly composed of γ-alumina obtained by dehydrating aluminum oxide at a temperature of 700 ° C. or less, and containing saturated γ-alumina. It can adsorb almost any compound except hydrogen, and can effectively adsorb and remove particularly phosphate ions in water.
【0030】これら生分解性の高い合成樹脂で濾材を形
成することにより、濾材本来の基本機能である脱窒菌の
住処を提供するのみならず、脱窒菌の栄養源も同時に供
給することが可能となる。By forming the filter medium with these highly biodegradable synthetic resins, it is possible not only to provide a place for denitrifying bacteria, which is the basic function of the filter medium, but also to supply a nutrient source of the denitrifying bacteria at the same time. Become.
【0031】さらには、これら生分解性の高い樹脂にゼ
オライトを添加し濾材を構成することで、水中のアンモ
ニウムイオンが吸着除去され、脱窒作用による窒素除去
と相乗的に作用し水中の総窒素を低減できる。Further, by adding zeolite to these highly biodegradable resins to form a filter medium, ammonium ions in water are adsorbed and removed, and act synergistically with the removal of nitrogen by denitrification to produce total nitrogen in water. Can be reduced.
【0032】また、これら生分解性の高い樹脂に活性ア
ルミナを添加し濾材を構成することで、水中のリン酸イ
オンを効果的に低減できる。Further, by adding activated alumina to these highly biodegradable resins to constitute a filter material, phosphate ions in water can be effectively reduced.
【0033】これら生分解性の高い合成樹脂にゼオライ
トや活性アルミナを添加し濾材を構成した場合、脱窒菌
により分解された合成樹脂は、より低分子量の有機物
(モノマー等)となり濾材表面から欠落、除去されるた
め、常に新鮮なゼオライトや活性アルミナの表面が水中
に露出することとなり、アンモニウムイオンやリン酸イ
オンの除去効率が一層向上する。When zeolite or activated alumina is added to these highly biodegradable synthetic resins to form a filter material, the synthetic resin decomposed by the denitrifying bacterium becomes a lower molecular weight organic substance (monomer, etc.) and is dropped from the filter material surface. Since it is removed, the surface of fresh zeolite and activated alumina is always exposed in water, and the efficiency of removing ammonium ions and phosphate ions is further improved.
【0034】[0034]
【実施例】以下、本発明の具体例について説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Specific examples of the present invention will be described below.
【0035】なお、本発明はこれらの具体例に限定され
るものではない。 (実施例1)ポリビニルアルコールと澱粉とのアロイの
代表例として、商品名マタービーAI05H(日本合成
化学工業株式会社製)を用い、外径10mm、内径4mm、
長さ10mmの円筒状濾材を射出溶融成形法(溶融温度約
165゜C)により得た。The present invention is not limited to these specific examples. (Example 1) As a typical example of an alloy of polyvinyl alcohol and starch, trade name Materby AI05H (manufactured by Nippon Synthetic Chemical Industry Co., Ltd.) was used.
A cylindrical filter medium having a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 165 ° C).
【0036】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中に入れ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated with an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen, and nitrate. The time change of the nitrogen concentration was measured.
【0037】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表1)に示す。The results are shown in Table 1 as a comparative example together with a filter medium comprising calcium silicate and a magnesium compound (corresponding to a conventional filter medium).
【0038】[0038]
【表1】 [Table 1]
【0039】(表1)から明らかなように、本実施例1
の濾材は比較例1に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is apparent from Table 1, the present embodiment 1
Since the filter medium has a more effective denitrifying effect and releases nitrite ions as nitrogen gas as compared with Comparative Example 1, the concentration of nitrite nitrogen is extremely low. It can be seen that the concentration of nitrogen is also small.
【0040】(実施例2)乳酸重合体の代表例として、
商品名ラクティ(株式会社島津製作所)を用い、外径1
0mm、内径4mm、長さ10mmの円筒状濾材を射出溶融成
形法(溶融温度約160゜C)により得た。Example 2 As a typical example of a lactic acid polymer,
Using the product name Rakuti (Shimadzu Corporation), outer diameter 1
A cylindrical filter medium having a diameter of 0 mm, an inner diameter of 4 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 160 ° C.).
【0041】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen and nitrate. The time change of the nitrogen concentration was measured.
【0042】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表2)に示す。The results are shown in Table 2 together with a filter material comprising calcium silicate and a magnesium compound (corresponding to a conventional filter material) as a comparative example.
【0043】[0043]
【表2】 [Table 2]
【0044】(表2)から明らかなように、本実施例2
の濾材は比較例2に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is evident from (Table 2), the present embodiment 2
The filter medium has a denitrifying effect more effective than that of Comparative Example 2 and releases nitrite ions as nitrogen gas. Therefore, the concentration of nitrite nitrogen is remarkably low. It can be seen that the concentration of nitrogen is also small.
【0045】(実施例3)ヒドロキシ酪酸とヒドロキシ
吉草酸との共重合体の代表例として、商品名バイオポー
ルD311G(日本モンサント株式会社製)を用い、外
径10mm、内径4mm、長さ10mmの円筒状濾材を射出溶
融成形法(溶融温度約170゜C)により得た。(Example 3) As a typical example of a copolymer of hydroxybutyric acid and hydroxyvaleric acid, Biopol D311G (trade name, manufactured by Monsanto Japan Limited) was used and had an outer diameter of 10 mm, an inner diameter of 4 mm, and a length of 10 mm. A cylindrical filter medium was obtained by an injection melt molding method (melting temperature about 170 ° C).
【0046】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by a pump of 8 L / min to circulate ammonia nitrogen, nitrite nitrogen and nitrate. The time change of the nitrogen concentration was measured.
【0047】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表3)に示す。The results are shown in Table 3 as a comparative example together with a filter medium comprising calcium silicate and a magnesium compound (corresponding to a conventional filter medium).
【0048】[0048]
【表3】 [Table 3]
【0049】(表3)から明らかなように、本実施例3
の濾材は比較例3に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is clear from Table 3, the present embodiment 3
The filter medium has a denitrification effect more effective than Comparative Example 3, and releases nitrite ions as nitrogen gas. Therefore, the concentration of nitrite nitrogen is extremely low. It can be seen that the concentration of nitrogen is also small.
【0050】(実施例4)ポリオール類と脂肪族ジカル
ボン酸との縮合重合物の代表例として、商品名ビオノー
レ#1020(昭和高分子株式会社製)を用い、外径1
0mm、内径4mm、長さ10mmの円筒状濾材を射出溶融成
形法(溶融温度約170゜C)により得た。(Example 4) As a typical example of a condensation polymer of a polyol and an aliphatic dicarboxylic acid, trade name Bionore # 1020 (manufactured by Showa Polymer Co., Ltd.) was used.
A cylindrical filter medium having a diameter of 0 mm, an inner diameter of 4 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 170 ° C.).
【0051】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen and nitrate. The time change of the nitrogen concentration was measured.
【0052】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表4)に示す。The results are shown in Table 4 together with a filter medium comprising calcium silicate and a magnesium compound (corresponding to a conventional filter medium) as a comparative example.
【0053】[0053]
【表4】 [Table 4]
【0054】(表4)から明らかなように、本実施例4
の濾材は比較例4に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is clear from (Table 4), the present embodiment 4
Since the filter medium has a more effective denitrifying effect and releases nitrite ions as nitrogen gas as compared with Comparative Example 4, the concentration of nitrite nitrogen is remarkably low. It can be seen that the concentration of nitrogen is also small.
【0055】(実施例5)ポリ(γ−メチル−Lグルタ
メート)の代表例として、商品名アジコートA−200
0(味の素株式会社製)を用い、外径10mm、内径4m
m、長さ10mmの円筒状濾材を射出溶融成形法(溶融温
度約155゜C)により得た。(Example 5) As a typical example of poly (γ-methyl-L-glutamate), trade name Ajiquat A-200 is used.
0 (manufactured by Ajinomoto Co., Inc.), outer diameter 10 mm, inner diameter 4 m
A cylindrical filter medium having a length of 10 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 155 ° C.).
【0056】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by a pump of 8 L / min to circulate ammonia nitrogen, nitrite nitrogen, nitrate. The time change of the nitrogen concentration was measured.
【0057】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表5)に示す。The results are shown in Table 5 as a comparative example together with a filter medium comprising calcium silicate and a magnesium compound (corresponding to a conventional filter medium).
【0058】[0058]
【表5】 [Table 5]
【0059】(表5)から明らかなように、本実施例5
の濾材は比較例5に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As apparent from (Table 5), this embodiment 5
In the filter medium of the present invention, the denitrification effect works more effectively and the nitrite ions are released as nitrogen gas as compared with Comparative Example 5, so that the concentration of nitrite nitrogen is remarkably low. It can be seen that the concentration of nitrogen is also small.
【0060】(実施例6)ポリ(ε−カプロラクトン)
の代表例として商品名プラクセルH−4(ダイセル化学
株式会社製)を用い、外径10mm、内径4mm、長さ10
mmの円筒状濾材を射出溶融成形法(溶融温度約155゜
C)により得た。Example 6 Poly (ε-caprolactone)
As a typical example, a trade name of Placcel H-4 (manufactured by Daicel Chemical Co., Ltd.) is used.
mm cylindrical filter media were obtained by injection melt molding (melting temperature about 155 ° C).
【0061】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen and nitrate. The time change of the nitrogen concentration was measured.
【0062】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表6)に示す。The results are shown in Table 6 together with a filter material comprising calcium silicate and a magnesium compound (corresponding to a conventional filter material) as a comparative example.
【0063】[0063]
【表6】 [Table 6]
【0064】(表6)から明らかなように、本実施例6
の濾材は比較例6に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is clear from Table 6, this embodiment 6
In the filter medium of the present invention, since the denitrification function works more effectively and the nitrite ions are released as nitrogen gas as compared with Comparative Example 6, the concentration of nitrite nitrogen is extremely low. It can be seen that the concentration of nitrogen is also small.
【0065】(実施例7)乳酸重合体の代表例として、
商品名ラクティ(株式会社島津製作所製)を50重量
%、ヒドロキシ酪酸とヒドロキシ吉草酸との共重合体の
代表例として、商品名バイオポールD311G(日本モ
ンサント株式会社製)を50重量%ををペレット状態で
混合し、40mm単軸押し出し機を用いて単一混合物(ペ
レット状)を得た。Example 7 As a typical example of a lactic acid polymer,
Pellets 50% by weight of trade name Lacty (manufactured by Shimadzu Corporation) and 50% by weight of trade name Biopol D311G (manufactured by Nippon Monsanto Co., Ltd.) as a representative example of a copolymer of hydroxybutyric acid and hydroxyvaleric acid The mixture was mixed in a state, and a single mixture (pellet) was obtained using a 40 mm single screw extruder.
【0066】本単一混合物を用い外径10mm、内径4m
m、長さ10mmの円筒状濾材を射出溶融成形法(溶融温
度約165゜C)により得た。Using this single mixture, outer diameter 10 mm, inner diameter 4 m
A cylindrical filter medium having a length of 10 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 165 ° C.).
【0067】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is placed in 100 L of water previously adjusted to a concentration of 10 ppm as ammonium nitrogen using ammonium chloride, and water is circulated by an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen, and nitrate. The time change of the nitrogen concentration was measured.
【0068】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表7)に示す。The results are shown in Table 7 together with a filter material comprising calcium silicate and a magnesium compound (corresponding to a conventional filter material) as a comparative example.
【0069】[0069]
【表7】 [Table 7]
【0070】(表7)から明らかなように、本実施例7
の濾材は比較例7に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出するため、亜硝酸体窒素
の濃度が著しく小さく、その結果亜硝酸イオンの酸化に
よって生ずる硝酸体窒素の濃度も小さいことがわかる。As is clear from (Table 7), this embodiment 7
In the filter medium of the present invention, the denitrification effect works more effectively and the nitrite ions are released as nitrogen gas as compared with Comparative Example 7, so that the concentration of nitrite nitrogen is extremely low. It can be seen that the concentration of nitrogen is also small.
【0071】(実施例8)ヒドロキシ酪酸とヒドロキシ
吉草酸との共重合体の代表として、商品名バイオポール
D311G(日本モンサント株式会社製)に、平均粒径
約3μmの天然ゼオライトと40mm単軸押し出し機を用
いて16重量%添加した。Example 8 As a representative of a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a natural zeolite having an average particle size of about 3 μm and a uniaxial extrusion of 40 mm were applied to Biopol D311G (trade name, manufactured by Monsanto Japan Limited). 16% by weight was added using a mixer.
【0072】本樹脂60gを用いて外径10mm、内径4
mm、長さ10mmの円筒状濾材を射出溶融成形法(溶融温
度約170゜C)により得た。An outer diameter of 10 mm and an inner diameter of 4
A cylindrical filter medium having a length of 10 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 170 ° C.).
【0073】本濾材60gを、塩化アンモニウムを用い
アンモニア体窒素として10ppmの濃度にあらかじめ
調整した水100L中にいれ、8L/分のポンプで水を
循環させアンモニア体窒素、亜硝酸体窒素、硝酸体窒素
濃度の時間変化を測定した。60 g of the present filter medium is put into 100 L of water previously adjusted to a concentration of 10 ppm as ammonia nitrogen using ammonium chloride, and water is circulated by an 8 L / min pump to circulate ammonia nitrogen, nitrite nitrogen and nitrate. The time change of the nitrogen concentration was measured.
【0074】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表8)に示す。The results are shown in Table 8 together with a filter material comprising calcium silicate and a magnesium compound (corresponding to a conventional filter material) as a comparative example.
【0075】[0075]
【表8】 [Table 8]
【0076】(表8)から明らかなように、本実施例8
の濾材は比較例8に比して脱窒作用が有効に働き、亜硝
酸イオンを窒素ガスとして放出すること、および濾材に
添加したゼオライトがアンモニウムイオンを効果的に水
中から除去するために、亜硝酸体窒素の濃度が著しく小
さく、その結果亜硝酸イオンの酸化によって生ずる硝酸
体窒素の濃度も小さいことがわかる。As is clear from Table 8, this embodiment 8
The filter medium has a denitrification effect more effective than Comparative Example 8, releases nitrite ions as nitrogen gas, and the zeolite added to the filter medium effectively removes ammonium ions from water. It can be seen that the concentration of nitrate nitrogen is extremely low, and as a result, the concentration of nitrate nitrogen generated by oxidation of nitrite ions is also low.
【0077】(実施例9)ヒドロキシ酪酸とヒドロキシ
吉草酸との共重合体の代表例として、商品名バイオポー
ルD311G(日本モンサント株式会社製)に、平均粒
径約3μmの天然ゼオライトと平均粒径1μmの活性ア
ルミナを40mm単軸押し出し機を用いてそれぞれ16重
量%添加した。Example 9 As a typical example of a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a natural zeolite having an average particle size of about 3 μm and an average particle size of Biopol D311G (manufactured by Monsanto Japan Limited) were used. 1 μm of activated alumina was added in an amount of 16% by weight using a 40 mm single screw extruder.
【0078】本樹脂60gを用いて外径10mm、内径4
mm、長さ10mmの円筒状濾材を射出溶融成形法(溶融温
度約170゜C)により得た。An outer diameter of 10 mm and an inner diameter of 4
A cylindrical filter medium having a length of 10 mm and a length of 10 mm was obtained by an injection melt molding method (melting temperature: about 170 ° C.).
【0079】本濾材60gを、塩化アンモニウムとリン
酸二水素ナトリウムを用いアンモニア体窒素として10
ppm、リン酸体リンとして12ppmの濃度にあらか
じめ調整した水100L中にいれ、8L/分のポンプで
水を循環させアンモニア体窒素、亜硝酸体窒素、硝酸体
窒素、リン酸体リン濃度の時間変化を測定した。[0079] 60 g of the present filter medium was converted into ammonia nitrogen using ammonium chloride and sodium dihydrogen phosphate.
ppm, phosphoric acid phosphorus, put in 100 L of water adjusted to a concentration of 12 ppm in advance, circulate water with a pump of 8 L / min, and simulate ammonia ammonia, nitrite nitrogen, nitrate nitrogen, phosphate phosphorus concentration time The change was measured.
【0080】結果を、比較例として珪酸カルシウムとマ
グネシウム化合物からなる濾過材(従来技術の濾材に相
当)とともに(表9)に示す。The results are shown in Table 9 as a comparative example together with a filter medium comprising calcium silicate and a magnesium compound (corresponding to a conventional filter medium).
【0081】[0081]
【表9】 [Table 9]
【0082】(表9)から明らかなように、本実施例9
の濾材は比較例9に比して脱窒作用が有効に働き亜硝酸
イオンを窒素ガスとして放出すること、および濾材に添
加したゼオライトがアンモニウムイオンを効果的に水中
から除去するために、亜硝酸体窒素の濃度が著しく小さ
く、その結果亜硝酸イオンの酸化によって生ずる硝酸体
窒素の濃度も小さいことがわかる。As apparent from (Table 9), the present embodiment 9
The filter medium of the present invention has a denitrifying effect more effective than that of Comparative Example 9 to release nitrite ions as nitrogen gas, and the zeolite added to the filter medium effectively removes ammonium ions from water. It can be seen that the concentration of body nitrogen is extremely low, and as a result, the concentration of nitrate nitrogen generated by oxidation of nitrite ions is also small.
【0083】さらに濾材に添加した活性アルミナがリン
イオンを効果的に水中から除去するために、リン酸体リ
ンの濃度が比較例9に比して著しく小さいことがわか
る。Further, since the activated alumina added to the filter medium effectively removes phosphorus ions from water, it can be seen that the concentration of phosphoric acid phosphorus is significantly lower than that of Comparative Example 9.
【0084】なお、本実施例1ないし9に用いた濾材の
形状は円筒状としたが、濾材の形状はこれに限定するも
のではない。Although the shape of the filter medium used in Examples 1 to 9 is cylindrical, the shape of the filter medium is not limited to this.
【0085】また、本実施例8,9に用いたゼオライト
の添加量は16重量%としたが、ゼオライトの添加量は
これに限定するものではなく、要求されるアンモニア低
減効果、水量の諸条件により任意に変更可能である。The amount of zeolite used in Examples 8 and 9 was 16% by weight. However, the amount of zeolite added is not limited to this, and the required ammonia reduction effect and various conditions for the amount of water are required. Can be changed arbitrarily.
【0086】また、本実施例9に用いた活性アルミナの
添加量は16重量%としたが、活性アルミナの添加量は
これに限定するものではなく、要求されるリン濃度低減
効果、水量の諸条件により任意に変更可能である。The amount of activated alumina used in Example 9 was set at 16% by weight, but the amount of activated alumina added is not limited to this. It can be arbitrarily changed according to conditions.
【0087】[0087]
【発明の効果】以上のように本発明の各手段によれば、
ポリビニルアルコールと澱粉とのアロイ、乳酸重合体、
ヒドロキシ酪酸とヒドロキシ吉草酸との共重合体、ポリ
オール類と脂肪族ジカルボン酸との縮合重合物、ポリ
(γ−メチル−Lグルタメート)、ポリ(ε−カプロラ
クトン)のうち少なくとも1種類以上の合成樹脂を成形
した濾材を構成したものであり、さらにはポリビニルア
ルコールと澱粉とのアロイ、乳酸重合体、ヒドロキシ酪
酸とヒドロキシ吉草酸との共重合体、ポリオール類と脂
肪族ジカルボンとの縮合重合物、ポリ(γ−メチル−L
グルタメート)、ポリ(ε−カプロラクトン)のうち少
なくとも1種類以上の合成樹脂に、ゼオライト、活性ア
ルミナから選ばれる少なくとも1種類以上の粉末を添加
した合成樹脂を成形して濾材を構成したもので、脱窒菌
の栄養を添加する必要なく脱窒作用を得ることができ、
さらには、同時にアンモニウムイオンやリン酸イオンの
除去性能に優れるという効果を奏するものである。As described above, according to each means of the present invention,
Alloy of polyvinyl alcohol and starch, lactic acid polymer,
Synthetic resin of at least one of a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a condensation polymer of polyols and aliphatic dicarboxylic acid, poly (γ-methyl-L-glutamate) and poly (ε-caprolactone) An alloy of polyvinyl alcohol and starch, a lactic acid polymer, a copolymer of hydroxybutyric acid and hydroxyvaleric acid, a condensation polymer of polyols and an aliphatic dicarboxylic acid, (Γ-methyl-L
Glutamate), poly (ε-caprolactone), and at least one synthetic resin added with at least one powder selected from zeolite and activated alumina to form a synthetic resin to form a filter material. Denitrification can be obtained without the need to add nutrients for nitrifying bacteria,
Further, it has an effect of being excellent in the performance of removing ammonium ions and phosphate ions at the same time.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C02F 3/10 C02F 3/10 A ──────────────────────────────────────────────────続 き Continued on front page (51) Int.Cl. 6 Identification code FI C02F 3/10 C02F 3/10 A
Claims (2)
乳酸重合体、ヒドロキシ酪酸とヒドロキシ吉草酸との共
重合体、ポリオール類と脂肪族ジカルボン酸との縮合重
合物、ポリ(γ−メチル−Lグルタメート)、ポリ(ε
−カプロラクトン)のうち少なくとも1種類以上の合成
樹脂を成形した濾材。An alloy of polyvinyl alcohol and starch,
Lactic acid polymer, copolymer of hydroxybutyric acid and hydroxyvaleric acid, condensation polymer of polyols and aliphatic dicarboxylic acid, poly (γ-methyl-L-glutamate), poly (ε
-Caprolactone) of at least one synthetic resin.
乳酸重合体、ヒドロキシ酪酸とヒドロキシ吉草酸との共
重合体、ポリオール類と脂肪族ジカルボン酸との縮合重
合物、ポリ(γ−メチル−Lグルタメート)、ポリ(ε
−カプロラクトン)の少なくとも1種類以上の合成樹脂
に、ゼオライト、活性アルミナから選ばれる少なくとも
1種類以上の粉末を添加した合成樹脂を成形した濾材。2. An alloy of polyvinyl alcohol and starch,
Lactic acid polymer, copolymer of hydroxybutyric acid and hydroxyvaleric acid, condensation polymer of polyols and aliphatic dicarboxylic acid, poly (γ-methyl-L-glutamate), poly (ε
-Caprolactone) formed from a synthetic resin obtained by adding at least one kind of powder selected from zeolite and activated alumina to at least one kind of synthetic resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8335345A JPH10165733A (en) | 1996-12-16 | 1996-12-16 | Filter media |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8335345A JPH10165733A (en) | 1996-12-16 | 1996-12-16 | Filter media |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH10165733A true JPH10165733A (en) | 1998-06-23 |
Family
ID=18287491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8335345A Pending JPH10165733A (en) | 1996-12-16 | 1996-12-16 | Filter media |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH10165733A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000254687A (en) * | 1999-03-08 | 2000-09-19 | Taisei Corp | Groundwater purification method |
| WO2001070637A1 (en) * | 2000-03-24 | 2001-09-27 | Japan Science And Technology Corporation | Method for direct clarification of ground water polluted with nitrate |
| JP2002136991A (en) * | 2000-11-07 | 2002-05-14 | Taisei Corp | Denitrification treatment method |
| WO2002094015A3 (en) * | 2001-04-26 | 2004-01-22 | Tetra Gmbh | Denitrification of aquarium water with the aid of polycaprolactone |
| US8372895B2 (en) * | 2006-06-30 | 2013-02-12 | Scil Technology Gmbh | Biomaterial containing degradation stabilized polymer |
-
1996
- 1996-12-16 JP JP8335345A patent/JPH10165733A/en active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000254687A (en) * | 1999-03-08 | 2000-09-19 | Taisei Corp | Groundwater purification method |
| WO2001070637A1 (en) * | 2000-03-24 | 2001-09-27 | Japan Science And Technology Corporation | Method for direct clarification of ground water polluted with nitrate |
| US6926831B2 (en) | 2000-03-24 | 2005-08-09 | Japan Science And Technology Corporation | Method for direct clarification of groundwater polluted with nitrate |
| JP2002136991A (en) * | 2000-11-07 | 2002-05-14 | Taisei Corp | Denitrification treatment method |
| WO2002094015A3 (en) * | 2001-04-26 | 2004-01-22 | Tetra Gmbh | Denitrification of aquarium water with the aid of polycaprolactone |
| JP2004526460A (en) * | 2001-04-26 | 2004-09-02 | テトラ・ゲーエムベーハー | Denitrification of aquarium water |
| US7244358B2 (en) | 2001-04-26 | 2007-07-17 | Tetra Gmbh | Denitrification of aquarium water |
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