JP2017057327A - Polyurethane foam for water treatment carrier - Google Patents

Polyurethane foam for water treatment carrier Download PDF

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JP2017057327A
JP2017057327A JP2015184584A JP2015184584A JP2017057327A JP 2017057327 A JP2017057327 A JP 2017057327A JP 2015184584 A JP2015184584 A JP 2015184584A JP 2015184584 A JP2015184584 A JP 2015184584A JP 2017057327 A JP2017057327 A JP 2017057327A
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polyether polyol
water
polyurethane foam
polyol
water treatment
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JP6625849B2 (en
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尚哉 是佐
Naoya Koresa
尚哉 是佐
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Achilles Corp
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Abstract

PROBLEM TO BE SOLVED: To provide a polyurethane foam for water treatment carrier having high submergence without specific post-processing on a carrier itself.SOLUTION: There is provided a polyurethane foam for water treatment carrier consisting of a polyol component, an isocyanate component, a catalyst, a foaming agent and a foam stabilizer, wherein the polyol component contains polyether polyol (I) having a number average molecular weight of 3000 to 5000, an average functional group number of 2 to 4 and an ethylene oxide percentage content of 60% or more, and polyether polyol (II) having a number average molecular weight of 2000 to 4000, an average functional group number of 2 to 4 and an ethylene oxide percentage content of 20% or less, ratio of the polyether polyol (I) and the polyether polyol (II) is, by weight ratio, polyether polyol (I)/polyether polyol (II)=60 to 90%/40 to 10%, the isocyanate component is diphenylmethane diisocyanate, and submergence is 600 seconds or less.SELECTED DRAWING: Figure 1

Description

本発明は排水中に浸漬して使用される水処理担体に用いられるポリウレタンフォームに関する。   The present invention relates to a polyurethane foam used for a water treatment carrier used by being immersed in waste water.

排水処理としては、微生物による生物処理方法があり、該方法は、一般家庭や工場施設、産業施設等から排出される排水を溜めた処理槽に、微生物を担持する担体を浸漬し、該微生物の働きを利用して排水を処理することを特徴としている。   As a wastewater treatment, there is a biological treatment method using microorganisms, which involves immersing a carrier supporting microorganisms in a treatment tank in which wastewater discharged from general households, factory facilities, industrial facilities, etc. is stored. It is characterized by treating the wastewater using its function.

前記生物処理方法としては、樹脂発泡体からなる水処理担体を、浄化槽等に設けられた曝気槽中等(以下処理槽と記載)に投入・配設し、樹脂発泡体の内部に微生物を繁殖・担持(以下定着と記載)させ、前記樹脂発泡体に保持された微生物により、汚水中の有機物を分解させるといった処理方法である。   As the biological treatment method, a water treatment carrier made of a resin foam is placed in and disposed in an aeration tank provided in a septic tank or the like (hereinafter referred to as a treatment tank), and microorganisms are propagated inside the resin foam. This is a treatment method in which organic matter in wastewater is decomposed by microorganisms supported (hereinafter referred to as fixing) and held by the resin foam.

前記処理方法において、樹脂発泡体を用いる理由としては、表面積が大きく、微生物が樹脂発泡体のセルの表面に生物膜を効率よく形成しやすいため、汚水の処理能力を高めることができることが挙げられる。なお、前記樹脂発泡体としては、例えば、ポリオレフィン系樹脂発泡体やポリウレタン系樹脂発泡体等が挙げられる。   In the treatment method, the reason why the resin foam is used is that the surface area is large and microorganisms can easily form a biofilm on the surface of the cell of the resin foam. . Examples of the resin foam include polyolefin resin foam and polyurethane resin foam.

しかし、前記樹脂発泡体であるポリウレタンフォームは一般的に親水性が低く、水に馴染み難い上、発泡気泡(セル)によって内部に空気を保持している。この為、処理槽に樹脂発泡体からなる10mm程度のサイコロ状の担体を投入しても、水面下に沈み難く、比重等も低いため水面上に山のように浮かんでしまい易い。結果として、担体に排水が浸漬し、攪拌により排水中を旋回しだすまで長い時間を必要とし、ものによっては水面上に数日間浮き続けるものもあった。生物処理法による排水処理において、担体が排水中に浸漬しないことには、担体に微生物が定着せず、安定した排水の処理性能が得られない。従って、担体の排水へ投入した時点から浸漬するまでに要する時間(以下沈水性と記載)をより短縮することが求められていた。   However, the polyurethane foam, which is the resin foam, generally has low hydrophilicity and is not easily adapted to water, and air is held inside by foamed cells (cells). For this reason, even if a 10-mm dice carrier made of a resin foam is put into the treatment tank, it is difficult to sink below the surface of the water, and the specific gravity and the like are low, so that it tends to float on the surface of the water. As a result, it took a long time for the waste water to be immersed in the carrier and swirled through the waste water by stirring, and depending on the thing, it continued to float on the water surface for several days. In the wastewater treatment by the biological treatment method, if the carrier is not immersed in the wastewater, microorganisms do not settle on the carrier and stable wastewater treatment performance cannot be obtained. Accordingly, there has been a demand for further shortening the time (hereinafter referred to as submergence) required from the time when the carrier is put into the waste water until it is immersed.

前記問題を解決するために、発泡体のセルを粗くし、またセル膜を除去(除膜処理)し、発泡体内部への排水の侵入性を向上させたもの(特許文献1)や、無機系繊維、無機系微粒子、金属繊維、金属微粒子、合成樹脂等の見かけ比重向上材を塗布したり、イソシアネート末端ポリウレタンプレポリマーを付着・硬化させたりして見かけ比重を調整することなどが行われてきた(特許文献2、特許文献3)。   In order to solve the above problems, the foam cell is roughened, the cell membrane is removed (film removal treatment), and the drainage into the foam is improved (Patent Document 1), inorganic It has been performed to adjust the apparent specific gravity by applying an apparent specific gravity improver such as fiber, inorganic fine particle, metal fiber, metal fine particle or synthetic resin, or by adhering and curing an isocyanate-terminated polyurethane prepolymer. (Patent Document 2, Patent Document 3).

特開2004−250593号公報JP 2004-250593 A 特開2002−292385号公報JP 2002-292385 A 特開2010−119979号公報JP 2010-119979 A

特許文献1のように、除膜処理を施すことで、発泡体の通水性は向上し、物理的に水を通し易くはなったが、発泡体自体の疎水性により浸漬にかかる時間の短縮は十分とは言えず、また、セル膜を除去した結果として、微生物を担持し難くなるという問題もあった。 一方、見かけ比重を向上させている特許文献2や特許文献3は、樹脂等を担体の一面に塗布していることにより該箇所の排水の侵入性が低下し、浸漬の時間短縮が不十分であることに加え、実際に使用する際、すなわち処理槽内において攪拌されている際等に前記比重向上のために付着させている素材が脱落し、担体自体が水を汚す原因になるといった問題もあった。   As in Patent Document 1, by removing the film, the water permeability of the foam is improved, and it is easy to physically pass water. However, the time required for immersion is shortened due to the hydrophobicity of the foam itself. It was not sufficient, and there was also a problem that it became difficult to support microorganisms as a result of removing the cell membrane. On the other hand, in Patent Document 2 and Patent Document 3 in which the apparent specific gravity is improved, the penetration property of the drainage of the portion is lowered by applying a resin or the like on one surface of the carrier, and the dipping time is not sufficiently shortened. In addition to the above, when actually used, that is, when being stirred in the treatment tank, there is a problem that the material attached to improve the specific gravity falls off, causing the carrier itself to pollute the water. there were.

本発明は、上記問題点を解決し、担体自体に後処理を施さずに高い沈水性を有する水処理担体用ポリウレタンフォームを提供することを目的とする。   An object of the present invention is to solve the above-mentioned problems and to provide a polyurethane foam for a water treatment carrier having high water settling without post-treatment of the carrier itself.

上記課題を解決するために、本発明の水処理担体用のポリウレタンフォームは、(1)ポリオール成分、イソシアネート成分、触媒、発泡剤、整泡剤からなり、前記ポリオール成分は、数平均分子量が3000〜5000、平均官能基数が2〜4、エチレンオキサイド含有率が60%以上であるポリエーテルポリオール(I)と、数平均分子量が2000〜4000、平均官能基数が2〜4、エチレンオキサイド含有率が20%以下であるポリエーテルポリオール(II)とを含み、前記ポリエーテルポリオール(I)と前記ポリエーテルポリオール(II)の比率が、重量比で、ポリエーテルポリオール(I)/ポリエーテルポリオール(II)=60〜90%/40〜10%で、また、前記イソシアネート成分が、ジフェニルメタンジイソシアネートであり、沈水性が600秒以下であることを特徴とする。
更に、(2)セル数が25〜45個/25mmで、且つ通気量が3ml/cm/s以上とするとより好ましい。
In order to solve the above problems, the polyurethane foam for a water treatment carrier of the present invention comprises (1) a polyol component, an isocyanate component, a catalyst, a foaming agent, and a foam stabilizer, and the polyol component has a number average molecular weight of 3000. To 5000, polyether polyol (I) having an average number of functional groups of 2 to 4, ethylene oxide content of 60% or more, number average molecular weight of 2000 to 4000, average number of functional groups of 2 to 4, ethylene oxide content of The polyether polyol (II) is 20% or less, and the ratio of the polyether polyol (I) to the polyether polyol (II) is, by weight ratio, polyether polyol (I) / polyether polyol (II ) = 60-90% / 40-10%, and the isocyanate component is diphenylmethane dii A cyanate, characterized in that submerged resistance is less than 600 seconds.
Furthermore, (2) It is more preferable that the number of cells is 25 to 45 cells / 25 mm and the air flow rate is 3 ml / cm 2 / s or more.

本発明の水処理担体用ポリウレタンフォームは、発泡体に特別な後処理を施すことなく沈水性が非常に高い。従って、本発明の水処理担体用ポリウレタンフォームを用いれば、水処理担体を処理槽に投入した後、速やかに浸漬し、微生物の定着段階へ速やかに移行することができる。この為、従来の水処理担体と比較し、安定した水処理性能を発揮するまでに要する時間を大きく短縮することができる。   The polyurethane foam for a water treatment carrier of the present invention has very high water settling without subjecting the foam to a special post-treatment. Therefore, if the polyurethane foam for a water treatment carrier of the present invention is used, the water treatment carrier can be quickly immersed in the treatment tank and then quickly transferred to the microorganism fixing stage. For this reason, compared with the conventional water treatment support | carrier, the time required to exhibit the stable water treatment performance can be shortened greatly.

沈水性を説明するための参考図である。It is a reference figure for explaining submergence.

以下に本発明の水処理担体用ポリウレタンフォームに関し、図を用いて詳細に説明する。   Hereinafter, the polyurethane foam for a water treatment carrier of the present invention will be described in detail with reference to the drawings.

図1にて沈水性試験の参考図を示している。本発明における「沈水性」とは、排水上に水処理担体を投入してから、該水処理担体が水中へ沈む性質を指す。   FIG. 1 shows a reference diagram of the submersion test. The “water subsidence” in the present invention refers to the property that the water treatment carrier sinks into water after the water treatment carrier is put on the waste water.

本発明の水処理担体用ポリウレタンフォームは、ポリオール成分、イソシアネート成分、発泡剤、整泡剤、触媒からなる原料を混合・発泡させてなり、沈水性が600秒以下である。   The polyurethane foam for a water treatment carrier of the present invention is obtained by mixing and foaming raw materials comprising a polyol component, an isocyanate component, a foaming agent, a foam stabilizer, and a catalyst, and has a water settling of 600 seconds or less.

前記ポリオール成分としては、ポリエーテルポリオール(I)と、ポリエーテルポリオール(II)との少なくとも2種を含む。   As said polyol component, at least 2 sort (s) of polyether polyol (I) and polyether polyol (II) is included.

ポリエーテルポリオール(I)は、数平均分子量が3000〜5000、平均官能基数が2〜4、エチレンオキサイド含有率が60%以上である。また、前記EO含有率は70%以上が好ましい。   Polyether polyol (I) has a number average molecular weight of 3000 to 5000, an average number of functional groups of 2 to 4, and an ethylene oxide content of 60% or more. The EO content is preferably 70% or more.

ポリエーテルポリオール(II)と、数平均分子量が2000〜4000、平均官能基数が2〜4、エチレンオキサイド含有率が20%以下である。 The polyether polyol (II) has a number average molecular weight of 2000 to 4000, an average number of functional groups of 2 to 4, and an ethylene oxide content of 20% or less.

前記ポリエーテルポリオール(I)とポリエーテルポリオール(II)の配合比率は、ポリエーテルポリオール(I)とポリエーテルポリオール(II)の合計量を100重量%とした場合に、ポリエーテルポリオール(I)/ポリエーテルポリオール(II)が60〜90%/40〜10%である。
また、ポリオール成分中のEO含有率を45〜68%とするとより好ましい。EO含有率が高すぎる場合、コラップスが生じ易く、一方、低すぎる場合は、発泡する際に収縮が起こり易い。
The blending ratio of the polyether polyol (I) and the polyether polyol (II) is such that when the total amount of the polyether polyol (I) and the polyether polyol (II) is 100% by weight, the polyether polyol (I) / Polyether polyol (II) is 60 to 90% / 40 to 10%.
The EO content in the polyol component is more preferably 45 to 68%. If the EO content is too high, collapse tends to occur, while if it is too low, shrinkage tends to occur when foaming.

なお、前記ポリオール成分としては、本発明の効果を損なわない程度であれば、一般に軟質ポリウレタンフォームに用いられている公知のポリオールを併用してもよい。例えば、架橋剤となり得る低分子量ポリオール等が挙げられる。   In addition, as said polyol component, if it is a grade which does not impair the effect of this invention, you may use together the well-known polyol generally used for the flexible polyurethane foam. For example, low molecular weight polyols that can be used as a crosslinking agent are exemplified.

前記イソシアネート成分としては、ジフェニルメタンジイソシアネート(MDI)を用いる。
また、ポリオール成分とイソシアネート成分との配合比率としては、イソシアネートインデックスで90〜120の重量割合とすることが好ましい。前記イソシアネートインデックスの数値範囲とすることで、所定の沈水性を得やすい。
Diphenylmethane diisocyanate (MDI) is used as the isocyanate component.
Moreover, it is preferable to set it as the weight ratio of 90-120 by an isocyanate index as a compounding ratio of a polyol component and an isocyanate component. By setting the isocyanate index in the numerical range, it is easy to obtain predetermined water settling.

なお、前記イソシアネート成分として、本発明の効果を損なわない程度であれば、軟質ポリウレタンフォームに使用されている公知のイソシアネートを併用してもよい。
公知のイソシアネートとしては、例えばトリレンジイソシアネート(TDI)1,5−ナフタレンジイソシアネート、パラフェニレンジイソシアネート等の芳香族ポリイソシアネートや、更に、ヘキサメチレンジイソシアネート、水添MDI、イソホロンジイソシアネート等の脂肪族ポリイソシアネートを用いることもできる。これらの他、プレポリマー型のポリイソシアネートを用いることもできる。
In addition, as long as it is a grade which does not impair the effect of this invention, you may use together the well-known isocyanate currently used for the flexible polyurethane foam as said isocyanate component.
Examples of known isocyanates include aromatic polyisocyanates such as tolylene diisocyanate (TDI) 1,5-naphthalene diisocyanate and paraphenylene diisocyanate, and aliphatic polyisocyanates such as hexamethylene diisocyanate, hydrogenated MDI and isophorone diisocyanate. It can also be used. In addition to these, a prepolymer type polyisocyanate can also be used.

発泡剤としては、ポリウレタンフォームの製造に用いられる公知のものが使用できる。例えば、低沸点不活性溶剤としてトリクロロフルオロメタン、ジクロロジフルオロメタン等のフロン系化合物等、メチレンクロライド、液化炭酸ガス反応によってガスを発生するものとして水、酸アミド、ニトロアルカン等、熱分解してガスを発生するものとして重炭酸ナトリウム、炭酸アンモニウム等がある。これら発泡剤は、単独で用いてもよく、2種以上併用してもよい。なお、好ましくは、水とメチレンクロライドを併用することが挙げられる。水とメチレンクロライドを併用することでポリウレタンフォームが良好に発泡させられるため好ましい。   As a foaming agent, the well-known thing used for manufacture of a polyurethane foam can be used. For example, water, acid amides, nitroalkanes, etc., which decomposes by heat, such as trichlorofluoromethane and chlorodifluoromethane as low-boiling inert solvents, methylene chloride, water, acid amide, nitroalkane etc. Examples of those that generate water include sodium bicarbonate and ammonium carbonate. These foaming agents may be used alone or in combination of two or more. Preferably, water and methylene chloride are used in combination. Use of water and methylene chloride is preferable because the polyurethane foam can be foamed well.

前記発泡剤として水を用いる場合は、ポリオール成分100重量%に対し1.5〜5重量%含有させることが好ましい。更に、メチレンクロライドを併用する場合は、11重量%以下で含有させることが好ましい。メチレンクロライドを前記範囲で併用とすることで高い通気量及び沈水性を得られやすい。   When water is used as the foaming agent, it is preferably contained in an amount of 1.5 to 5% by weight based on 100% by weight of the polyol component. Further, when methylene chloride is used in combination, it is preferably contained at 11% by weight or less. By using methylene chloride in the above range, a high air flow rate and water settling can be easily obtained.

整泡剤としては、軟質ポリウレタンフォームの製造に用いられる公知のものが使用できる。例えば、各種シロキサン−ポリエーテルブロック共重合体等のシリコーン系整泡剤を用いることができる。   As a foam stabilizer, a well-known thing used for manufacture of a flexible polyurethane foam can be used. For example, silicone type foam stabilizers such as various siloxane-polyether block copolymers can be used.

なお、前記整泡剤の配合量としては、前記ポリオール成分100重量%に対して0.5〜3.0重量%とすると好ましい。少ない場合、整泡効果が得られ難く、一方、多すぎる場合は通気量や圧縮残留ひずみが悪化するおそれがある。   The blending amount of the foam stabilizer is preferably 0.5 to 3.0% by weight with respect to 100% by weight of the polyol component. When the amount is too small, it is difficult to obtain a foam regulating effect, while when it is too large, there is a possibility that the air flow rate and the compression residual strain are deteriorated.

触媒としては、ポリウレタンフォームの製造に用いられる公知のものが使用できる。例えば、トリエチルアミン、トリエチレンジアミン、ビス(2−ジメチルアミノエチル)エーテル、N−メチルモルホリン、ジメチルアミノメチルフェノール、イミダゾール等の3級アミン化合物などのアミン系触媒を用いることができる。また、スタナスオクトエート等の有機錫化合物、ニッケルアセチルアセトネート等の有機ニッケル化合物などの金属系触媒を用いることもできる。これら触媒としては単独で用いてもよく、2種以上を併用してもよい。なお、触媒の配合量は、前記ポリオール成分を100重量%とした場合に、0.1〜1.5重量%とすることができる。   As a catalyst, the well-known thing used for manufacture of a polyurethane foam can be used. For example, amine-based catalysts such as tertiary amine compounds such as triethylamine, triethylenediamine, bis (2-dimethylaminoethyl) ether, N-methylmorpholine, dimethylaminomethylphenol, and imidazole can be used. In addition, a metal catalyst such as an organic tin compound such as stannous octoate or an organic nickel compound such as nickel acetylacetonate may be used. These catalysts may be used alone or in combination of two or more. In addition, the compounding quantity of a catalyst can be 0.1-1.5 weight%, when the said polyol component is 100 weight%.

また、必要に応じ、本発明の効果を損なわない範囲で他の添加剤を併用することもできる。例えば、酸化防止剤、紫外線吸収剤、着色剤、及びウレタンフォーム原料の粘度を低下させ、攪拌、混合を容易にするための希釈剤等が挙げられる。   If necessary, other additives can be used in combination as long as the effects of the present invention are not impaired. For example, an antioxidant, a UV absorber, a colorant, and a diluent for reducing the viscosity of the urethane foam raw material to facilitate stirring and mixing.

本発明の水処理担体用ポリウレタンフォームは、沈水性が600秒以下である。この為、処理槽に投入した際に、早急に排水に浸漬し、排水処理効率が向上する。   The polyurethane foam for a water treatment carrier of the present invention has a water settling of 600 seconds or less. For this reason, when thrown into the treatment tank, it is immediately immersed in the waste water, and the waste water treatment efficiency is improved.

また、水処理担体用ポリウレタンフォームは、除膜処理を施さずに通気量が3ml/cm/s以上が好ましく、また、90ml/cm/s以上であるとより好ましく、220ml/cm/s以上とすると更に好ましい。前記通気量が3ml/cm/s以上であると、沈水性を良好に600秒以下とすることができ、また90ml/cm/s以上であれば、沈水性が120秒を下回り、更に、220ml/cm/s以上であれば沈水性が60秒を下回るため、水処理担体の浸漬に要する時間の大幅な短縮が可能となる。なお、通気量が330ml/cm/sを超える場合、硬さや機械的強度が低下するおそれがあるため通気量の上限を330ml/cm/s以下とすると好ましい。 The polyurethane foam for a water treatment carrier preferably has an air permeability of 3 ml / cm 2 / s or more without being subjected to film removal treatment, more preferably 90 ml / cm 2 / s or more, and 220 ml / cm 2 / s. More preferably, it is s or more. If the aeration rate is 3 ml / cm 2 / s or more, the water settling can be satisfactorily 600 seconds or less, and if it is 90 ml / cm 2 / s or more, the water settling is less than 120 seconds, If it is 220 ml / cm 2 / s or more, the water settling is less than 60 seconds, so that the time required for the immersion of the water treatment carrier can be greatly reduced. Incidentally, when the aeration amount can exceed 330ml / cm 2 / s, the hardness and mechanical strength of the upper limit of the air permeability of at most 330ml / cm 2 / s for fear is to decrease preferred.

更に、水処理担体用ポリウレタンフォームは、セル数が25〜45個/25mmであることが好ましい。セル数が前記数値範囲であることで、機械的強度及び耐摩耗性に優れるため好ましい。   Furthermore, the polyurethane foam for a water treatment carrier preferably has 25 to 45 cells / 25 mm. It is preferable for the number of cells to be in the above numerical range because of excellent mechanical strength and wear resistance.

本発明の水処理担体用ポリウレタンフォームの製造方法としては、従来公知の方法により製造される。例えば、ポリオール成分に、発泡剤、整泡剤、触媒、その他助剤等のイソシアネート成分を除いた成分を混合し、その後イソシアネート成分と混合・発泡させる等の方法で得ることができる。   The polyurethane foam for a water treatment carrier of the present invention is produced by a conventionally known method. For example, it can be obtained by a method in which a polyol component is mixed with a component excluding an isocyanate component such as a foaming agent, a foam stabilizer, a catalyst, and other auxiliary agents, and then mixed and foamed with the isocyanate component.

以下、実施例により本発明を具体的に説明するが、本発明は以下の実施例に限定されるものではない。
[試料]
<ポリオール成分>
ポリオールA:数平均分子量3360、官能基数3、EO含有率75%のポリエーテルポリオール(三井化学株式会社製、アクトコールEP−505S)
ポリオールB:数平均分子量3000、官能基数3、EO含有率0%のポリエーテルポリオール(旭硝子株式会社製、EXCENOL3030)
<イソシアネート成分>
イソシアネートA:NCO含有率が31.5%のポリメリックMDI(東ソー株式会社製、MR−200)
イソシアネートB:NCO含有率が42.8%のTDI(三井化学株式会社製、コスモネートT−80)
<発泡剤>
発泡剤A:水(イオン交換水)
発泡剤B:メチレンクロライド
<整泡剤>
整泡剤:シリコーン系界面活性剤(東レ・ダウコーニング株式会社製、SH−192)
<触媒>
触媒A:第三級アミン触媒、トリエチレンジアミン33%のジプロピレングリコール溶液(東ソー株式会社製、TEDA−L33)
触媒B:スタナスオクトエート(日東化学株式会社製、ネオスタンU−28)
EXAMPLES Hereinafter, although an Example demonstrates this invention concretely, this invention is not limited to a following example.
[sample]
<Polyol component>
Polyol A: polyether polyol (Accor EP-505S, manufactured by Mitsui Chemicals, Inc.) having a number average molecular weight of 3360, a functional group number of 3, and an EO content of 75%
Polyol B: Polyether polyol having a number average molecular weight of 3,000, a functional group number of 3, and an EO content of 0% (Asahi Glass Co., Ltd., EXCENOL3030)
<Isocyanate component>
Isocyanate A: Polymeric MDI having an NCO content of 31.5% (manufactured by Tosoh Corporation, MR-200)
Isocyanate B: TDI with an NCO content of 42.8% (Mitsui Chemicals Cosmonate T-80)
<Foaming agent>
Foaming agent A: water (ion exchange water)
Foaming agent B: methylene chloride <foam stabilizer>
Foam stabilizer: Silicone surfactant (manufactured by Dow Corning Toray, SH-192)
<Catalyst>
Catalyst A: tertiary amine catalyst, triethylenediamine 33% dipropylene glycol solution (TODA Corporation, TEDA-L33)
Catalyst B: Stanas octoate (Nitto Chemical Co., Ltd., Neostan U-28)

表1及び表2に記載の配合比率にて、ポリオール成分に各種発泡剤、整泡剤、触媒を混合し、次いでイソシアネート成分と混合させ、発泡・硬化させてポリウレタンフォームを製造し、得られたポリウレタンフォームについて、以下の方法にて各種評価を行った。   At the blending ratios shown in Table 1 and Table 2, various foaming agents, foam stabilizers and catalysts were mixed with the polyol component, then mixed with the isocyanate component, and foamed and cured to produce a polyurethane foam. Various evaluations were performed on the polyurethane foam by the following methods.

[密度]
JIS K 7222 A法に基づいて測定した。
[セル数]
JIS K 6400(附属書)に基づいて測定した。
[フラジール式通気量]
JIS K 6400−7 B法に基づいて測定した。
[沈水性]
得られたポリウレタンフォームを10mm×10mm×10mmのキューブ状に裁断し、水面に担体を静置した段階(図1−(a))から、担体の下面から水が浸み込み、担体が徐々に水中へ沈む段階(図1−(b))を経て、担体上面まで完全に水に水没(図1−(c))するまでに要した時間を測定した。
[density]
It measured based on JISK7222A method.
[Number of cells]
Measured based on JIS K 6400 (Annex).
[Fragile airflow]
It measured based on JISK6400-7B method.
[Submergence]
The obtained polyurethane foam is cut into a cube of 10 mm × 10 mm × 10 mm, and from the stage of standing the carrier on the water surface (FIG. 1- (a)), water soaks from the lower surface of the carrier, and the carrier gradually The time required to completely submerge in water (FIG. 1- (c)) through the stage of sinking into water (FIG. 1- (b)) was completely measured up to the upper surface of the carrier.

Figure 2017057327
Figure 2017057327

Figure 2017057327
Figure 2017057327

<実施例1〜10>
本発明の水処理担体用ポリウレタンフォームは、沈水性が600S以下と非常に高い性能を有する。従って、排水に投入した際には短時間で浸漬することができる。
<Examples 1 to 10>
The polyurethane foam for a water treatment carrier of the present invention has a very high performance such that the water settling is 600 S or less. Therefore, it can be immersed in a short time when thrown into the waste water.

<比較例1、比較例2>
比較例1は、ポリオールA(ポリエーテルポリオール(I))を55.0重量%と、ポリオールB(ポリエーテルポリオール(II))を45.0重量%からなるEO含有率41%のポリオール成分を使用した。一方、比較例2は、ポリオールA(ポリエーテルポリオール(I))を95.0重量%、ポリオールB(ポリエーテルポリオール(II))を5.0重量%で配合し、EO含有率が71%のポリオール成分を使用した。
結果として、比較例1は発泡後の収縮が激しく、比較例2はコラップスが生じ、どちらも良好な発泡体が得られなかった。
<比較例3>
比較例3は、イソシアネート成分としてTDIを使用した。
結果として、沈水性が690秒と長かった。
<参考例1>
参考例1として、従来用いられている水処理担体用ポリウレタンフォームを検討した。
結果として、沈水性の検討結果で数日を要し、浸漬時間が長い実用性の低いものであることが確認された。
<参考例2>
参考例2として、浸水性を高めるために前記参考例1の水処理担体用ポリウレタンフォームに除膜処理を施した無膜ポリウレタンフォームを検討した。
結果として、除膜処理が施されているため、発泡体自体の通水性は確認されているが、結果的に沈水性に要した時間は数日を要するものであった。
<Comparative Example 1 and Comparative Example 2>
Comparative Example 1 is a polyol component having an EO content of 41%, comprising 55.0% by weight of polyol A (polyether polyol (I)) and 45.0% by weight of polyol B (polyether polyol (II)). used. On the other hand, in Comparative Example 2, polyol A (polyether polyol (I)) was blended at 95.0 wt% and polyol B (polyether polyol (II)) at 5.0 wt%, and the EO content was 71%. The polyol component was used.
As a result, Comparative Example 1 had severe shrinkage after foaming, and Comparative Example 2 had collapsed, and neither of them had a good foam.
<Comparative Example 3>
In Comparative Example 3, TDI was used as the isocyanate component.
As a result, the water settling was as long as 690 seconds.
<Reference Example 1>
As Reference Example 1, a conventionally used polyurethane foam for water treatment carrier was examined.
As a result, it was confirmed that the submergence study results required several days, and the immersion time was long and the practicality was low.
<Reference Example 2>
As Reference Example 2, a non-film polyurethane foam obtained by subjecting the polyurethane foam for a water treatment carrier of Reference Example 1 to film removal treatment in order to enhance water immersion was examined.
As a result, since the film removal treatment has been performed, the water permeability of the foam itself has been confirmed, but as a result, the time required for water subsidence required several days.

前記実施例にて確認されたように、本発明における水処理担体用ポリウレタンフォームは、従来の水処理担体用ポリウレタンフォームと比較し、非常に高い沈水性を有しており、処理槽に投入されてから浸漬するまでに要する時間を大幅に短縮することができ、水処理の効率化に繋がるものである。   As confirmed in the above examples, the polyurethane foam for water treatment carrier in the present invention has very high water subsidence compared with the conventional polyurethane foam for water treatment carrier and is put into the treatment tank. It is possible to greatly reduce the time required for immersion from the beginning, leading to the efficiency of water treatment.

1:水処理担体
2:排水
3:水処理担体における浸漬領域
1: Water treatment carrier 2: Drainage 3: Immersion area in water treatment carrier

Claims (2)

ポリオール成分、イソシアネート成分、触媒、発泡剤、整泡剤からなる水処理担体用のポリウレタンフォームであり、
前記ポリオール成分は、数平均分子量が3000〜5000、平均官能基数が2〜4、エチレンオキサイド含有率が60%以上であるポリエーテルポリオール(I)と、数平均分子量が2000〜4000、平均官能基数が2〜4、エチレンオキサイド含有率が20%以下であるポリエーテルポリオール(II)とを含み、
前記ポリエーテルポリオール(I)と前記ポリエーテルポリオール(II)の比率が、重量比で、ポリエーテルポリオール(I)/ポリエーテルポリオール(II)=60〜90%/40〜10%であり、
前記イソシアネート成分が、ジフェニルメタンジイソシアネートであり、
沈水性が600秒以下であることを特徴とする水処理担体用ポリウレタンフォーム。
Polyurethane foam for water treatment carrier consisting of polyol component, isocyanate component, catalyst, foaming agent, foam stabilizer,
The polyol component has a polyether polyol (I) having a number average molecular weight of 3000 to 5000, an average functional group number of 2 to 4, an ethylene oxide content of 60% or more, a number average molecular weight of 2000 to 4000, and an average functional group number. 2 to 4 and a polyether polyol (II) having an ethylene oxide content of 20% or less,
The ratio of the polyether polyol (I) and the polyether polyol (II) is, by weight ratio, polyether polyol (I) / polyether polyol (II) = 60 to 90% / 40 to 10%,
The isocyanate component is diphenylmethane diisocyanate;
A polyurethane foam for a water treatment carrier, wherein the water settling is 600 seconds or less.
セル数が25〜45個/25mmで、且つ通気量が3ml/cm/s以上であることを特徴とする請求項1に記載の水処理担体用ポリウレタンフォーム。
2. The polyurethane foam for water treatment carrier according to claim 1, wherein the number of cells is 25 to 45 cells / 25 mm, and the air flow rate is 3 ml / cm 2 / s or more.
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