JP2009189906A - Alkaline wastewater treatment agent - Google Patents
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Abstract
【課題】本発明は、環境汚染を軽減するアルカリ排水の処理方法を提供することを目的とする。
【解決手段】本発明は、コンクリート構造物の解体時およびコンクリート廃材を再生砕石に加工する際に生じるアルカリ排水をpH調整するためにpH緩衝性能を有する高分子化合物を使用することを特徴とする。
【選択図】なしAn object of the present invention is to provide an alkaline wastewater treatment method that reduces environmental pollution.
[MEANS FOR SOLVING PROBLEMS] The present invention is characterized in that a polymer compound having a pH buffering performance is used to adjust the pH of alkaline drainage generated during the demolition of a concrete structure and when processing concrete waste into recycled crushed stone. .
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Description
本発明は、コンクリート構造物の解体時およびコンクリート廃材を再生砕石に加工する際に生じるアルカリ排水に過剰に添加してもpHが5.5以下に外れることなく排水のpH調整を行うことができるpH緩衝機能を有する高分子化合物含有液状物。 INDUSTRIAL APPLICABILITY The present invention can adjust the pH of drainage without deviating pH to 5.5 or less even when excessively added to alkaline drainage generated when demolishing a concrete structure and processing concrete waste into recycled crushed stone. A polymer compound-containing liquid material having a pH buffering function.
コンクリートの構造物、例えばビルなどを解体する場合や廃材として生じるコンクリート片を再生砕石として加工する場合には粉塵の飛散防止のため水をかけることが一般に行われている。また、建物や橋脚などの耐震補強工事などにおいては既設コンクリートの表面を高圧ウォータージェットなどで切削する工法が一般に行われている。これらコンクリートの粉塵を含む排水は概ね高アルカリ性を示しpHが12を超える場合もある。これらの排水をそのまま排水すると環境に影響を与えるものであった。 When dismantling a concrete structure, such as a building, or when processing a piece of concrete produced as a waste material as recycled crushed stone, it is common practice to apply water to prevent dust from scattering. In addition, in seismic reinforcement work such as buildings and piers, a method of cutting the surface of existing concrete with a high-pressure water jet is generally performed. The waste water containing dust of concrete generally exhibits high alkalinity and sometimes has a pH exceeding 12. If these wastewaters were drained as they were, they would affect the environment.
これを解決するため、アルカリ排水をpH調整するための粉末状有機酸と、この粉末をはさんで担持する一対のスパンボンド不織布とを備え、アルカリ排水が通水されたとき、クエン酸が溶解してアルカリ排水のpH調整を行う排水処理方法が提案された(特許文献1参照)。
以上説明したコンクリートの構造物の解体や再生砕石への加工の場合は、発生する排水を回収して酸などのpH調整剤を添加することができ、中和することは可能である。しかしながら、排水を全て回収するには相応の貯蔵設備と中和を行う設備が必要となる。特にコンクリート構造物の解体では、工事現場は一定ではなく随時移動するため貯蔵設備や中和のための設備も移動させる必要があり、コスト的にも技術的にも大規模な工事でしか採用が難しい。そこで中小規模の工事においても採用可能な排水処理方法が求められている。 In the case of dismantling the concrete structure described above or processing into recycled crushed stone, the generated waste water can be recovered and a pH adjuster such as an acid can be added and neutralized. However, in order to collect all wastewater, appropriate storage facilities and neutralization facilities are required. Especially in the dismantling of concrete structures, the construction site is not constant, so it is necessary to move the storage facilities and neutralization facilities, which is only used for large-scale construction in terms of cost and technology. difficult. Therefore, there is a demand for a wastewater treatment method that can be used in small and medium-sized construction.
特許文献1では粉末状有機酸をはさんで担持する一対のスパンボンド不織布とを備え、これにアルカリ排水が通水することにより有機酸が溶解してアルカリ排水のpH調整を行う排水処理方法により貯蔵設備や中和を行う設備が不要になる可能性を示唆している。しかし、特許文献1の技術では、該文献の本文中にも記載してあるようにアルカリ排水のpH調整に必要な酸量を予め求める必要がある。一旦、貯蔵することができれば必要な量を求めることは可能であるが、ウォータージェットからの排水などを直接、排水する場合においては酸の必要量を求めることは困難であるとともに、やはり貯蔵設備が必要となる。また、酸の必要量を求めるにはある程度の専門知識が必要である。万一、酸を過剰に添加した場合には酸性排水を生じる可能性も秘めている。 Patent Document 1 includes a pair of spunbond nonwoven fabrics that support a powdered organic acid, and a wastewater treatment method that adjusts the pH of the alkaline drainage by dissolving the organic acid by passing the alkaline drainage through the nonwoven fabric. This suggests that storage facilities and neutralization facilities may be unnecessary. However, in the technique of Patent Document 1, it is necessary to obtain in advance the amount of acid necessary for adjusting the pH of the alkaline waste water as described in the text of the document. Once it can be stored, it is possible to determine the required amount, but when draining water from a water jet directly, it is difficult to determine the required amount of acid, and storage facilities are also required. Necessary. In addition, a certain amount of expertise is required to determine the required amount of acid. In the unlikely event that an acid is added in excess, there is also the possibility of generating acidic waste water.
工事現場の付近に河川や湖沼、海がある場合、アルカリ排水が流れ込み漁場などを汚染した例もある。こうした事情を踏まえて、近年、コンクリートの構造物の解体や再生砕石への加工などにより発生するアルカリ排水に対し規制を打ち出した自治体もあり、大きな社会問題化している。 When there are rivers, lakes, and seas in the vicinity of the construction site, there are cases where alkaline drainage flows and pollutes fishing grounds. In light of these circumstances, in recent years, there have been local governments that have stipulated regulations on alkaline drainage generated by dismantling concrete structures and processing them into recycled crushed stone, which has become a major social problem.
そこで、このような課題を解決するために本発明は、アルカリ排水をpH調整するためにpH緩衝性能を有する高分子化合物を使用することを特徴とする環境汚染を軽減するアルカリ排水の処理方法を提供することを目的とする。 Therefore, in order to solve such problems, the present invention provides an alkaline wastewater treatment method for reducing environmental pollution, characterized by using a polymer compound having pH buffering performance to adjust pH of alkaline wastewater. The purpose is to provide.
本発明はコンクリート構造物の解体時およびコンクリート廃材を再生砕石に加工する際に生じるアルカリ排水をpH調整するためにpH緩衝性能を有する高分子化合物を使用することを特徴とする。 The present invention is characterized in that a polymer compound having a pH buffering performance is used to adjust pH of alkaline drainage generated at the time of dismantling a concrete structure and processing a concrete waste material into recycled crushed stone.
本発明によれば、コンクリート構造物の解体時およびコンクリート廃材を再生砕石に加工する際に生じるアルカリ排水を貯蔵する施設や中和を行うための特別な設備を必要とせず、低コストで中和処理して排水でき、環境汚染を大きく軽減できる。 According to the present invention, it is possible to neutralize at a low cost without the need for a facility for storing alkaline wastewater generated when demolishing a concrete structure and when processing concrete waste into recycled crushed stone, or special facilities for neutralization. Can be treated and drained, greatly reducing environmental pollution.
本発明の第1の形態はコンクリート構造物の解体の際に粉塵の飛散防止のために使用される水や再生砕石への加工時に粉塵の飛散防止や冷却目的で使用される水、さらにはウォータージェットで使用される水に予め、pH緩衝能力を有する高分子化合物を添加しておくものである。このときに用いる高分子化合物はカルボキシル基を3mmol/g以上含有している必要があり、3mmol/g未満では十分なpH緩衝性を得るために必要な量が多くなり、コスト的に不利となる。該高分子化合物は水に添加した時に、その水のpHが5.5以上となるよう含有しているカルボキシル基の一部をアルカリ金属イオン、アルカリ土類金属イオン、アンモニウムイオン、4級アンモニウムイオンから選ばれた1種類以上のカチオンで中和しておく必要がある。これにより過剰に添加されることがあってもpHは5.5以下になることはない。また、ウォータージェットで使用される場合などにおいてはpH緩衝機能を有する高分子化合物は水には溶解しない微粒子状であることが好ましい。高分子化合物は溶解すると液の粘度が著しく上昇するため、ウォータージェットのように高圧で射出することが困難となり、コスト的にも技術的にも著しく不利となる。この場合の粒子径は射出ノズルの口径にもよるが、50μm以下、更には10μm以下が好ましい。液状物中の前記高分子化合物の濃度は、5質量%〜20質量%であることが好ましい。 The first aspect of the present invention is water used for preventing dust scattering during the dismantling of a concrete structure, water used for preventing dust scattering and cooling when processing into recycled crushed stone, and water. A polymer compound having a pH buffering capacity is previously added to water used in the jet. The polymer compound used at this time must contain 3 mmol / g or more of carboxyl groups, and if it is less than 3 mmol / g, the amount necessary for obtaining sufficient pH buffering properties increases, which is disadvantageous in terms of cost. . When the polymer compound is added to water, some of the carboxyl groups contained in the water so that the pH of the water is 5.5 or higher are alkali metal ions, alkaline earth metal ions, ammonium ions, quaternary ammonium ions. It is necessary to neutralize with one or more kinds of cations selected from As a result, even if it is excessively added, the pH does not become 5.5 or less. When used in a water jet, the polymer compound having a pH buffering function is preferably in the form of fine particles that do not dissolve in water. When the polymer compound is dissolved, the viscosity of the liquid is remarkably increased, so that it is difficult to inject at a high pressure like a water jet, which is extremely disadvantageous in terms of cost and technology. In this case, the particle diameter depends on the diameter of the injection nozzle, but is preferably 50 μm or less, more preferably 10 μm or less. The concentration of the polymer compound in the liquid material is preferably 5% by mass to 20% by mass.
本発明の第2の形態は再生砕石として加工されたコンクリート片等からの粉塵防止のために使用される(かけられる)水に添加することである。再生砕石は少なからず屋外で野積みされる場合があり、表面が乾燥すると粉塵を発生し周辺環境を汚染する可能性が高い。また、雨にさらされた場合は表面が洗い流されることによりアルカリ排水を生じる可能性も否定できない。屋外に野積みされた再生砕石等にpH緩衝性を有する高分子化合物を添加した水をかけることにより、雨にさらされた場合にも表面のアルカリ成分は予め中和されているため環境汚染を軽減できる。 The second mode of the present invention is to add to water used (sprayed) to prevent dust from concrete pieces processed as recycled crushed stone. Recycled crushed stones are often piled up outdoors, and when the surface is dry, there is a high possibility of generating dust and polluting the surrounding environment. Moreover, when exposed to rain, there is no denying the possibility that alkaline drainage will occur due to the surface being washed away. By applying water with a pH-buffering polymer compound to recycled crushed stones, etc. that are piled outdoors, the alkaline components on the surface are neutralized in advance even when exposed to rain. Can be reduced.
また、第2の形態に従属するものであるが、本発明では高分子化合物を用いていることから再生砕石等にかけた後、コンクリート表面に高分子化合物が吸着し保水層を形成することから乾燥速度を低下させることができる。また、本来なら乾燥時には風で飛散する微粉末が固着あるいは団粒化することで飛散を防止し環境汚染を軽減できる。なお、第1、第2の形態ともにウォータージェットなどの特殊な場合を除いて粘度上昇が問題とならなければ高分子化合物は水溶性であっても構わない。 Although dependent on the second embodiment, since the present invention uses a polymer compound, the polymer compound is adsorbed on the concrete surface after being subjected to recycled crushed stone and the like, and a water retention layer is formed. The speed can be reduced. In addition, when the powder is dried, the fine powder that is scattered by the wind is fixed or agglomerated to prevent scattering and reduce environmental pollution. In both the first and second embodiments, the polymer compound may be water-soluble unless an increase in viscosity is a problem except in special cases such as a water jet.
本発明に採用し得るpH緩衝性能を有する高分子化合物を例示すればポリアクリル酸系高分子、メタクリル酸系高分子、マレイン酸系高分子、フマル酸系高分子などを挙げることができるが、これに限定されるものではない。 Examples of polymer compounds having pH buffering performance that can be employed in the present invention include polyacrylic acid polymers, methacrylic acid polymers, maleic acid polymers, and fumaric acid polymers. It is not limited to this.
次に、実施例および比較例により本発明を説明する。
再生砕石(コンクリート廃材を小さく砕いたもの)1kgをイオン交換水100gで洗浄した洗浄液をアルカリ排水とした。該アルカリ排水のpHは11.3であり、希塩酸による中和滴定の結果アルカリ含有量は4.5×10−3ミリ当量/gであった。
Next, the present invention will be described with reference to examples and comparative examples.
A cleaning liquid obtained by washing 1 kg of recycled crushed stone (crushed concrete waste material) with 100 g of ion-exchanged water was used as alkaline drainage. The pH of the alkaline drainage was 11.3. As a result of neutralization titration with dilute hydrochloric acid, the alkali content was 4.5 × 10 −3 meq / g.
実施例1
pH緩衝性能を有する高分子化合物として東洋紡績社製液状保水材エスペックL(ポリアクリル酸ソーダ、粒子径約1μm、固形分9%)を乾燥して固形分を取り出しサンプル1とした。サンプル1のカルボキシル基量を定量したところ7.0mmol/gであった。該乾燥体を再びイオン交換水に重量基準で9%に分散した状態でのpHは7.0であった。前述のアルカリ排水100gに、上記の高分子化合物9%分散液を添加していきpHの変化を調べた。20g添加した時点でのpHは9まで低下し、50gで8まで低下した。その後は徐々に低下したが、最終的には7.2で一定となった。
Example 1
A liquid water retention material Espec L (polysodium acrylate, particle size of about 1 μm, solid content 9%) manufactured by Toyobo Co., Ltd. was dried as a polymer compound having pH buffering performance, and the solid content was taken out as Sample 1. It was 7.0 mmol / g when the amount of carboxyl groups of sample 1 was quantified. The pH when the dried product was dispersed again in ion-exchanged water at 9% by weight was 7.0. The above-mentioned 9% dispersion of the polymer compound was added to 100 g of the above alkaline waste water, and the change in pH was examined. When 20 g was added, the pH dropped to 9, and 50 g dropped to 8. After that, it gradually decreased, but finally became constant at 7.2.
実施例2
東洋紡績社製液体保水材エスペックLに硫酸を加えてpHを5に調整した後、固形分を取り出しサンプル2とした。サンプル2を重量基準で9%になるようイオン交換水に分散した状態でpHを測定したところ5.5を示した。実施例1と同様にアルカリ排水100gにサンプル2の9%分散液を添加しながらpHの変化を観察した。10g添加した時点でpHは9まで低下し35gで7に達した。引き続き添加を継続したが、pHは5.8以下には低下しなかった。
Example 2
After adjusting the pH to 5 by adding sulfuric acid to liquid water retention material Espec L manufactured by Toyobo Co., Ltd., the solid content was taken out and used as sample 2. When pH was measured in a state where sample 2 was dispersed in ion-exchanged water so as to be 9% by weight, it was 5.5. As in Example 1, the pH change was observed while adding the 9% dispersion of Sample 2 to 100 g of alkaline waste water. When 10 g was added, the pH dropped to 9 and reached 7 at 35 g. The addition was continued, but the pH did not drop below 5.8.
比較例1
東洋紡績社製液体保水材エスペックLに硫酸を加えてpHを3に調整した後、固形分を取り出しサンプル3とした。サンプル3を9%になるようイオン交換水に分散した状態でpHを測定したところ3.8を示した。実施例1と同様にアルカリ排水100gにサンプル3の9%分散液を添加しながらpHの変化を観察した。4g添加した時点でpHは9まで低下し20gで7以下となった。引き続き添加を継続した結果、pHは5.5以下となり排水基準の下限を外れた。
Comparative Example 1
After adjusting the pH to 3 by adding sulfuric acid to liquid water retention material Espec L manufactured by Toyobo Co., Ltd., the solid content was taken out and used as sample 3. When pH was measured in a state where sample 3 was dispersed in ion-exchanged water so as to be 9%, it showed 3.8. As in Example 1, the pH change was observed while adding the 9% dispersion of Sample 3 to 100 g of alkaline waste water. When 4 g was added, the pH dropped to 9 and became 20 or less at 20 g. As a result of continuing the addition, the pH was 5.5 or less, which was outside the lower limit of the drainage standard.
実施例3
アクリロニトリル90対アクリル酸メチル10の重量比で総モノマー濃度10%でイオン交換水中で硫酸アンモニウムを重合開始剤として定法に従い重合体を得た。次に該重合体を20%の水加ヒドラジン水溶液中90℃で架橋構造を導入した後、5%水酸化ナトリウム水溶液で加水分解を行い、カルボキシル基含有量が5mmol/gのカルボキシル基含有高分子化合物を得た。この高分子化合物をイオン交換水中に分散し硫酸を添加してpHを6に調整した後、固形分を取り出しサンプル4とした。サンプル4を9%になるようイオン交換水に分散した状態でpHを測定したところ6.2を示した。実施例1と同様にアルカリ排水100gにサンプル4の9%分散液を添加しながらpHの変化を観察した。19g添加した時点でpHは9まで低下し47gで7に達した。引き続き添加を継続したが、最終的には6.3で一定となった。
Example 3
A polymer was obtained according to a conventional method using ammonium sulfate as a polymerization initiator in ion-exchanged water at a weight ratio of acrylonitrile 90 to methyl acrylate 10 and a total monomer concentration of 10%. Next, the polymer was introduced with a crosslinked structure in a 20% aqueous hydrazine solution at 90 ° C. and then hydrolyzed with a 5% aqueous sodium hydroxide solution to give a carboxyl group-containing polymer having a carboxyl group content of 5 mmol / g. A compound was obtained. This polymer compound was dispersed in ion-exchanged water, and sulfuric acid was added to adjust the pH to 6. Then, the solid content was taken out and used as sample 4. When pH was measured in a state where sample 4 was dispersed in ion-exchanged water so as to be 9%, it was 6.2. As in Example 1, the pH change was observed while adding the 9% dispersion of Sample 4 to 100 g of alkaline waste water. When 19 g was added, the pH dropped to 9 and reached 7 at 47 g. The addition was continued, but eventually became constant at 6.3.
比較例2
実施例3と同様の方法で架橋構造を導入した後、2%水酸化ナトリウム水溶液で加水分解を行い、カルボキシル基含有量が1mmol/gのカルボキシル基含有高分子化合物を得た。この高分子化合物をイオン交換水中に分散し硫酸を添加してpHを5に調整した後、固形分を取り出しサンプル5とした。サンプル4を9%になるようイオン交換水に分散した状態でpHを測定したところ5.8を示した。実施例1と同様にアルカリ排水100gにサンプル5の9%分散液を添加しながらpHの変化を観察した。pH9まで低下させるのに70gを要し、排水の中和効果としては不十分なものであった。
Comparative Example 2
After introducing a crosslinked structure in the same manner as in Example 3, hydrolysis was performed with a 2% aqueous sodium hydroxide solution to obtain a carboxyl group-containing polymer compound having a carboxyl group content of 1 mmol / g. This polymer compound was dispersed in ion-exchanged water and sulfuric acid was added to adjust the pH to 5. Then, the solid content was taken out and used as Sample 5. When pH was measured in a state where sample 4 was dispersed in ion-exchanged water so as to be 9%, it showed 5.8. As in Example 1, the pH change was observed while adding the 9% dispersion of Sample 5 to 100 g of alkaline waste water. It took 70 g to lower the pH to 9, which was insufficient as a neutralizing effect of the waste water.
実施例4
実施例1と同様の手順でpH7.0を示す東洋紡績社製エスペックL由来の高分子化合物の9%分散液を調整した。この分散液を10倍に希釈した液100gで再生砕石1kgを洗浄した時の洗浄液のpHは7.8であり、前述のイオン交換水で洗浄した時のpH11.3を大きく下回った。
Example 4
A 9% dispersion of a polymer compound derived from Espec L manufactured by Toyobo Co., Ltd. having a pH of 7.0 was prepared in the same procedure as in Example 1. The pH of the washing liquid when washing 1 kg of the reclaimed crushed stone with 100 g of a solution obtained by diluting the dispersion 10 times was 7.8, which was significantly lower than the pH 11.3 when washing with the above-mentioned ion exchange water.
本発明は、コンクリート構造物の解体時およびコンクリート廃材を再生砕石に加工する際に生じるアルカリ排水の中和に適用できる。 INDUSTRIAL APPLICABILITY The present invention can be applied to neutralization of alkaline drainage generated at the time of dismantling a concrete structure and processing concrete waste into recycled crushed stone.
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JP2007061749A (en) * | 2005-08-31 | 2007-03-15 | Taiheiyo Material Kk | Method for treating cement-containing waste liquid |
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JP2003025292A (en) * | 2001-07-13 | 2003-01-29 | Daisho Kagaku Kk | Chipping system and chipping method |
JP2004358357A (en) * | 2003-06-04 | 2004-12-24 | Nippon Shokubai Co Ltd | Method for flocculating high hardness liquid containing solid in suspended state |
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