JP6430212B2 - Coal ash treatment agent - Google Patents

Coal ash treatment agent Download PDF

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JP6430212B2
JP6430212B2 JP2014222700A JP2014222700A JP6430212B2 JP 6430212 B2 JP6430212 B2 JP 6430212B2 JP 2014222700 A JP2014222700 A JP 2014222700A JP 2014222700 A JP2014222700 A JP 2014222700A JP 6430212 B2 JP6430212 B2 JP 6430212B2
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信哉 赤江
信哉 赤江
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Taiheiyo Materials Corp
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    • YGENERAL 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
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Description

本発明は、石炭灰からの有害成分の溶出を抑制するための石炭灰処理剤に関する。   The present invention relates to a coal ash treatment agent for suppressing elution of harmful components from coal ash.

石炭の燃焼物である石炭灰は、火力発電需要の伸びから発生量が肥大しおり、その処理が課題となっている。その処理策として産業資源への活用が進められているが、資源活用できない大量の余剰分については、主に地中へ埋立処分されている。石炭灰の主な資源活用先は、セメント原料、コンクリート用混和材、埋戻し材、路盤材等の建設・土木資材が大半である。しかしながら、石炭灰には接水により周辺に溶出する微量成分が含まれており、この中には、フッ素、硼素、砒素、セレン及び所謂6価クロムを初めとする一部の重金属類などの土壌環境基準の規制対象となっている有害成分も含まれる。石炭灰の資源活用過程や埋立処分でも、多少とも接水する可能性を長期にわたって完全に排除するのは難しく、石炭灰中の有害成分の溶出防止策が検討されてきた。例えば、石炭灰中の重金属は、キレート剤を用いて不溶化処理する方法が知られている。(例えば、特許文献1参照。)しかし、キレート剤は非常に高価であることに加え、変質劣化し易いという問題があり、広く普及するには至っていない。また、石炭灰をセメントで固化し、溶出を抑制する方法も知られている。(例えば、特許文献2参照。)この方法は処理コストが比較的安く、石炭灰中の有害成分は概ね溶出抑制できるが、一方で、セメントにはクロムが含まれるため、長期にわたって6価クロムとして溶出する可能性が危惧される。このため硫酸第一鉄等の還元剤をセメントと併用することで溶出する6価クロムを不溶性の3価クロムにする方策も知られている。(例えば、特許文献3参照。)さらに、使用するセメントを高炉セメントにすれば、6価クロム等の重金属イオンが高炉スラグに吸着されるため、6価クロム等の溶出量が減じられることが知られている。(例えば、特許文献4参照。)   Coal ash, which is a combusted product of coal, is generated in large quantities due to an increase in demand for thermal power generation, and its treatment is an issue. As a treatment measure, it is being used for industrial resources, but a large amount of surplus that cannot be used is mainly disposed of in the ground. Coal ash is mainly used for construction and civil engineering materials such as cement raw materials, concrete admixtures, backfill materials and roadbed materials. However, coal ash contains trace components that elute to the surroundings due to water contact, and this includes soil such as fluorine, boron, arsenic, selenium and some heavy metals such as so-called hexavalent chromium. It also includes harmful components that are subject to environmental standards. Even in the coal ash resource utilization process and landfill disposal, it is difficult to completely eliminate the possibility of water contact over a long period of time, and measures to prevent the leaching of harmful components in coal ash have been studied. For example, a method of insolubilizing heavy metals in coal ash using a chelating agent is known. (For example, refer to Patent Document 1.) However, in addition to being very expensive, the chelating agent has a problem of being easily deteriorated and has not been widely spread. There is also known a method of solidifying coal ash with cement to suppress elution. (For example, refer to Patent Document 2.) This method has a relatively low processing cost and can generally prevent harmful components in coal ash from being eluted, but on the other hand, since cement contains chromium, There is concern about the possibility of elution. For this reason, there is also known a method in which hexavalent chromium eluted by using a reducing agent such as ferrous sulfate in combination with cement is made insoluble trivalent chromium. (For example, refer to Patent Document 3.) Furthermore, it is known that if the cement used is blast furnace cement, heavy metal ions such as hexavalent chromium are adsorbed on the blast furnace slag, so that the elution amount of hexavalent chromium and the like is reduced. It has been. (For example, see Patent Document 4)

しかるに、還元剤の使用は、セメントと石炭灰の両者から溶出する6価クロムの還元にはかなりの量の還元剤が必要になり、コスト的に高騰する。しかも、重金属類以外の溶出成分には殆ど効果が無い。また、高炉セメントの使用は一般に強度が低くなるため資源活用には制約が生じる他、硬化に時間がかかるため、石炭灰が接水状態に晒されている時間が長くなり、その間は石炭灰からの有害成分の溶出が進み易く、吸着量を遙かに上回る溶出量となり、溶出防止の盲点となっている。   However, the use of a reducing agent requires a considerable amount of reducing agent to reduce hexavalent chromium eluted from both cement and coal ash, which increases the cost. In addition, there is almost no effect on eluted components other than heavy metals. In addition, the use of blast furnace cement generally has low strength, so there are restrictions on the utilization of resources, and it takes time to harden, so the time during which coal ash is exposed to water contact conditions becomes longer. Elution of harmful components easily proceeds, and the elution amount far exceeds the adsorption amount, which is a blind spot for preventing elution.

特開2001−121133号公報JP 2001-121133 A 特開2004−089816号公報JP 2004-089816 A 特開平09−314092号公報JP 09-314092 A 特開2007−22694号公報JP 2007-22694 A

本発明は、廉価なセメントを用いて石炭灰からの有害成分の溶出を抑制する際の前記問題点を解決するためのものである。即ち、石炭灰中に含まれ、例えば周辺土壌等へ溶出する有害成分を封じる手段として、特定のセメントを使用せずとも処理に使用するセメントからの6価クロム等の有害成分の溶出を抑制しつつ、石炭灰からの有害成分の溶出を処理から短時間で抑制でき、長期にわたり溶出抑制し続けることに適した石炭灰処理剤および該石炭灰処理剤を使用した簡便で作業性に優れた処理方法を提供する。   The present invention is to solve the above-mentioned problems when suppressing the elution of harmful components from coal ash using inexpensive cement. In other words, as a means to seal off harmful components contained in coal ash, for example, eluting to surrounding soil, etc., it suppresses the elution of harmful components such as hexavalent chromium from cement used for treatment without using specific cement. However, the elution of harmful components from coal ash can be suppressed in a short time from the treatment, and the coal ash treatment agent suitable for continuing to suppress the elution over a long period of time and the simple and excellent workability treatment using the coal ash treatment agent Provide a method.

本発明者は、前記課題解決のため検討した結果、例えば普通ポルトランドセメントなどの任意の品種のセメントと、カルシウムアルミネートなどの特定成分を含む水硬性組成物が、注水後短時間で石炭灰を固化でき、そのため処理に伴う石炭灰からの有害成分の溶出量も殆ど無く、また固化後は石炭灰からの有害成分の溶出は長期にわたり安定して抑制でき、しかも使用したセメントからの6価クロム等の重金属類の溶出も、十分抑制できたことから、本発明を完成させた。   As a result of investigations for solving the above problems, the present inventor has found that a hydraulic composition containing any kind of cement such as ordinary Portland cement and a specific component such as calcium aluminate can produce coal ash in a short time after water injection. It can be solidified, so there is almost no leaching of harmful components from coal ash during processing, and after solidification, the leaching of harmful components from coal ash can be stably suppressed over a long period of time, and hexavalent chromium from the cement used. Since the elution of heavy metals such as these was also sufficiently suppressed, the present invention was completed.

即ち、本発明は、次の(1)〜(3)で表す石炭灰処理剤および(4)で表される石炭灰の処理方法である。(1)セメント、カルシウムアルミネート、石膏類、アルカリ金属炭酸塩及びポリカルボン酸系減水剤を含有する石炭灰処理剤。(2)カルシウムアルミネートが、CaOとAl23の含有モル比(CaO/Al23)が1.2〜1.6のカルシウムアルミネートである前記(1)の石炭灰処理剤。(3)フッ素、硼素、砒素、セレン又は6価クロムの何れかを溶出する石炭灰に使用する前記(1)又は(2)の石炭灰処理剤。(4)石炭灰100質量部に対し、前記(1)〜(3)何れかの石炭灰処理剤20〜35質量部と水とを混合することを特徴とする石炭灰の処理方法。 That is, the present invention is a coal ash treating agent represented by the following (1) to (3) and a method for treating coal ash represented by (4). (1) Coal ash treatment agent containing cement, calcium aluminate, gypsum, alkali metal carbonate and polycarboxylic acid water reducing agent. (2) Calcium aluminate, coal ash treatment agent of the molar ratio of CaO and Al 2 O 3 (CaO / Al 2 O 3) is calcium aluminate 1.2-1.6 (1). (3) The coal ash treatment agent according to (1) or (2), which is used for coal ash eluting any one of fluorine, boron, arsenic, selenium and hexavalent chromium. (4) A method for treating coal ash, comprising mixing 20 to 35 parts by mass of any of the coal ash treating agents (1) to (3) and water with respect to 100 parts by mass of coal ash.

本発明によれば、石炭灰中に含まれ、例えば周辺土壌等へ溶出する有害成分を、処理開始から短時間で溶出抑制でき、長期にわたり有害成分の溶出抑制を持続でき、しかも処理剤からの有害成分の溶出も十分抑制された比較的廉価な石炭灰処理剤が提供される。また本発明によれば、有害成分の溶出を抑制するために有効な容易で作業性の良い石炭灰の処理方法が提供される。   According to the present invention, harmful components contained in coal ash, e.g., eluting into surrounding soil, etc., can be suppressed in a short time from the start of treatment, and can be maintained for a long period of time. Provided is a relatively inexpensive coal ash treatment agent in which elution of harmful components is sufficiently suppressed. Moreover, according to this invention, the processing method of the coal ash which is effective in order to suppress the elution of a harmful | toxic component and is easy and good workability | operativity is provided.

本発明の石炭灰処理剤に含有されるセメントは、水硬性のセメントなら特に限定されない。具体的には、例えば、普通、早強、超早強、中庸熱、低発熱等の各種ポルトランドセメント、またポルトランドセメントにフライアッシュ、スラグ粉、シリカフューム等を混和させた混合セメント等を使用することができる。この中では比較的安価且つ安定して入手できること及び調混合使用に関する汎用性に優れること等の利点から普通ボルトランドセメントが好ましい。   The cement contained in the coal ash treatment agent of the present invention is not particularly limited as long as it is a hydraulic cement. Specifically, for example, various ordinary portland cements such as normal, early strength, ultra-early strength, moderate heat, and low heat generation, and mixed cement obtained by mixing portland cement with fly ash, slag powder, silica fume, etc. Can do. Of these, ordinary bolt land cement is preferable because it is relatively inexpensive and can be obtained stably, and has excellent versatility with respect to mixing and use.

本発明の石炭灰処理剤に含有されるカルシウムアルミネートは、化学成分としてCaOとAl23からなる結晶質又はガラス化が進んだ構造の水和活性物質であれば何れのものでも良い。また、CaOとAl23に加えて他の化学成分が加わった化合物、固溶体若しくはガラス質物質又はこれらの混合物などであっても、本発明の効果を実質喪失させない限り何れのものでも良い。特に限定されるものではないが、好ましくはCaOとAl23の化学成分含有モル比がCaO/Al23=1.2〜1.6のカルシウムアルミネートを使用すると、急硬性に優れ、しかも処理時の作業性向上のために瞬結性が発現され難いので良い。より好ましくは、CaOとAl23の含有モル比がCaO/Al23=1.2〜1.6であって、ガラス化率が25〜75%以上のカルシウムアルミネートにすると、さらに適度な反応活性を具備し易いので良い。カルシウムアルミネートを含有することで凝結が速くなり、早期に石炭灰を締め固め、石炭灰からの溶出成分の溶出拡散をし難くすることができる。石炭灰処理剤に含有されるカルシウムアルミネートの量は特に限定されるものではないが、セメント含有量100質量部に対し、他の特性に支障なく硬化までの時間をより速くする上で、6〜15質量部が好ましく、8〜12質量部がより好ましい。 The calcium aluminate contained in the coal ash treatment agent of the present invention may be any hydrated active substance having a structure of crystallized or advanced vitrification composed of CaO and Al 2 O 3 as chemical components. Further, a compound, a solid solution, a glassy substance or a mixture thereof in which other chemical components are added in addition to CaO and Al 2 O 3 may be used as long as the effects of the present invention are not substantially lost. Although not particularly limited, and preferably chemical components molar ratio of CaO and Al 2 O 3 uses calcium aluminate CaO / Al 2 O 3 = 1.2~1.6 , excellent rapid hardening In addition, it is good because instantaneous setting is difficult to be expressed in order to improve workability during processing. More preferably, when the content molar ratio of CaO and Al 2 O 3 is CaO / Al 2 O 3 = 1.2 to 1.6 and the vitrification rate is 25 to 75% or more, a calcium aluminate is further added. It may be easy to have an appropriate reaction activity. Containing calcium aluminate speeds up the setting, makes it possible to consolidate coal ash at an early stage and make it difficult to elute and diffuse the eluted components from the coal ash. The amount of calcium aluminate contained in the coal ash treatment agent is not particularly limited. However, in order to make the time to cure faster without affecting other properties with respect to 100 parts by mass of cement, -15 mass parts is preferable, and 8-12 mass parts is more preferable.

本発明の石炭灰処理剤に含有される石膏類は、無水石膏、半水石膏、二水石膏及び硫酸カルシウムからなる群から選ばれる何れか1種または2種以上のものを使用できる。石膏類の含有は、硬化促進の観点から有要であり、石炭灰を溶出し難い強固な状態に速くせしめることに貢献する。特に、無水石膏を含有するとこの作用をより強く発現させることができる。石炭灰処理剤中の石膏類の含有量は、特に限定されないが、セメント含有量100質量部に対し、6〜15質量部が好ましく、8〜12質量部がより好ましい。   As the gypsum contained in the coal ash treatment agent of the present invention, any one or more selected from the group consisting of anhydrous gypsum, hemihydrate gypsum, dihydrate gypsum and calcium sulfate can be used. The inclusion of gypsum is important from the viewpoint of accelerating hardening, and contributes to making the coal ash difficult to elute and to make it harder quickly. In particular, when anhydrous gypsum is contained, this effect can be expressed more strongly. Although content of the gypsum in a coal ash processing agent is not specifically limited, 6-15 mass parts is preferable with respect to 100 mass parts of cement contents, and 8-12 mass parts is more preferable.

本発明の石炭灰処理剤に含有されるアルカリ金属炭酸塩は、注水時から凝結を促進させ、水和反応時間を短縮させることで処理から短時間での有害成分の溶出抑制を一層強化させることに貢献する。また、凝結を水和反応が停止するまで進め続ける作用を有すため、溶出抑制作用の向上がその間維持される。アルカリ金属炭酸塩としては、炭酸リチウム、炭酸ナトリウム、炭酸カリウムの何れか1種又は2種以上を使用できる。好ましくは炭酸リチウムを含有するのが、より良好な凝結性が得やすくなり、早期強度発現性が高まる。石炭灰処理剤中のアルカリ金属炭酸塩の含有量は、特に限定されるものではないが、セメント含有量100質量部に対し、0.1〜0.8質量部が好ましく、0.3〜0.6質量部がより好ましい。 The alkali metal carbonate contained in the coal ash treatment agent of the present invention further enhances the suppression of harmful component elution in a short time from the treatment by promoting condensation from the time of water injection and shortening the hydration reaction time. To contribute. Moreover, since it has the effect | action which continues advancing until a hydration reaction stops, the improvement of an elution suppression effect is maintained in the meantime. As the alkali metal carbonate, any one or more of lithium carbonate, sodium carbonate, and potassium carbonate can be used. When lithium carbonate is preferably contained, better coagulation properties are easily obtained, and early strength development is enhanced. The content of the alkali metal carbonate in the coal ash treatment agent is not particularly limited, but is preferably 0.1 to 0.8 parts by mass, and 0.3 to 0 with respect to 100 parts by mass of the cement content. More preferably, 6 parts by mass.

本発明の石炭灰処理剤に含有されるポリカルボン酸系減水剤は、ポリカルボン酸を有効成分とするものであって、減水剤、高性能減水剤、分散剤、流動化剤と称されているものなら何れのものでも良い。形態も液状、顆粒状のどちらでも良い。また、その一部をポリカルボン酸以外のものを有効成分とする減水剤類に置換することも可能であるが、ポリカルボン酸を有効成分とするもののみの使用が推奨される。ポリカルボン酸系減水剤の含有により、石炭灰中の有害溶出成分の溶出を抑える上で、セメント系組成物への注水量を低減させるのに有益である。また、特にポリカルボン酸を有効成分とすることで、カルシウムアルミネート併用による石炭灰混練時の抵抗を低減でき、円滑に石炭灰の溶出抑制処理を行うことができる。また、石炭灰をモルタル・コンクリート系部材や製品に有効活用する上では、このことは特に有用となる。石炭灰処理剤中のポリカルボン酸系減水剤の含有量は、特に限定されるものではないが、セメント含有量100質量部に対し、0.05〜0.4質量部が好ましく、0.1〜0.3質量部がより好ましい。   The polycarboxylic acid-based water reducing agent contained in the coal ash treatment agent of the present invention contains polycarboxylic acid as an active ingredient, and is referred to as a water reducing agent, a high-performance water reducing agent, a dispersant, and a fluidizing agent. Any thing is acceptable. The form may be either liquid or granular. Moreover, although it is possible to replace a part thereof with a water reducing agent having an active ingredient other than polycarboxylic acid, it is recommended to use only one having polycarboxylic acid as an active ingredient. By containing a polycarboxylic acid-based water reducing agent, it is beneficial to reduce the amount of water injected into the cement-based composition in order to suppress the dissolution of harmful elution components in coal ash. Moreover, the resistance at the time of coal ash kneading | mixing by calcium aluminate combined use can be reduced especially by using polycarboxylic acid as an active ingredient, and the elution suppression process of coal ash can be performed smoothly. In addition, this is particularly useful in effectively utilizing coal ash for mortar / concrete components and products. The content of the polycarboxylic acid-based water reducing agent in the coal ash treatment agent is not particularly limited, but is preferably 0.05 to 0.4 parts by mass with respect to 100 parts by mass of cement, -0.3 mass part is more preferable.

また、本発明の石炭灰処理剤には前記以外の成分も、本発明の効果を喪失させない限り含有は許容される。   Further, the coal ash treating agent of the present invention can contain components other than those described above unless the effects of the present invention are lost.

また、本発明の石炭灰処理剤の粉末度は制限されない。石炭灰からの有害溶出成分の溶出抑制効果とコストとの観点からは、含有成分毎に適値を選択すれば良い。具体的には、ブレーン比表面積で、例えば、セメントは凡そ2800〜3600cm2/g、カルシウムアルミネートは約4000〜7500cm2/g、石膏類は概ね3000〜6500cm2/gを挙げることができるが、記載例に限定されない。 Moreover, the fineness of the coal ash treatment agent of the present invention is not limited. From the viewpoint of the elution suppression effect of harmful elution components from coal ash and cost, an appropriate value may be selected for each contained component. Specifically, Blaine specific surface area, for example, although cement about 2800~3600cm 2 / g, calcium aluminate about 4000~7500cm 2 / g, gypsum may generally can be given 3000~6500cm 2 / g It is not limited to the description example.

また、本発明の石炭灰処理剤で処理対象とする石炭灰は、特に限定されるものではなく、また何れの石炭に由来する灰でも良い。好ましくは、フッ素、硼素、砒素、セレン又は6価クロムの何れか1種以上を溶出する石炭灰とする。本発明では、フッ素、硼素、砒素、セレン、6価クロムの各々を有害成分と称する。そして、このような有害成分を溶出する石炭灰を、溶出抑制するための処理に、本発明の石炭灰処理剤を使用する。   In addition, the coal ash to be treated with the coal ash treating agent of the present invention is not particularly limited, and may be ash derived from any coal. Preferably, the coal ash elutes at least one of fluorine, boron, arsenic, selenium, and hexavalent chromium. In the present invention, each of fluorine, boron, arsenic, selenium, and hexavalent chromium is referred to as a harmful component. And the coal ash processing agent of this invention is used for the process for carrying out the elution suppression of the coal ash which elutes such a harmful | toxic component.

また、本発明の石炭灰の処理方法は、石炭灰100質量部に、前記石炭灰処理剤20〜35質量部と水を添加し、混練する。混練方法は限定されないが、例えば、ホバートミキサー等の市販の混合装置を使用して行うことができる。混練時間は通常は1〜2分程度で良いが、混練量や混練装置により適宜調整するのが望ましい。混練後は大気中に放置するだけで所望の溶出抑制機能が発現できる。石炭灰100質量部に対する石炭灰処理剤の添加量が20質量部未満では硬化が十分進まなかったり、硬化までの時間を十分短縮できないことがあり、溶出抑制が不十分となることがあるので適当ではない。また、水の添加量は特に限定されず、使用するセメント及びカルシウムアルミネート等の水和反応物質が過不足無く水和できる量であって、減水剤の配合量を考慮した上で石炭灰との混練時の混合抵抗が混合に支障をきたすほど高くならない添加量を選定すれば良い。例えば予備実験などで選定することが好ましいが、具体的な目安として例えば、石炭灰100質量部に対する水の添加量は10〜30質量部を挙げることができる。この水量に限定それるものではないが、10質量部より少ないと混練作業時の混合抵抗が増加する虞がある。また30質量部より多いと硬化時間が長くなる虞がある。   Moreover, the processing method of the coal ash of this invention adds and knead | mixes the said coal ash processing agent 20-35 mass parts and water to 100 mass parts of coal ash. Although the kneading method is not limited, for example, it can be performed using a commercially available mixing apparatus such as a Hobart mixer. The kneading time is usually about 1 to 2 minutes, but it is desirable to adjust appropriately depending on the kneading amount and the kneading apparatus. After kneading, a desired elution suppression function can be exhibited simply by leaving it in the air. If the addition amount of the coal ash treatment agent with respect to 100 parts by mass of coal ash is less than 20 parts by mass, curing may not proceed sufficiently or the time until curing may not be shortened sufficiently, and elution suppression may be insufficient. is not. Further, the amount of water added is not particularly limited, and the amount of hydration reactants such as cement and calcium aluminate used can be hydrated without excess or deficiency, and considering the blending amount of the water reducing agent, What is necessary is just to select the addition amount which the mixing resistance at the time of kneading | mixing does not become so high that it will interfere with mixing. For example, although it is preferable to select by preliminary experiment etc., as a specific standard, the addition amount of water with respect to 100 mass parts of coal ash can mention 10-30 mass parts, for example. Although not limited to this amount of water, if it is less than 10 parts by mass, the mixing resistance during the kneading operation may increase. Moreover, when it exceeds 30 mass parts, there exists a possibility that hardening time may become long.

また、前記処理方法では、石炭灰の活用を目的とした処理方法の態様として、石炭灰に前記石炭灰処理剤と水を添加する際に、活用用途に応じて、例えばモルタルやコンクリートに使用できる各種骨材、膨張材、収縮低減材、短繊維等から選択される材料を、本発明の効果を喪失させない範囲で併用添加し、所望の用途に適した硬化体を任意に作製することもできる。さらに、必要に応じ、注水後の混練物を、成形に供したり、養生に供したりしても良い。   Moreover, in the said processing method, when adding the said coal ash processing agent and water to coal ash as an aspect of the processing method aiming at utilization of coal ash, according to a utilization use, it can be used for mortar and concrete, for example. A material selected from various aggregates, expansion materials, shrinkage reduction materials, short fibers, etc. can be added in combination as long as the effects of the present invention are not lost, and a cured product suitable for a desired application can be arbitrarily produced. . Furthermore, if necessary, the kneaded product after water injection may be subjected to molding or curing.

以下、本発明を実施例によって具体的に説明するが、本発明は記載した実施例に限定されるものではない。   EXAMPLES Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited to the described examples.

市販粉末試薬のCaCO3、Al23及びSiO2を原料に用い、表1の化学成分含有量のカルシウムアルミネートのクリンカが得られるように配合された原料混合物を、電気炉で、1800℃1時間加熱した。所定加熱後は直ちにクリンカを炉外に取り出し、適宜冷却用ガス(N2)をクリンカ表面に吹付けて急冷処理した。急冷したクリンカをボールミルで粉砕し、分級装置で整粒し、ブレーン比表面積約5000cm2/gのカルシウムアルミネート粉末を作製した。この粉末を粉末エックス線回折装置を用い、質量がM1のカルシウムアルミネートに含まれる各鉱物の質量を内部標準法等で定量し、定量できた含有鉱物相の総和質量(M2)を算出し、残部を純ガラス相と見なし、次式によってガラス化率を算出した。
ガラス化率(%)=(1−M2/M1)×100
カルシウムアルミネート粉末のガラス化率及び化学成分としてのCaOとAl23の含有モル比も併せて表1に表す。
Using a commercially available powder reagent CaCO 3 , Al 2 O 3 and SiO 2 as raw materials, a raw material mixture formulated so as to obtain a calcium aluminate clinker having a chemical component content shown in Table 1 was obtained in an electric furnace at 1800 ° C. Heated for 1 hour. Immediately after the predetermined heating, the clinker was taken out of the furnace, and a cooling gas (N 2 ) was sprayed onto the clinker surface as appropriate for rapid cooling. The rapidly cooled clinker was pulverized with a ball mill and sized with a classifier to prepare a calcium aluminate powder having a Blaine specific surface area of about 5000 cm 2 / g. Using a powder X-ray diffractometer for this powder, the mass of each mineral contained in the calcium aluminate with a mass of M1 is quantified by an internal standard method, etc., and the total mass (M2) of the contained mineral phase that can be quantified is calculated. Was regarded as a pure glass phase, and the vitrification rate was calculated by the following formula.
Vitrification rate (%) = (1-M2 / M1) × 100
The vitrification ratio of calcium aluminate powder and the molar ratio of CaO and Al 2 O 3 as chemical components are also shown in Table 1.

Figure 0006430212
Figure 0006430212

このようにして得られたカルシウムアルミネート粉末と、何れも市販品の普通ポルトランドセメント、高炉セメント、II型無水石膏(ブレーン比表面積6000cm2/g)、二水石膏(ブレーン比表面積5500cm2/g)、炭酸リチウム(粉末試薬)、炭酸ナトリウム(粉末試薬)、ポリカルボン酸系顆粒状減水剤、ナフタレンスルホン酸系液状減水剤(固形分濃度30%)から選定された成分を表2に表す配合量となるようヘンシェルミキサを用いて約2分間混合し、処理剤を作製した。 Thus calcium aluminate powder obtained in both of the commercially available ordinary portland cement, blast furnace cement, II type anhydrous gypsum (Blaine specific surface area of 6000 cm 2 / g), gypsum (Blaine specific surface area of 5500cm 2 / g ), Lithium carbonate (powder reagent), sodium carbonate (powder reagent), polycarboxylic acid granular water reducing agent, naphthalenesulfonic acid liquid water reducing agent (solid content concentration 30%) A treatment agent was prepared by mixing for about 2 minutes using a Henschel mixer.

Figure 0006430212
Figure 0006430212

今回、処理対象とした石炭灰は、硼素、フッ素、砒素、セレン及びクロムを含むものであって、環境庁告示第46号に準じた方法で測定した結果、硼素の溶出量2.9mg/リットル、フッ素の溶出量1.4mg/リットル、砒素の溶出量0.11mg/リットル、セレンの溶出量0.08mg/リットル、6価クロムの溶出量0.15mg/リットルのものである。   The coal ash to be treated this time contains boron, fluorine, arsenic, selenium, and chromium, and as a result of measurement by a method according to Environment Agency Notification No. 46, the amount of boron elution is 2.9 mg / liter. Fluorine elution amount 1.4 mg / liter, arsenic elution amount 0.11 mg / liter, selenium elution amount 0.08 mg / liter, hexavalent chromium elution amount 0.15 mg / liter.

この石炭灰に、前記作製した処理剤と水を、表3で表す配合となるように、先ず石炭灰をホバートミキサに移し、次いで処理剤と水を添加し、ホバートミキサを約2分間低速混合した。混合停止後直ぐに、ミキサ内壁の付着物をヘラで素早く掻き落とし、再度約2分間混合することで、石炭灰の処理を行った。この処理は何れも約20℃±1℃の環境下で行った。   First, the coal ash is transferred to a Hobart mixer, and then the treatment agent and water are added to the coal ash so as to have the composition shown in Table 3, and then the Hobart mixer is mixed at a low speed for about 2 minutes. did. Immediately after the mixing was stopped, the adhering matter on the inner wall of the mixer was quickly scraped off with a spatula and mixed again for about 2 minutes to treat the coal ash. All of these treatments were performed in an environment of about 20 ° C. ± 1 ° C.

Figure 0006430212
Figure 0006430212

この処理による処理体の性状とその処理の作業性を評価するため、処理体の混合性を調べた。即ち、混合中は混合抵抗が少なく明らかに流動状態を呈し、且つ目視により概ね斑無く均一な混練物が得らるものを混合性「良好」と判断し、それ以外の状態であったもの(凝結が速過ぎて混合できなかったものを含む。)は全て混合性「不良」と判断した。   In order to evaluate the properties of the treatment body and the workability of the treatment, the mixing properties of the treatment bodies were examined. That is, during mixing, the mixing resistance is small and clearly exhibits a fluid state, and a visually uniform and uniform kneaded product is determined to be “good” for mixing, and other than that ( Including those that could not be mixed because the setting was too fast.

また、前記の混合終了から2時間経過後の処理体の混練物に対し、断面積0.125cm2のプロクター針を用いたプロクター貫入試験を20℃±1℃の環境下で行い、処理体の凝結性を評価した。プロクター貫入抵抗値が28N/mm2以上で凝結時間の終結に達しているものを凝結性「良好」と判断し、28N/mm2に達していないもの又は測定が不能であったものを凝結性「不良」と判断した。 Further, a proctor penetration test using a proctor needle having a cross-sectional area of 0.125 cm 2 was performed in an environment of 20 ° C. ± 1 ° C. with respect to the kneaded product after 2 hours from the end of mixing. The setting property was evaluated. Proctor penetration resistance value is 28N / mm 2 or more and the end of the setting time is judged to be “good”, and if it does not reach 28N / mm 2 or measurement is impossible Judged as “bad”.

また、前記の混合終了直後の処理体の混練物を、内径5mmで高さ10mmの円筒型枠に充填し、20℃±1℃の環境下で6時間静置後に脱型して円柱状の硬化物(供試体)を得た。約20℃±1℃の大気中に放置した材齢1日、28日及び91日の供試体に対し、JIS A 1108に準拠した方法で一軸圧縮強度を測定し、処理体の硬化性状に関する評価とした。石炭灰を処理してなる処理体に関する以上の評価結果は表3に纏めて表す。尚、混合時の流動性が著しく低く型枠充填できなかったものや型枠充填できても硬化しなかったものは、強度測定不能につき表中では「−」と表示した。   Further, the kneaded product of the processed body immediately after the mixing is filled into a cylindrical frame having an inner diameter of 5 mm and a height of 10 mm, and left to stand for 6 hours in an environment of 20 ° C. ± 1 ° C., and then demolded to form a cylindrical shape. A cured product (specimen) was obtained. Uniaxial compressive strength was measured by a method in accordance with JIS A 1108 for specimens of 1 day, 28 days, and 91 days of age, which were left in the atmosphere of about 20 ° C. ± 1 ° C., and evaluation on the curing properties of the treated body. It was. The above evaluation results relating to the treated body obtained by treating coal ash are summarized in Table 3. In addition, in the table, “−” was indicated for those in which the fluidity at the time of mixing was extremely low and the mold could not be filled or the mold could be filled but not cured.

また、前記のように作製した供試体を、脱型後20℃±1℃で7日間風乾養生し、次いでジョークラッシャーで粉砕し、粉砕物を2mm目篩を通過させて粉末を採取した。この粉末50.0gを内容積1000mlのポリ容器に入れ、純水1リットルに0.5規定の塩酸を添加してpH6.1に調整した溶媒500gを加え、市販の振とう装置で、200回/分の振とうを6時間行った。振とう後は20℃(±1℃)の恒温器中で30分間静置し、ポリ容器内に生じた上澄みを、孔径0.45μmメンプレンフィルターで濾過し、検液を得た。この検液に対し、硼素、フッ素、砒素、セレン及び6価クロムの溶出量を以下の方法でそれぞれ測定した。材齢1日の処理体(供試体)からの前記溶出成分の溶出量検出値を表4に表す。また、同様の方法で行った材齢91日の処理体(供試体)からの前記溶出成分の溶出量の検出値を表5に表す。   Further, the specimen prepared as described above was air-dried at 20 ° C. ± 1 ° C. for 7 days after demolding, then pulverized with a jaw crusher, and the pulverized product was passed through a 2 mm sieve to collect powder. 50.0 g of this powder was put into a plastic container having an internal volume of 1000 ml, 500 g of a solvent adjusted to pH 6.1 by adding 0.5 N hydrochloric acid to 1 liter of pure water, and 200 times with a commercially available shaker. Shaking / min for 6 hours. After shaking, it was allowed to stand for 30 minutes in a thermostat at 20 ° C. (± 1 ° C.), and the supernatant produced in the plastic container was filtered through a membrane filter having a pore size of 0.45 μm to obtain a test solution. With respect to this test solution, the elution amounts of boron, fluorine, arsenic, selenium and hexavalent chromium were measured by the following methods. Table 4 shows the elution amount detection values of the elution components from the treated body (specimen) at the age of 1 day. Further, Table 5 shows the detected values of the elution amounts of the elution components from the 91-day-old treated body (test body), which was performed in the same manner.

何れも環境庁告示第46号に規定された方法であって、
・硼素;JIS K 0102−2008の47.3「ICP発光分光分析法」
・フッ素;昭和46年12月環境庁告示第59号付表6イオンクロマトグラフ法
・砒素;JIS K 0102−2008の61.4「ICP質量分析法」
・セレン;JIS K 0102−2008の61.4「ICP質量分析法」
・6価クロム;JIS K 0102−2008の65.2.1「ジフェニルカルバジド吸光光度法」
Both are the methods stipulated in Environment Agency Notification No. 46,
Boron: JIS K 0102-2008, 47.3 “ICP emission spectroscopy”
・ Fluorine: December, 1971 Environment Agency Notification No. 59, Appendix Table 6 Ion Chromatograph Method ・ Arsenic: 61.4 “ICP Mass Spectrometry” of JIS K 0102-2008
・ Selenium; JIS K 0102-2008 61.4 “ICP Mass Spectrometry”
Hexavalent chromium; JIS K 0102-2008 65.2.1 “Diphenylcarbazide absorptiometry”

Figure 0006430212
Figure 0006430212

Figure 0006430212
Figure 0006430212

以上の結果から、本発明の石炭灰処理剤は、処理後短時間で石炭灰中の有害成分の溶出抑制作用が発現でき、この溶出抑制作用は長期間持続していることがわかる。しかも、有害成分を溶出抑制するための石炭灰の処理は、簡単で作業性にも優れた処理方法で処理できることがわかる。これに対し、従来技術などの本発明から外れる技術では、処理後短時間では有害成分の溶出を殆ど抑制できないか、ある程度抑制できてもそのための処理操作、例えば高い混合抵抗などの負荷がかかり、作業性が劣ることがわかる。   From the above results, it can be seen that the coal ash treatment agent of the present invention can exhibit the elution suppressing action of harmful components in the coal ash in a short time after the treatment, and this elution suppressing action lasts for a long time. Moreover, it can be seen that the treatment of coal ash for suppressing the release of harmful components can be carried out by a treatment method that is simple and excellent in workability. On the other hand, in the technology deviating from the present invention such as the prior art, elution of harmful components can hardly be suppressed in a short time after the processing, or even if it can be suppressed to some extent, a processing operation for that, for example, a load such as high mixing resistance is applied, It turns out that workability is inferior.

Claims (4)

石炭灰からの有害成分の溶出を抑制するための石炭灰処理剤であって、
セメント、CaOとAl 2 3 の含有モル比(CaO/Al )が1.2〜1.6のカルシウムアルミネート、石膏類、アルカリ金属炭酸塩及びポリカルボン酸系減水剤を含有する石炭灰処理剤。
A coal ash treatment agent for suppressing elution of harmful components from coal ash,
Cement, containing calcium aluminate, gypsum, alkali metal carbonate and polycarboxylic acid-based water reducing agent having a molar ratio of CaO to Al 2 O 3 (CaO / Al 2 O 3 ) of 1.2 to 1.6 Coal ash treatment agent.
前記石炭灰処理剤に含有される前記カルシウムアルミネートの量は、前記セメント含有量100質量部に対し6〜15質量部であり、The amount of the calcium aluminate contained in the coal ash treatment agent is 6 to 15 parts by mass with respect to 100 parts by mass of the cement.
前記石炭灰処理剤に含有される前記石膏類の量は、前記セメント含有量100質量部に対し6〜15質量部であり、The amount of the gypsum contained in the coal ash treatment agent is 6 to 15 parts by mass with respect to 100 parts by mass of the cement.
前記石炭灰処理剤に含有される前記アルカリ金属炭酸塩の量は、前記セメント含有量100質量部に対し0.1〜0.8質量部であり、The amount of the alkali metal carbonate contained in the coal ash treatment agent is 0.1 to 0.8 parts by mass with respect to 100 parts by mass of the cement,
前記石炭灰処理剤に含有されるポリカルボン酸系減水剤の量は、前記セメント含有量100質量部に対し0.05〜0.4質量部であるThe amount of the polycarboxylic acid-based water reducing agent contained in the coal ash treatment agent is 0.05 to 0.4 parts by mass with respect to 100 parts by mass of the cement.
請求項1に記載の石炭灰処理剤。The coal ash treatment agent according to claim 1.
フッ素、硼素、砒素、セレン又は6価クロムの何れかを溶出する石炭灰に使用する請求項1又は2記載の石炭灰処理剤。 The coal ash treatment agent according to claim 1 or 2, which is used for coal ash eluting any one of fluorine, boron, arsenic, selenium and hexavalent chromium. 石炭灰100質量部に対し、請求項1〜3何れか記載の石炭灰処理剤20〜35質量部と水とを混合することを特徴とする石炭灰からの有害成分の溶出を抑制する石炭灰処理方法。 Coal ash which suppresses the elution of harmful components from coal ash, wherein 20 to 35 parts by mass of coal ash treating agent according to any one of claims 1 to 3 and water are mixed with respect to 100 parts by mass of coal ash. Processing method.
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