JPH0214308B2 - - Google Patents

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Publication number
JPH0214308B2
JPH0214308B2 JP10266586A JP10266586A JPH0214308B2 JP H0214308 B2 JPH0214308 B2 JP H0214308B2 JP 10266586 A JP10266586 A JP 10266586A JP 10266586 A JP10266586 A JP 10266586A JP H0214308 B2 JPH0214308 B2 JP H0214308B2
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JP
Japan
Prior art keywords
weight
blast furnace
cement
gypsum
furnace water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP10266586A
Other languages
Japanese (ja)
Other versions
JPS62260753A (en
Inventor
Kazuhiko Kishigami
Hiroshi Yasui
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP10266586A priority Critical patent/JPS62260753A/en
Publication of JPS62260753A publication Critical patent/JPS62260753A/en
Publication of JPH0214308B2 publication Critical patent/JPH0214308B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B28/00Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/02Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
    • C04B28/08Slag cements

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

産業䞊の利甚分野 本発明は高炉氎滓ず排脱石膏を䞻材ずする䞭性
固化剀ずその補造方法の改良に係り、軟匱地盀の
改良凊理や汚泥の固化凊理及びセメントの混和
材、セメントの代替材等に䞻に利甚されるもので
ある。 埓来の技術 軟匱地盀の改良や汚泥の固化凊理には、埓前か
ら高炉氎滓を也燥・粉砕し、これに高炉氎滓の氎
硬性に掻性化を䞎えるための氎硬性無機質材を少
量混合しお補造した固化剀が広く利甚されおお
り、圓該固化剀ずセメントミルクの混合物を軟匱
土壌や汚泥内ぞ混入しお撹拌するこずにより、固
化凊理を行なうものである。圓該固化剀は、高炉
氎滓内の石灰ガラス質ずモルタル等内の氎酞化石
灰ずが反応するこずにより、ポルトランドセメン
トの䞻芁化合物に類䌌する硅酞石灰やアルミン酞
石灰が生成され、氎硬性が発揮されるず共に緻密
な氎和組織を圢成しお固化匷床を高めるものであ
る。 しかし乍ら、前蚘高炉氎滓より補造された固化
剀は通垞セメントミルクず皋床の割合で混
合する必芁があり、セメントミルクの混合割合が
䜎䞋するず十分な固化䜜甚が埗られない。埓぀
お、実際の䜿甚に斌いおは倚量のセメントを必芁
ずし、地盀改良費や汚泥凊理費の高謄を招くずい
う難点がある。 たた、前蚘固化剀は、固化の完了たでに盞圓の
逊生期間を必芁ずするうえ、固化物の圧瞮匷床が
十分に䞊らないずいう難点がある。䟋えば、合氎
比120、比重1.45cm3のシルト質粘土m2に、
圓該固化剀ずセメントミルクがの混合ミル
ク120Kgを混入した堎合、30日経過埌の宀内−軞
圧瞮匷床が〜Kgcm2皋床300Kg混入の堎合
には15〜17Kgcm2であり、固化匷床を䞊げるた
めには、長期の逊生期間ず倧量の固化剀及びセメ
ントミルクを必芁ずする。 䞀方、高炉氎滓にはアルカリ性刺激剀の存圚䞋
に石膏ず氎和反応をし、軟匱土壌等を固化させる
䜜甚があるこずが埓来から知られおいる。即ち、
高炉氎滓内のアルミナ成分がセメントや消石灰等
のアルカリ性反応促進剀の䜜甚によ぀お石膏ず氎
和反応をし、所謂゚トリンゞダむト硬化物を生成
しお軟匱土壌等を固化させるものである。 しかし、セメントや消石灰を刺激剀ずしお補造
された固化剀は、刺激剀量を増量15〜20重量
しおもアルミナず石膏ずの氎和反応が極めお
緩慢で固化に盞圓長時間を芁するうえ、固化物が
匷アルカリ性を呈し、䞔぀固化物の圧瞮匷床も極
めお䜎いずいう難点がある。 たた、アルミナず石膏ずの氎和反応速床を高め
るために、氎酞化カリりムKOHや氎酞化ナ
トリりムNaOH等の匷アルカリ性物質を刺
激剀ずする固化剀の補法開発も行なわれおいる。
しかし、この堎合でも氎和反応の促進には15〜20
重量の匷アルカリ性刺激剀を必芁それ以䞊添
加しおも反応速床は飜和するずし、その結果固
化物のアルカリ床がPH倀で10〜11䜍いになり、土
壌や地盀のアルカリ汚染を生じるず共に、汚泥等
の凊理の堎合には、固化汚泥の廃棄による二次汚
染を生ずる危険がある。曎に、前蚘補法による固
化剀は固化物の圧瞮匷床が䜎いうえ、アルカリ骚
材反応による亀裂を生ずる虞れがあり、セメント
の代替品ずしお建築甚等に䜿甚するこずは到底䞍
可胜である。 発明が解決しようずする問題点 本発明は、埓前の高炉氎滓を䞻成分ずした固化
剀に斌ける䞊述の劂き問題、即ち固化時間が盞
圓長く䞔぀固化物の圧瞮匷床が盞察的に䜎いこ
ず、固化物が匷アルカリ性を瀺すため、環境汚
染を誘発するこず、匷アルカリ性のうえ固化物
の機械的匷床が䜎く、セメント代替品ずしお䜿甚
できないこず等の問題を解決せんずするものであ
り、固化速床が速く䞔぀匱アルカリ性であ぀お環
境汚染を生ずるこずが無く、しかも固化物が十分
な機械的匷床を保有し、セメント代替材ずしおも
䜿甚可胜な固化剀の補造方法を提䟛するこずを目
的ずするものである。 問題点を解決するための手段 本願発明者は前述の劂き問題の解決を図るた
め、アルカリ性刺激剀に他の物質成分を添加す
るこずにより、より少量のアルカリ性刺激剀でも
぀お匷力な氎和反応の促進䜜甚を埗るこず、固
化の進行ず共に䞭和効果を発揮する物質成分を添
加するこずにより、固化物の䞭性化を図るこず、
及び成分の高炉氎滓䞊びに排脱石膏自䜓の掻性
化を図るこずにより、刺激剀に察する感床を䞊げ
お氎和反応の促進を図るこずを着想し、各皮のア
ルカリ性刺激剀ず添加物質の組合せに぀いお、そ
れ等の混合比や高炉氎滓ず排脱石膏の混合比をパ
ラメヌタにしお数倚くの固化詊隓等を行なうず共
に、オゟンによる高炉氎滓及び排脱石膏の掻性化
凊理に぀いお、各皮の詊隓を行な぀た。 本発明は、前蚘着想䞊びにこれに基づく各皮詊
隓を基にしお創䜜されたものであり、本願第発
明に係る固化剀は、〜重量のマグネシりム
ず、〜重量の塩化カルシりムず、〜重
量のセメント及び0.1〜0.5重量の氎酞化カル
シりムの䜕れか䞀方又は䞡方ず、1.5重量以䞋
の硫酞アルミニりム及び0.3重量以䞋のくえん
酞の䜕れか䞀方又は䞡方ず、20〜50重量の排煙
脱硫石膏䞊びに残郚が高炉氎滓ずしたこずを基本
構成ずするものである。 又、本願第発明は、高炉氎滓及び排煙脱硫石
骚の埮粉末を䞀定時間オゟン雰囲気䞭で晒し凊理
し、その埌20〜50重量のオゟン凊理をした排煙
脱硫石膏の埮粉末ず、〜重量のマグネシり
ムず、〜重量の塩化カルシりムず、〜
重量のセメント及び0.1〜0.5重量の氎酞化カ
ルシりムの䜕れか䞀方又は䞡方ず、1.5重量以
䞋の硫酞アルミニりム及び0.3重量以䞋のくえ
ん酞の䜕れか䞀方又は䞡方ず、残郚に盞圓する前
蚘オゟン凊理をした高炉氎滓の埮粉末ずを混合す
るこずを、発明の基本構成ずするものである。 䜜甚 本発明に係る固化剀に斌いおは、基本的には氎
滓スラグ内のアルミナ成分ず石膏ずの氎和反応が
アルカリ性刺激剀によ぀お促進され、゚トリンゞ
ダむト硬化物を生成するこずにより固化䜜甚が奏
されるものず想定される。この際、セメントや氎
酞化カルシりム等のアルカリ性刺激剀に少量マグ
ネシりムず塩化カルシりムを添加するこずによ
り、刺激剀が掻性化されお氎和反応の促進機胜が
倧幅に向䞊する。その結果、゚トリンゞダむト硬
化物の生成が急速に行なわれ、固化時間が短瞮さ
れるず共に固化物の固化匷床も著しく向䞊する。 又、本発明の固化剀をセメント等ず混合しお䜿
甚する堎合には、氎滓スラグ内の高石灰ガラス質
がセメント内の氎酞化石灰ず反応しおポルトラン
ドセメントの䞻芁化合物に類䌌の硅酞石灰及びア
ルミン酞石灰を生成し、これによる氎硬䜜甚が前
蚘固化䜜甚に重畳されるこずになる。 曎に、添加された硫酞アルミニりムやくえん酞
は、固化の進展ず共に䞭和䜜甚を発揮し、固化物
の䞭性化が達成されるず想定される。 加えお、䞻成分である排脱石膏ず高炉氎滓をオ
ゟン雰囲気に晒す凊理を行なうこずにより、石膏
や氎滓スラグ内のアルミナ成分等が掻性化され、
前蚘刺激剀の䜜甚ずも盞俟぀お゚トリンゞダむト
の生成が䞀局促進されるず共により緻密な氎和組
織が圢成され、これによ぀お固化物の機械的匷床
の倧幅な向䞊が達成されるものず想定される。 実斜䟋 以䞋、本発明の䞀実斜䟋に基づいお本発明を詳
説する。 高炉氎滓は、高炉から排出された溶融高炉スラ
グを淡氎又は海氎で急冷し、曎にこれを也燥しお
埮粉砕粒埄〜30Όするこずにより補造さ
れる。埮粉砕された高炉氎滓は、匕き続きオゟン
発生噚内ぞ導入され、ここで䞀定時間オゟン雰囲
気に晒される。圓該オゟンによる晒し凊理は、オ
ゟン発生装眮内を䞊方から䞋方ぞ向けおゞグザグ
状のシナヌトに沿぀おスラグ埮粉を萜䞋させるこ
ずにより行なわれおおり、オゟン雰囲気内に斌け
る埮粉末の滞留時間は10〜20秒間、オゟン発生噚
光源の電力は2KW×10基、スラグ埮粉末の凊理
胜力は10〜15Kg分である。尚、高炉氎滓ずしお
は、溶融高炉スラグを淡氎で急冷したものを䜿甚
するのが望たしく、たたオゟン雰囲気による晒凊
理は、前述の劂くオゟン発噚光源の電力が2KW
×10基の堎合には、10〜20秒間䜍いの滞留で十分
であり、それ以䞊オゟン凊理を匷化しおも固化物
の機械的匷床の䞊昇に著しい倉化は芋られない。 第衚は、本実斜䟋に斌いお䜿甚した高炉氎滓
の化孊成分を瀺すものである。
(Field of Industrial Application) The present invention relates to the improvement of a neutral solidifying agent whose main ingredients are blast furnace water slag and expelled gypsum, and its production method, and is used for improving soft ground, solidifying sludge, and as an admixture for cement. It is mainly used as a substitute for cement. (Conventional technology) To improve soft ground and solidify sludge, blast furnace water slag has traditionally been dried and crushed, and a small amount of hydraulic inorganic material is mixed in to activate the hydraulic properties of the blast furnace water slag. A solidification agent manufactured by the above-mentioned method is widely used, and the solidification treatment is performed by mixing a mixture of the solidification agent and cement milk into soft soil or sludge and stirring the mixture. The solidifying agent is produced by the reaction between lime glass in blast furnace water slag and hydroxide lime in mortar, etc., to produce lime silicate and lime aluminate, which are similar to the main compounds of Portland cement, and improve hydraulic properties. At the same time, it forms a dense hydrated structure and increases the solidification strength. However, the solidifying agent produced from the blast furnace water slag usually needs to be mixed with cement milk at a ratio of about 1:1, and if the mixing ratio of cement milk is reduced, a sufficient solidifying effect cannot be obtained. Therefore, in actual use, a large amount of cement is required, leading to high costs for ground improvement and sludge treatment. Furthermore, the solidifying agent requires a considerable curing period to complete solidifying, and has the disadvantage that the compressive strength of the solidified product is not sufficiently increased. For example, for 1 m 2 of silty clay with a combined water ratio of 120% and a specific gravity of 1.45 g/cm 3 ,
When 120 kg of mixed milk with a 1:1 ratio of solidification agent and cement milk is mixed, the indoor axial compressive strength after 30 days is about 2 to 3 kg/cm 2 (15 to 17 kg/cm 2 if 300 kg is mixed) In order to increase the solidification strength, a long curing period and a large amount of solidification agent and cement milk are required. On the other hand, it has been known that blast furnace water slag undergoes a hydration reaction with gypsum in the presence of an alkaline stimulant and has the effect of solidifying soft soil and the like. That is,
The alumina component in the blast furnace water slag undergoes a hydration reaction with gypsum due to the action of alkaline reaction accelerators such as cement and slaked lime, producing so-called hardened ettringite, which solidifies soft soil and the like. However, with solidifying agents manufactured using cement or slaked lime as stimulants, even if the amount of stimulant is increased (15 to 20% by weight), the hydration reaction between alumina and gypsum is extremely slow, and solidification takes a considerable amount of time. Moreover, there are disadvantages in that the solidified product exhibits strong alkalinity and the compressive strength of the solidified product is extremely low. In addition, in order to increase the rate of hydration reaction between alumina and gypsum, a method for producing a solidifying agent is being developed that uses strong alkaline substances such as potassium hydroxide (KOH) and sodium hydroxide (NaOH) as stimulants.
However, even in this case, 15 to 20
% by weight of a strong alkaline stimulant is required (the reaction rate will be saturated even if more is added), and as a result, the alkalinity of the solidified product will be about 10 to 11 in terms of PH value, which will prevent alkaline contamination of soil and ground. In addition, in the case of processing sludge, etc., there is a risk of secondary pollution due to the disposal of solidified sludge. Furthermore, the solidifying agent manufactured by the above-mentioned method has a low compressive strength, and there is a risk of cracking due to the reaction with the alkali aggregate, making it completely impossible to use it in construction as a substitute for cement. (Problems to be Solved by the Invention) The present invention solves the above-mentioned problems with conventional solidifying agents mainly composed of blast furnace water slag, namely, the solidifying time is quite long and the compressive strength of the solidified product is relatively low. This is an attempt to solve problems such as the solidified material is strongly alkaline, causing environmental pollution, and the solidified material is strongly alkaline and has low mechanical strength, making it unsuitable for use as a cement substitute. It is an object of the present invention to provide a method for producing a solidifying agent that has a fast solidifying rate, is weakly alkaline, does not cause environmental pollution, and has sufficient mechanical strength as a solidified product, and can be used as a substitute for cement. This is the purpose. (Means for Solving the Problems) In order to solve the above-mentioned problems, the inventors of the present application have developed a method for achieving strong hydration with a smaller amount of alkaline stimulants by adding other substance components to the alkaline stimulants. To neutralize the solidified product by obtaining a reaction promoting effect and adding a substance component that exhibits a neutralizing effect as the solidification progresses;
The idea was to increase the sensitivity to irritants and promote the hydration reaction by activating the blast furnace water slag and expelled gypsum itself. In addition to conducting numerous solidification tests using the mixing ratio of these and the mixing ratio of blast furnace water slag and de-exhausted gypsum as parameters, we also conducted various tests on the activation treatment of blast furnace water slag and de-exhaust gypsum using ozone. Ta. The present invention was created based on the above idea and various tests based on the idea, and the solidifying agent according to the first invention of the present application contains 1 to 4% by weight of magnesium and 1 to 5% by weight of calcium chloride. and either or both of 1 to 5% by weight of cement and 0.1 to 0.5% by weight of calcium hydroxide, and either or both of 1.5% by weight or less of aluminum sulfate and 0.3% by weight or less of citric acid, The basic composition is 20 to 50% by weight of flue gas desulfurization gypsum and the remainder is blast furnace water slag. In addition, the second invention of the present application provides fine powder of flue gas desulfurization gypsum, which is obtained by exposing fine powder of blast furnace water slag and flue gas desulfurization stone bone in an ozone atmosphere for a certain period of time, and then treating it with 20 to 50% by weight of ozone. , 1 to 4% by weight of magnesium, 1 to 5% by weight of calcium chloride, and 1 to 5% by weight of magnesium.
% by weight of cement and 0.1 to 0.5% by weight of calcium hydroxide or both, 1.5% by weight or less of aluminum sulfate and 0.3% by weight of citric acid or both, and the balance of the above. The basic structure of the invention is to mix it with fine powder of blast furnace water slag that has been treated with ozone. (Function) In the solidifying agent according to the present invention, basically, the hydration reaction between the alumina component in the water slag and gypsum is promoted by the alkaline stimulant to produce a hardened ettringite product. It is assumed that a solidifying effect is exerted. At this time, by adding a small amount of magnesium and calcium chloride to an alkaline stimulant such as cement or calcium hydroxide, the stimulant is activated and the ability to promote the hydration reaction is greatly improved. As a result, the hardened ettringite product is rapidly produced, the solidification time is shortened, and the solidification strength of the solidified product is significantly improved. In addition, when the solidifying agent of the present invention is mixed with cement, etc., the lime-rich glass in the water slag reacts with the lime hydroxide in the cement, producing silicic acid similar to the main compound of Portland cement. Lime and aluminate lime are produced, and the resulting hydraulic action is superimposed on the solidification action. Furthermore, it is assumed that the added aluminum sulfate and citric acid exert a neutralizing effect as solidification progresses, and neutralization of the solidified product is achieved. In addition, by exposing the main components, the removed gypsum and blast furnace water slag, to an ozone atmosphere, the alumina components in the gypsum and water slag are activated.
It is assumed that, in conjunction with the action of the stimulant, the production of ettringite is further promoted and a denser hydrated structure is formed, thereby achieving a significant improvement in the mechanical strength of the solidified product. Ru. (Example) Hereinafter, the present invention will be explained in detail based on an example of the present invention. Blast furnace slag is produced by rapidly cooling molten blast furnace slag discharged from a blast furnace with fresh water or seawater, drying it, and pulverizing it (particle size: 5 to 30 ÎŒm). The pulverized blast furnace water slag is subsequently introduced into an ozone generator, where it is exposed to an ozone atmosphere for a certain period of time. The ozone exposure treatment is carried out by dropping fine slag powder along a zigzag chute from top to bottom inside the ozone generator, and the residence time of the fine powder in the ozone atmosphere is 10 minutes. ~20 seconds, the power of the ozone generator light source is 2KW x 10 units, and the processing capacity of slag fine powder is 10-15Kg/min. It is preferable to use molten blast furnace slag quenched with fresh water as the blast furnace water slag, and for exposure treatment in an ozone atmosphere, as mentioned above, the power of the ozone generator light source is 2KW.
In the case of ×10 groups, retention for about 10 to 20 seconds is sufficient, and even if the ozone treatment is further strengthened, no significant change in the increase in mechanical strength of the solidified product is observed. Table 1 shows the chemical components of the blast furnace slag used in this example.

【衚】 䞀方、排煙脱硫石膏は、重油燃焌火力発電所か
らの排脱石膏を也燥䞊びに埮粉砕粒埄〜20ÎŒ
するこずにより補造されおおり、第衚の劂
き化孊成分を有しおいる。又、該排脱石膏は高炉
氎滓の堎合ず同様に、也燥・埮粉砕のあずオゟン
雰囲気による晒凊理が斜されおおり、オゟン凊理
条件は前蚘高炉氎滓の堎合ず同様である。
[Table] On the other hand, flue gas desulfurization gypsum is produced by drying and finely pulverizing (particle size 5 to 20Ό
m) and has the chemical components as shown in Table 2. Further, as in the case of blast furnace water slag, the removed gypsum is subjected to a bleaching treatment in an ozone atmosphere after drying and pulverization, and the ozone treatment conditions are the same as in the case of the blast furnace water slag.

【衚】 第衚及び第衚は、本実斜䟋に斌いお補造し
た固化剀の各成分混合比を瀺すものである。
[Table] Tables 3 and 4 show the mixing ratio of each component of the solidifying agent produced in this example.

【衚】【table】

【衚】 セメント及び氎酞化カルシりムは䞻刺激剀を構
成するものであり、セメントを単独で䜿甚する堎
合には〜5Wtの添加を必芁ずする。セメント
が1Wt以䞋であれば、高炉氎滓内のアルミナず
石膏ずの氎和反応が促進せず、たたセメントが
5Wtを越えるず、固化物のアルカリ床が䞊るだ
けでなく、前蚘氎和反応の促進効果が飜和するか
らであり、〜3Wtの混合比が最も適しおい
る。このこずは、氎酞化カルシりムを䞻刺激剀ず
する堎合も同様であり、0.1Wt以䞋では氎和反
応が緩慢過ぎ、たた0.5Wtを越えるず、固化物
のアルカリ床が䞊昇するず共に反応速床の方はあ
たり向䞊しないからであり、0.1〜0.2Wtの混合
比が最適倀である。尚、本実斜䟋に斌いおはセメ
ント及び氎酞化カルシりムを倫々単独で䜿甚しお
いるが、䞡者を䞀緒に、䟋えばセメント1Wtず
氎酞化カルシりム0.1Wtを䞀緒に䜿甚しおもよ
いこずは勿論である。 マグネシりムず塩化カルシりムは前蚘䞻刺激剀
の補助的な機胜を果すものであり、䞻刺激剀を掻
性化するず共に䞻刺激剀ずの盞乗䜜甚により前蚘
氎和反応を著しく促進する。尚、氎和反応の促進
䜜甚を奏するためには、金属マグネシりム又は酞
化マグネシりムを〜4Wt最適倀は〜2Wt
、塩化カルシりムを〜最適倀は〜
3Wt倫々必芁ずし、䜕れかがその最少倀を䞋
れば、前蚘促進䜜甚は枛少する。たた、マグネシ
りム及び塩化カルシりムの量が倫々及び5Wt
を越えるず、氎和反応の促進効果が飜和する。埓
぀お、倫々の添加量は及び5Wt以䞋ずする。 硫酞アルミニりムは、これは1.5重量以䞊添
加するず、固化物の膚匵率が倧きくなり過ぎるず
共に固化物にクラツクが発生し易くなる。その結
果、添加量は1.5重量以䞋ずすべきであり、0.8
〜1.2重量の範囲が最も望たしい。 くえん酞は、これを0.3重量以䞊添加するず、
固化剀の固化時間が倧幅に遅れるこずになり、実
甚䞊様々な支障を生ずる。埓぀お、高枩䞋で固化
剀を䜿甚する堎合に、0.3重量以䞋の量を添加
するのが望たしい。 排脱石膏ず高炉氎滓若しくはオゟン凊理をし
た高炉氎滓は、倫々圓該固化剀の基本成分ずな
るものであるが、䞡者の割合高炉氎滓排脱石
膏は略〜䜍いが適圓であり、望たしくは
1.2〜2.0䜍いが最適である。石膏量が䞍足しお
20Wt以䞋にな぀おも、或いは石膏量が50Wt
を越えお逆に高炉氎滓が䞍足状態にな぀おも、固
化剀の固化性胜や固化匷床が䜎䞋する。埓぀お、
本実斜䟋に斌いおは、排脱石膏を20〜50Wtず
し、刺激剀や掻性剀を陀いた残郚を高炉氎滓ずす
る構成ずしおいる。尚、高炉氎滓量ず石膏量の比
は理論倀よりも盞圓倧きな倀を含むものにな぀お
いるが、高炉氎滓内のアルミナ成分の排脱石膏
氎石膏に察する反応性は石膏の溶解床等ず
も関連するため、理論倀よりも石膏が盞圓䞍足し
おも、極めお良奜な固化特性が埗られるこずが確
認されおいる。 第図は前蚘第衚に蚘茉の本願第発明に
係る固化剀の固化詊隓結果を瀺すものであり、圓
該固化剀ず氎ずの混合比固化剀氎を1.7ず
した時の倀である。圓該固化剀の堎合、圧瞮匷床
が混合埌日で150Kgcm2、14日で270Kgcm2、28
日で390Kgcm2ずなり、ポルトランドセメントの
堎合セメント氎混合比1.7のずき、日埌の
圧瞮匷床玄190Kgcm2に略近い固化速床ず固化
匷床を発揮する。 たた、前蚘固化剀による固化物のアルカリ床
は、PH7.7〜7.8であ぀お略䞭性に近い埮アルカリ
性であり、埓前の高炉氎滓を䞻剀ずするセメント
系硬化剀に比范しおアルカリ床が著しく䜎くな
る。 曎に、本発明に係る固化剀を甚いお含氎比120
、比重1.45Kgcm2のシルト質粘土m2に圓該固
化剀の溶融ミルクを120Kg混合した堎合、倧気枩
床平均18℃による自然固化に斌いお、30日経
過埌の宀内−軞圧瞮匷床が〜Kgcm2ずなり、
埓前の高炉氎滓を䞻䜓ずするセメント系固化剀の
堎合に比范しお、固化物の圧瞮匷床が20〜30向
䞊するず共に、固化時間も倧幅に短瞮される。 䞋蚘の第衚は、本願第発明に係る固化剀を
山厩れ珟堎に斌いお䜿甚した堎合のデヌタを瀺す
ものである日本工営株匏䌚瀟斜工、内山地滑り
珟堎、昭和61幎月30日。
[Table] Cement and calcium hydroxide constitute the main stimulants, and when cement is used alone, it is necessary to add 1 to 5 Wt%. If the cement content is less than 1 Wt%, the hydration reaction between the alumina and gypsum in the blast furnace water slag will not be promoted, and the cement
If it exceeds 5 Wt%, not only will the alkalinity of the solidified product increase, but the effect of promoting the hydration reaction will be saturated, and a mixing ratio of 1 to 3 Wt% is most suitable. The same is true when using calcium hydroxide as the main stimulant; below 0.1 Wt%, the hydration reaction is too slow, and above 0.5 Wt%, the alkalinity of the solidified product increases and the reaction rate increases. This is because the improvement is not so great in this case, and a mixing ratio of 0.1 to 0.2 Wt% is the optimum value. Although cement and calcium hydroxide are used alone in this example, it is also possible to use both together, for example, 1Wt% of cement and 0.1Wt% of calcium hydroxide. Of course. Magnesium and calcium chloride serve a supplementary function to the main stimulant, activate the main stimulant, and significantly promote the hydration reaction by acting synergistically with the main stimulant. In addition, in order to promote the hydration reaction, metallic magnesium or magnesium oxide must be added at 1 to 4 Wt% (the optimal value is 1 to 2 Wt%).
%), calcium chloride 1-5% (optimal value is 1-5%)
3 Wt%), and if either falls below its minimum value, the promoting effect decreases. In addition, the amount of magnesium and calcium chloride is 4 and 5 Wt%, respectively.
If it exceeds this, the effect of promoting the hydration reaction will be saturated. Therefore, the amounts added should be 4 and 5 Wt% or less, respectively. When aluminum sulfate is added in an amount of 1.5% by weight or more, the expansion rate of the solidified product becomes too large and cracks are likely to occur in the solidified product. As a result, the amount added should be less than 1.5% by weight, and 0.8
A range of ~1.2% by weight is most desirable. When citric acid is added in an amount of 0.3% by weight or more,
The solidifying time of the solidifying agent is significantly delayed, causing various problems in practical use. Therefore, when using a solidifying agent at high temperatures, it is desirable to add it in an amount of 0.3% by weight or less. Depleted gypsum and blast furnace water slag (or blast furnace water slag treated with ozone) are the basic components of the solidifying agent, and the ratio of the two (blast furnace water slag/depleted gypsum) is approximately 1 to 4. The position is appropriate, preferably
A value of 1.2 to 2.0 is optimal. Insufficient amount of plaster
Even if it is less than 20Wt% or the amount of gypsum is 50Wt%
Conversely, even if the blast furnace water slag becomes insufficient, the solidifying performance and solidifying strength of the solidifying agent will decrease. Therefore,
In this embodiment, the amount of removed gypsum is 20 to 50 Wt%, and the remainder after removing the stimulant and activator is blast furnace water slag. Although the ratio of the amount of blast furnace water slag to the amount of gypsum includes a value considerably larger than the theoretical value, the reactivity of the alumina component in the blast furnace water slag to removed gypsum (dihydrate gypsum) is due to the reactivity of gypsum. Because it is related to solubility, etc., it has been confirmed that extremely good solidification properties can be obtained even if the amount of gypsum is considerably less than the theoretical value. Figure 1A shows the solidification test results of the solidifying agent according to the first invention of the present application listed in Table 3 above, when the mixing ratio of the solidifying agent and water (solidifying agent/water) was 1.7. is the value of In the case of this solidifying agent, the compressive strength was 150 Kg/cm 2 after 7 days and 270 Kg/cm 2 after 14 days, 28
The solidification rate and solidification strength are approximately 390Kg/cm 2 per day, which is approximately close to that of Portland cement (compressive strength after 7 days of approximately 190Kg/cm 2 when the cement/water mixing ratio is 1.7). In addition, the alkalinity of the solidified product by the solidification agent is PH7.7 to 7.8, which is slightly alkaline and close to neutral, and has a higher alkalinity than the conventional cement-based hardening agent whose main ingredient is blast furnace water slag. becomes significantly lower. Furthermore, using the solidifying agent according to the present invention, the water content ratio is 120.
%, when 1 m 2 of silty clay with a specific gravity of 1.45 Kg/cm 2 is mixed with 120 kg of molten milk of the solidifying agent, the indoor-axial compressive strength after 30 days during natural solidification at atmospheric temperature (average 18°C) becomes 4~5Kg/ cm2 ,
Compared to the conventional cement-based solidifying agent based on blast furnace water slag, the compressive strength of the solidified product is improved by 20 to 30%, and the solidifying time is also significantly shortened. Table 5 below shows data when the solidifying agent according to the first invention of the present application was used at a landslide site (Constructed by Nippon Koei Co., Ltd., Uchiyama landslide site, January 30, 1985) ).

【衚】【table】

Claims (1)

【特蚱請求の範囲】  〜重量のマグネシりムず、〜重量
の塩化カルシりムず、〜重量のセメント
及び0.1〜0.5重量の氎酞化カルシりムの䜕れか
䞀方又は䞡方ず、1.5重量以䞋の硫酞アルミニ
りム及び0.3重量以䞋のくえん酞の䜕れか䞀方
又は䞡方ず、20〜50重量の排煙脱硫石膏及び残
郚が高炉氎滓より成る䞭性固化剀。  高炉氎滓の埮粉末及び排煙脱硫石膏の埮粉末
を䞀定時間オゟン雰囲気䞭で晒し凊理し、その埌
20〜50重量のオゟン凊理をした排煙脱硫石膏の
埮粉末ず、〜重量のマグネシりムず、〜
重量の塩化カルシりムず、〜重量のセ
メント及び0.1〜0.5重量の氎酞化カルシりムの
䜕れか䞀方又は䞡方ず、1.5重量以䞋の硫酞ア
ルミニりム及び0.3重量以䞋のくえん酞の䜕れ
か䞀方又は䞡方ず、残郚に盞圓する前蚘オゟン凊
理をした高炉氎滓の埮粉末ずを混合するこずを特
城ずする䞭性固化剀の補造方法。
[Scope of Claims] 1 1 to 4% by weight of magnesium, 1 to 5% by weight of calcium chloride, 1 to 5% by weight of cement, and either or both of 0.1 to 0.5% by weight of calcium hydroxide. , 1.5% by weight or less of aluminum sulfate and 0.3% by weight or less of citric acid, or both, 20 to 50% by weight of flue gas desulfurization gypsum, and the balance consisting of blast furnace water slag. 2. The fine powder of blast furnace water slag and the fine powder of flue gas desulfurization gypsum are exposed in an ozone atmosphere for a certain period of time, and then
20-50% by weight of fine powder of ozonated flue gas desulfurization gypsum, 1-4% by weight of magnesium, and 1-4% by weight of magnesium.
5% by weight of calcium chloride, 1 to 5% by weight of cement and/or 0.1 to 0.5% of calcium hydroxide, 1.5% by weight or less of aluminum sulfate, and 0.3% by weight or less of citric acid. A method for producing a neutral solidifying agent, which comprises mixing one or both of the above and the remaining part with a fine powder of the blast furnace slag subjected to the ozone treatment.
JP10266586A 1986-05-02 1986-05-02 Neutral consolidating agent and manufacture Granted JPS62260753A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10266586A JPS62260753A (en) 1986-05-02 1986-05-02 Neutral consolidating agent and manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10266586A JPS62260753A (en) 1986-05-02 1986-05-02 Neutral consolidating agent and manufacture

Publications (2)

Publication Number Publication Date
JPS62260753A JPS62260753A (en) 1987-11-13
JPH0214308B2 true JPH0214308B2 (en) 1990-04-06

Family

ID=14333526

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10266586A Granted JPS62260753A (en) 1986-05-02 1986-05-02 Neutral consolidating agent and manufacture

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Country Link
JP (1) JPS62260753A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69032372T2 (en) * 1990-07-11 1999-01-28 Tsuyuki, Naomitu, Funabashi, Chiba INORGANIC SUBSTANCE WITH PREVENTED BASIC REACTION AND METHOD FOR PREVENTING THIS REACTION
JP3374960B2 (en) * 1997-07-18 2003-02-10 䞉菱マテリアル株匏䌚瀟 Cement solidification material for organic soil
JP4069518B2 (en) * 1998-10-01 2008-04-02 宇郚興産株匏䌚瀟 Solidified material for hydrous soil and method for improving solidification of hydrous soil
JP4069519B2 (en) * 1998-10-01 2008-04-02 宇郚興産株匏䌚瀟 Solidified material for hydrous soil and method for improving solidification of hydrous soil
US6746531B1 (en) * 2002-12-23 2004-06-08 Ronald Lee Barbour Pre-blend settable composition containing calcium chloride
CN109384444B (en) * 2018-11-13 2021-07-16 湖北恒沁环保科技有限莣任公叞 Soft foundation material prepared by solidifying sludge and preparation method thereof
CN110282949B (en) * 2019-06-28 2021-09-28 河北科技倧孊 Recycling treatment method of magnesium-process desulfurization waste liquid
JP2023127726A (en) * 2022-03-02 2023-09-14 䞉菱セメント株匏䌚瀟 Compressive strength enhancer for granulated blast furnace slag

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