JPS62247882A - Production of solidifying agent - Google Patents
Production of solidifying agentInfo
- Publication number
- JPS62247882A JPS62247882A JP61091494A JP9149486A JPS62247882A JP S62247882 A JPS62247882 A JP S62247882A JP 61091494 A JP61091494 A JP 61091494A JP 9149486 A JP9149486 A JP 9149486A JP S62247882 A JPS62247882 A JP S62247882A
- Authority
- JP
- Japan
- Prior art keywords
- cement
- blast furnace
- gypsum
- solidifying agent
- ozone
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は高炉水滓と排脱石膏を主材とする固化剤の製造
方法に係り、軟弱地盤の改良処理や汚泥の同化処理及び
セメントの混和材、セメントの代替材等に主に利用され
るものである。Detailed Description of the Invention (Industrial Field of Application) The present invention relates to a method for producing a solidifying agent mainly composed of blast furnace water slag and expelled gypsum, and is useful for improving soft ground, assimilating sludge, and cement. It is mainly used as an admixture and a substitute for cement.
(従来の技術)
軟弱地盤の改良や汚泥の固化処理には、従前から高炉水
滓を乾灼・粉砕し、これに高炉水砕の水硬性に活性化を
与えるための水硬性無機質材を少量混合して製造した固
化剤が広く利用されており、当該固化剤とセメントミル
クの混合物を軟弱土壌や汚泥内へ混入して攪拌すること
により、固化処理を行なうものである。当該固化剤は、
高炉水滓内の石灰ガラス質とモルタル等内の水酸化石灰
とが反応することにより、ポルトランドセメントの主要
化合物に類似する硅酸石灰やアルミン酸石灰が生成され
、水硬性が発揮されると共に緻密な水和組織を形成して
同化強度を高めるものである。(Conventional technology) In order to improve soft ground and solidify sludge, blast furnace water slag is traditionally burnt and crushed, and a small amount of hydraulic inorganic material is added to it to activate the hydraulic properties of blast furnace water slag. Solidifying agents produced by mixing are widely used, and solidifying treatment is performed by mixing a mixture of the solidifying agent and cement milk into soft soil or sludge and stirring. The solidifying agent is
When the lime glass in the blast furnace water slag reacts with the hydroxide lime in the mortar, lime silicate and lime aluminate, which are similar to the main compounds of Portland cement, are produced, which exhibits hydraulic properties and is dense. This increases the assimilation strength by forming a hydrated tissue.
しかし乍ら、前記高炉水滓より製造された固化剤は通常
セメントミルクと1:l程度の割合で混合する必要があ
り、セメントミルクの混合割合が低下すると十分な固化
作用が得られない。従って、実際の使用に於いては多量
のセメントを必要とし、地盤改良費や汚泥処理費の高、
腎を招くという難点がある。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, and ground improvement costs and sludge treatment costs are high.
The problem is that it can affect the kidneys.
また、前記固化剤は、固化の完了までに相当の養生期間
を必要とするうえ、同化物の圧縮強度が十分に上らない
という難点がある。例えば、含水比120%、比重1.
45 ?/l−のシルト質粘土1扉に、当該固化剤とセ
メントミルクが1=1の混合ミルク120KI?を混入
した場合、30日経過後の室内−軸圧縮強度が2〜3K
g/crI程度(300Kg混入の場合には15〜17
Kg/ cy& )であり、同化強度を上げるために
は、長期の養生期間と大量の固化剤及びセメントミルク
を必要とする。Further, the solidifying agent requires a considerable curing period to complete solidifying, and the compressive strength of the assimilate is not sufficiently increased. For example, water content 120%, specific gravity 1.
45? 1 door of /l- silty clay and 120 KI of mixed milk in which the solidifying agent and cement milk are 1=1? When mixed, the indoor-axial compressive strength after 30 days is 2-3K
g/crI (15 to 17 in the case of 300 kg contamination)
Kg/cy & ), and requires a long curing period and large amounts of solidification agent and cement milk to increase the assimilation strength.
一方、高炉水滓にはアルカリ性刺激剤の存在下に石膏と
水和反応をし、軟弱土壌等を固化させる作用があること
が従来から知られている。即ち、高炉水滓内のアルミナ
成分がセメントや消石灰等のアルカリ性反応促進剤の作
用によって石膏と水和反応をし、所謂上) IJンジャ
イト硬化物を生成して軟弱土壌等を固化させるものであ
る。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 IJ ngite, which solidifies soft soil, etc. .
しかし、セメントや消石灰を刺激剤として製造された固
化剤は、刺激剤量を増量(15〜20重量%)してもア
ルミナと石膏との水和反応が極めて緩慢で固化に相当長
時間を要するうえ、固形物が強アルカリ性を堅し、且つ
固化物の圧縮強度も極めて低いという難点がある。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 solid matter is strongly alkaline and the compressive strength of the solidified product is extremely low.
また、アルミナと石膏との水和反応速度を高めるために
、水酸化カリウム(KOH)や水酸化ナトリウム(Na
OH)等の強アルカリ性物質を刺激剤とする同化、剤の
製法開発も行なわれている。しかし、この場合でも水和
反応の促進には15〜20重量%の強アルカリ性刺激剤
を必要(それ以上添加しても反応速度は飽和する)とし
、その結果固化物のアルカリ度がPT(l直で10〜1
1位いになり、土壌や地盤のアルカリ汚染を生じると共
に、汚泥等の処理の場合には、同化汚泥の廃套による二
次汚染を生ずる危険がある。更に、前記製法にょる固化
剤は固化物の圧縮強度が低いうえ、アルカリ骨材反応に
よる亀裂を生ずる虞れがあり、七メ゛ントの代替品とし
て建築用等に使用することは到底不可能である。In addition, in order to increase the hydration reaction rate between alumina and gypsum, potassium hydroxide (KOH) and sodium hydroxide (Na
OH) and other strong alkaline substances are being used as stimulants to develop methods for producing assimilation agents. However, even in this case, 15 to 20% by weight of a strong alkaline stimulant is required to promote the hydration reaction (the reaction rate will be saturated even if more is added), and as a result, the alkalinity of the solidified product will be reduced to PT (l Directly 10-1
This results in alkaline contamination of the soil and ground, and in the case of sludge treatment, there is a risk of secondary contamination due to assimilated sludge waste. Furthermore, the solidifying agent produced by the above manufacturing method has a low compressive strength of the solidified product, and there is a risk of cracking due to the reaction with the alkali aggregate, so it is completely impossible to use it for construction purposes as a replacement for the 7-mention material. It is.
(発明が解決しようとする問題点)
本発明は、従前の高炉水滓を主成分とした固化剤に於け
る上述の如き問題、即ち■固化時間が相当長(目、つ固
化物の圧縮強度が相対的に低いこと、■固化物が強アル
カリ性を示すため、環境汚染を誘発すること、■強アル
カリ性のうえ固化物の機械的強度が低く、セメント代替
品として使用できないこと等の問題を解決せんとするも
のであり、同化速度が速く且つ弱アルカリ性であって環
境汚染を生ずることが無く、しかも固化物が十分な機械
的強度を保有し、セメント代替材としても使用可能な固
化剤の製造方法を提供することを目的とするものである
。(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: (1) the solidification time is considerably long (2) the compressive strength of the solidified product is Solved the problems such as: - The solidified product is strongly alkaline, causing environmental pollution; - Due to its strong alkalinity, the mechanical strength of the solidified product is low, and it cannot be used as a cement substitute. Production of a solidifying agent that has a fast assimilation 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. The purpose is to provide a method.
(問題点を解決するための手段)
本籍発明者は前述の如き問題の解決を図るため、■アル
カリ性刺激剤に他の物質成分を添加することにより、よ
り少量のアルカリ性刺激剤でもって強力な水和反応の促
進作用を得ること、及び■主成分の高炉水滓並びに排脱
石膏自体の活性化を図ることにより、刺激剤に対する感
度を上げて水和反応の促進を図ることを着想し、各種の
アルカリ性刺激剤と添加物質の組合せについて、それ等
の混合比や高炉水陸と排脱石膏の混合比をパラメータに
して数多くの固化試験等を行なうと共に、オゾンによる
高炉水滓及び排脱石膏の活性化処理について、各種の試
験を行なった。(Means for Solving the Problems) In order to solve the above-mentioned problems, the present inventor has proposed the following: ■ By adding other substances to the alkaline stimulant, a stronger water can be produced with a smaller amount of the alkaline stimulant. The idea was to increase the sensitivity to stimulants and promote the hydration reaction by activating the main components, blast furnace water slag and expelled gypsum itself. Regarding combinations of alkaline stimulants and additives, we conducted numerous solidification tests using their mixing ratios and the mixing ratios of blast furnace slag and removed gypsum as parameters, and also investigated the activation of blast furnace water slag and removed gypsum by ozone. Various tests were conducted regarding the chemical treatment.
本発明は、前記着想並びにこれに基づく各種試験を基に
して創作されたものであり、本願発明は高炉水滓及び排
煙脱硫石膏の微粉末を一定時間オゾン雰囲気中で晒し処
理し、その後20〜50重量%のオゾン処理をした排煙
脱硫石膏の微粉末と、1〜4重量%のマグネシウムと、
1〜5重量%の塩化カルシウムと、1〜5重量%のセメ
ント及び01〜05重量%の水着化カルシウムの何れが
一方又は両方と、残部に相当するオゾン処理をした高炉
水滓の微粉末とを混合することを特徴とする固化剤の製
造方法。The present invention was created based on the above idea and various tests based on the idea, and the present invention exposes fine powder of blast furnace water slag and flue gas desulfurization gypsum in an ozone atmosphere for a certain period of time, and then processes it for 20 days. ~50% by weight of fine powder of ozonated flue gas desulfurization gypsum, 1 to 4% by weight of magnesium,
1 to 5% by weight of calcium chloride, 1 to 5% by weight of cement and 01 to 05% by weight of hydrated calcium, either one or both, and the balance equivalent to fine powder of ozonated blast furnace slag. A method for producing a solidifying agent, which comprises mixing.
(作用)
本発明により製造した固化剤は、基本的には高炉水滓内
のアルミナ成分と石膏との水和反応がアルカリ性刺激剤
によって促進され、エトリンジヤイト硬化物を生成する
ことにより固化作用が臭されるものと想定される。また
、セメント等と混合して使用する場合には、高炉水滓内
の高石灰ガラス質がセメント内の水酸化石灰と反応して
セメントの主要化合物に類似の硅酸石灰及びアルミン酸
石灰を生成し、これ等による水硬作用が前記同化作用に
重畳される。(Function) The solidifying agent produced according to the present invention basically promotes the hydration reaction between the alumina component in the blast furnace water slag and gypsum with an alkaline stimulant, and by producing hardened ettringite, the solidifying action is odorless. It is assumed that In addition, when used in combination with cement, etc., the high lime glass in the blast furnace water slag reacts with the hydroxide lime in the cement to produce lime silicate and lime aluminate, which are similar to the main compounds of cement. However, the hydraulic action caused by these is superimposed on the assimilation action.
セメントや水酸化カルシウム等のアルカリ性刺激剤にマ
グネシウムと塩化カルシウムを少量添加することにより
、刺激剤が一層活性化されて水和反応の促進機能が向上
し、前記エトリンジヤイト硬化物の生成が促進されて同
化時間が短縮されると共に固化物の機械的強度も向上す
る。By adding a small amount of magnesium and calcium chloride to an alkaline stimulant such as cement or calcium hydroxide, the stimulant is further activated, its ability to promote the hydration reaction is improved, and the formation of the hardened ettringite product is promoted. Assimilation time is shortened and the mechanical strength of the solidified product is also improved.
又、主成分である排脱石膏と高炉水滓をオゾン雰囲気に
晒す処理を行なうことにより、石膏や水滓スラグ内のア
ルミナ成分等が活性化され、前記刺激剤の作用とも相俟
って工1− IJンジャイトの生成が一層促進されると
共により緻密な水和組織が形成され、これによって固化
物の機械的強度の大幅な向上が達成されるものと想定さ
れる。In addition, by exposing the main components of removed gypsum and blast furnace water slag to an ozone atmosphere, the alumina components in the gypsum and water slag are activated, and together with the action of the stimulant, the It is assumed that the production of 1-IJ ngite is further promoted and a denser hydrated structure is formed, thereby achieving a significant improvement in the mechanical strength of the solidified product.
(実施例) 以下、本発明の一実施例に基づいて本発明を詳説する。(Example) Hereinafter, the present invention will be explained in detail based on one embodiment of the present invention.
高炉水滓は、高炉から排出された溶融高炉スラグを淡水
又は海水で急冷し、更にこれを乾燥して微粉砕(粒径5
〜3011m)することにより製造される。微粉砕され
た高炉水滓は、引き続きオゾン発生器内へ導入され、こ
こで一定時間オゾン雰囲気に晒される。当該オゾンによ
る晒し処理は、オゾン発生装置内を上方から下方へ向け
てジグザグ状のシュートに沿ってスラグ微粉を落下さぜ
ることにより行なわれており、オゾン雰囲気内に於ける
微粉末の滞留時間は10〜20秒間、オゾン発生器光源
の電力は2KWX10基、スラグ微粉末の処理能力は1
0〜15 Kg /分である。尚、高炉水陸としては、
溶融高炉スラグを淡水で急冷したものを使用するのが望
ましく、またオゾン雰囲気による晒処理は、前述の如く
オゾン発器光源の電力が2KWX10基の場合には、1
0〜20秒間位いの滞留で十分であり、それ以上オゾン
処理を強化しても固化物の機械的強度の上昇に著しい変
化は見られない。Blast furnace slag is produced by rapidly cooling molten blast furnace slag discharged from a blast furnace with fresh water or seawater, then drying it and pulverizing it (particle size 5
~3011m). 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 performed 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 is 10 to 20 seconds, the power of the ozone generator light source is 2KW x 10 units, and the processing capacity of fine slag powder is 1
0-15 Kg/min. In addition, as a blast furnace amphibious land,
It is preferable to use molten blast furnace slag quenched with fresh water, and the exposure treatment in an ozone atmosphere is as follows:
Retention for about 0 to 20 seconds is sufficient, and even if the ozone treatment is further strengthened, no significant change is observed in the increase in mechanical strength of the solidified product.
第1表は、本実施例に於いて使用した高炉水滓の化学成
分を示すものである。Table 1 shows the chemical components of the blast furnace slag used in this example.
第1表 高炉水滓の化学成分(wt%)一方、排煙脱硫
石膏は、重油燃焼火力発電所からの排脱石膏を乾燥並び
に微粉砕(粒径5〜20μm)することにより製造され
ており、第2表の如き化学成分を有している。又、該排
脱石膏は高炉水滓の場合と同様に、乾燥・微粉砕のあと
オゾン雰囲気による晒処理が施されており、オゾン処理
条件は前記高炉水滓の場合と同様である。Table 1 Chemical composition of blast furnace water slag (wt%) On the other hand, flue gas desulfurization gypsum is manufactured by drying and finely pulverizing (particle size 5 to 20 μm) desulfurized gypsum from heavy oil-fired thermal power plants. , has 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.
第2表 排煙脱硫石膏の化学成分(wt%)第3表及び
゛第4表は、本実施例に於いて製造した固化剤の各成分
混合比を示すものである。Table 2 Chemical components (wt%) of flue gas desulfurization gypsum Tables 3 and 4 show the mixing ratio of each component of the solidifying agent produced in this example.
第3表 固化剤の成分(重量%)
第4表 固化剤の成分(重量%)
セメント及び水酸化カルシウムは主刺激剤を構成するも
のであり、セメントを単独で使用する場合には1〜5w
t%の添加を必要とする。セメントが1wt%以下であ
れば、高炉水滓内のアルミナと石膏との水和反応が促進
せず、またセメントが5wt%を越えると、固化物のア
ルカリ度が上るだけでなく、前記水和反応の促進効果が
飽和するからであり、1〜3wt%の混合比が最も適し
ている。Table 3 Components of solidifying agent (wt%) Table 4 Components of solidifying agent (% by weight) Cement and calcium hydroxide constitute the main irritants, and when cement is used alone, the amount of 1 to 5 w
t% addition is required. If the cement content is less than 1 wt%, the hydration reaction between alumina and gypsum in the blast furnace water slag will not be promoted, and if the cement content exceeds 5 wt%, not only will the alkalinity of the solidified product increase, but the hydration reaction will be accelerated. This is because the reaction promoting effect is saturated, and a mixing ratio of 1 to 3 wt% is most suitable.
このことは、水酸化カルシウムを主刺激剤とする場合も
同様であり、0.1 W t%以下では水和反応が緩慢
過ぎ、また0、 5 W t%を越えると、固化物のア
ルカリ度が上昇すると共に反応速度の方はあまり向上し
ないからであり、01〜0.2 W t%の混合比が最
適値である。尚、本実施例に於いてはセメント及び水酸
化カルシウムを夫々単独で使用しているが、両者を一緒
に、例えばセメンl−Iwt%と水酸化カルシウムO,
1wt%を一緒に使用してもよいことは勿論である。The same is true when calcium hydroxide is used 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 is low. This is because the reaction rate does not improve much as the amount increases, and a mixing ratio of 01 to 0.2 Wt% is the optimum value. In this example, cement and calcium hydroxide are used alone, but they can be used together, for example, cement l-Iwt% and calcium hydroxide O,
Of course, 1 wt% may also be used.
マグネシウムと塩化カルシウムは前記主刺激剤の補助的
な機能を果すものであり、主刺激剤を活性化すると共に
主刺激剤との相乗作用により前記水和反応を著しく促進
する。尚、水和反応の促進作用を奏するためには、マグ
ネシウムを1〜4wt%(最適値は1〜2wt%)、塩
化カルシウムを1〜5wt%(最適値は1〜3wt%)
夫々必要とし、何れかがその最少値を下れば、前記促進
作用は減少する。また、マグネシウム及び塩化カルシウ
ムの量が夫々4及び5wt%を越ると、水和反応の促進
効果が飽和する。従って、夫々の添加量は4及び5 W
t%以下とする。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, magnesium should be added at 1 to 4 wt% (optimal value is 1 to 2 wt%) and calcium chloride should be added at 1 to 5 wt% (optimal value is 1 to 3 wt%).
each is required, and if either falls below its minimum value, the promoting effect decreases. Furthermore, when the amounts of magnesium and calcium chloride exceed 4 and 5 wt%, respectively, the effect of promoting the hydration reaction is saturated. Therefore, the respective addition amounts are 4 and 5 W
t% or less.
オゾン処理をした排脱石膏とオゾン処理をした高炉水滓
は、夫々当該固化剤の基本成分となるものであるが、両
者の割合(高炉水滓/排脱石膏)は略1〜4位いが適当
であり、望ましくは12〜20位いが最適である。石膏
量が不足して20wt%以下になっても、或いは石膏量
が50wt%を越えて逆に高炉水滓が不足状態になって
も、固化剤の固化性能や固化強度が低下する。従って、
本実施例に於いては、排脱石膏を20〜50wt%とし
、刺激剤や活性剤を除いた残部を高炉水滓とする構成と
している。尚、高炉水滓量と石膏量の比は理論(直より
も相当大きな1直を含むものになっているが、高炉水滓
内のアルミナ成分の排脱石膏(2水石膏)に対する反応
性は石膏の溶解度等とも関連するため、理論値よりも石
膏が相当不足しても、極めて良好な固化特性が得られる
ことが確認されている。Ozone-treated degassed gypsum and ozone-treated blast furnace water slag are the basic components of the solidifying agent, but the ratio of the two (blast furnace water slag/degassed gypsum) is about 1 to 4. is suitable, and preferably 12 to 20 is optimal. Even if the amount of gypsum is insufficient and becomes less than 20 wt%, or even if the amount of gypsum exceeds 50 wt% and 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. The ratio of the amount of blast furnace water slag to the amount of gypsum is based on theory (including one shift, which is considerably larger than the direct shift), but the reactivity of the alumina component in the blast furnace water slag to the removed gypsum (dihydrate gypsum) is Since it is related to the solubility of gypsum, 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.
第1図は、前記第3表に記載の本発明により製造した固
化剤の固化試頓結果を示すものであり、曲線Aは本発明
に係る固化剤に関するものである。FIG. 1 shows the solidification test results of the solidifying agent produced according to the present invention as shown in Table 3, and curve A relates to the solidifying agent according to the present invention.
また、曲線Bは同じ化学成分物質であって、オゾン処理
をしていない高炉水滓と石膏を使用した場合のものであ
り、何れも固化剤と水との混合比(固化剤/水)を1.
7とした時の値である。Curve B is for the case where blast furnace water slag and gypsum, which have the same chemical composition and have not been subjected to ozone treatment, are used, and both have a different mixing ratio of solidifying agent and water (solidifying agent/water). 1.
This is the value when it is set to 7.
本発明により製造した固化剤の場合、圧縮強度が混合後
7日で200KF!/7.14日で330 Kg/ d
。In the case of the solidifying agent produced according to the present invention, the compressive strength is 200 KF 7 days after mixing! /7.330 Kg/d in 14 days
.
28日で54.0 K9 / 7となり、ポルトランド
セメントの場合と略同等の同化速度と圧縮強度を保有す
る。It becomes 54.0 K9/7 in 28 days, and has approximately the same assimilation rate and compressive strength as Portland cement.
また、高炉水滓並びに石膏のオゾン雰囲気による画処理
を行なわない場合に比較して、圧縮強度が略30%向上
することが判明している。Furthermore, it has been found that the compressive strength is improved by about 30% compared to the case where the blast furnace water slag and gypsum are not subjected to image treatment using an ozone atmosphere.
前記固化剤による固化物のアルカリ度は、PH85であ
って略中性に近い弱アルカリ性であり、従前の高炉水滓
を主剤とするセメント系硬化剤に比較してアルカリ度が
著しく低下する。The alkalinity of the solidified product by the solidification agent is PH85, which is a weak alkalinity close to neutrality, and the alkalinity is significantly lower than that of the conventional cement-based hardening agent whose main ingredient is blast furnace water slag.
更に、本発明により製造した固化剤を用いて含水比12
0%、比重1.45 K、、 / 7のシルト質粘土1
ゴに当該固化剤の溶融ミルクを120に9混合した場合
、大気温度(平均18℃)による自然同化に於いて、3
0日経過後の室内−軸圧縮強度が6〜7Kg/cdとな
り、従前の高炉水滓を主体とするセメント系固化剤に比
較して固化物の圧縮強度が30〜40%向上すると共に
、同化時間も大幅に短縮される。Furthermore, using the solidifying agent produced according to the present invention, the water content ratio is 12.
0%, specific gravity 1.45 K, / 7 silty clay 1
When 120:9 of molten milk of the solidification agent is mixed with Go, 3
After 0 days, the indoor-axial compressive strength is 6 to 7 Kg/cd, which improves the compressive strength of the solidified material by 30 to 40% compared to the conventional cement-based solidifying agent that mainly uses blast furnace water slag, and also reduces the assimilation time. is also significantly shortened.
(効果)
本発明に係る固化剤は、主成分である高炉水滓と排脱石
膏とをオゾン雰囲気中で一定時間晒し処理するようにし
ているため、両者が活性化されてより少ない刺激剤で水
和反応が迅速に進行すると共に、緻密な水和組織が形成
される。その結果、固化物の同化速度並びに圧縮強度が
大幅に向上する。(Effects) The solidifying agent according to the present invention is made by exposing the main components, blast furnace water slag and expelled gypsum, in an ozone atmosphere for a certain period of time, so that both are activated and less irritants are used. As the hydration reaction progresses rapidly, a dense hydrated structure is formed. As a result, the assimilation rate and compressive strength of the solidified material are significantly improved.
また、本発明に係る固化剤はマグネシウム等の添加によ
りアルカリ性刺激剤の水和反応の促進効果を著しく高め
るようにしているため、少量のアルカリ性刺激剤でもっ
て迅速な固化作用が達成される。従って、当該固化剤を
使用して土壌の改良処理やヘドロの同化処理等を行なっ
ても、所謂アルカリ汚染を生ずることは殆んどなく、し
かも固化作業に要する日程も著しく短縮され、作業能率
の向上を図り得る。Further, since the solidifying agent according to the present invention significantly enhances the effect of promoting the hydration reaction of the alkaline stimulant by adding magnesium or the like, a rapid solidifying effect can be achieved with a small amount of the alkaline stimulant. Therefore, even if soil improvement treatment or sludge assimilation treatment is performed using the solidification agent, so-called alkali pollution will hardly occur, and the time required for solidification work will be significantly shortened, improving work efficiency. Improvements can be made.
更に、本発明に係る固化剤はポルトランドセメントと略
同等の同化速度と固化物の圧縮強度を有しており、セメ
ント代替品として建材用に使用できると共に、アルカリ
性が極めて弱いので、所謂アルカリ骨材反応による構造
物の亀裂等を生ずる虞れも殆んと無い。Furthermore, the solidifying agent according to the present invention has approximately the same assimilation rate and compressive strength of the solidified product as Portland cement, and can be used for building materials as a cement substitute. There is almost no possibility that cracks or the like will occur in the structure due to the reaction.
そのうえ、本発明は高炉水滓と排脱石膏の有効利用を図
るものであり、省資源及び低コストという面でも従前の
セメント若しくはセメント系固化剤に比較して優れた効
用を有している。Furthermore, the present invention aims to effectively utilize blast furnace water slag and removed gypsum, and has superior effects in terms of resource saving and low cost compared to conventional cement or cement-based solidifying agents.
本発明は、上述の通り高い実用的効用を有するものであ
る。As mentioned above, the present invention has high practical utility.
第1図は、本発明に固化剤の硬化並びに強度特性を示す
ものである。
A 本発明に係る固化剤の特性曲線。
B 本発明と同じ化学成分であって、オゾン晒処理を行
なっていない高炉水陸と石膏を用いた固化剤の特性曲線
。
0均
第1
じFIG. 1 shows the curing and strength properties of the solidifying agent of the present invention. A Characteristic curve of the solidifying agent according to the present invention. B Characteristic curve of a solidifying agent using blast furnace land and land and gypsum, which have the same chemical components as those of the present invention but have not been subjected to ozone bleaching treatment. 0 yen 1st
Claims (1)
定時間オゾン雰囲気中で晒し処理し、その後20〜50
重量%のオゾン処理をした排煙脱硫石膏の微粉末と、1
〜4重量%のマグネシウムと、1〜5重量%の塩化カル
シウムと、1〜5重量%のセメント及び0.1〜0.5
重量%の水酸化カルシウムの何れか一方又は両方と、残
部に相当するオゾン処理をした高炉水滓の微粉末とを混
合することを特徴とする固化剤の製造方法。(1) 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
% by weight of ozone-treated flue gas desulfurization gypsum fine powder, and 1
-4% by weight magnesium, 1-5% by weight calcium chloride, 1-5% by weight cement and 0.1-0.5% by weight
1. A method for producing a solidifying agent, which comprises mixing one or both of calcium hydroxide in a weight percent and the balance of fine powder of ozone-treated blast furnace slag.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61091494A JPS62247882A (en) | 1986-04-21 | 1986-04-21 | Production of solidifying agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61091494A JPS62247882A (en) | 1986-04-21 | 1986-04-21 | Production of solidifying agent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62247882A true JPS62247882A (en) | 1987-10-28 |
| JPH0339984B2 JPH0339984B2 (en) | 1991-06-17 |
Family
ID=14027963
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61091494A Granted JPS62247882A (en) | 1986-04-21 | 1986-04-21 | Production of solidifying agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62247882A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006181432A (en) * | 2004-12-27 | 2006-07-13 | Kyushu Institute Of Technology | Waste treatment method and adsorbent for waste treatment |
| JP2008255360A (en) * | 2008-05-20 | 2008-10-23 | Chiyoda Ute Co Ltd | Soil modifying material and soil improving method |
| JP2023127725A (en) * | 2022-03-02 | 2023-09-14 | Ube三菱セメント株式会社 | Hydraulic composition, method for producing hydraulic composition, method for producing cured body, and method for suppressing variation in compressive strength |
| JP2023127726A (en) * | 2022-03-02 | 2023-09-14 | Ube三菱セメント株式会社 | Compressive strength enhancer for granulated blast furnace slag |
-
1986
- 1986-04-21 JP JP61091494A patent/JPS62247882A/en active Granted
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006181432A (en) * | 2004-12-27 | 2006-07-13 | Kyushu Institute Of Technology | Waste treatment method and adsorbent for waste treatment |
| JP2008255360A (en) * | 2008-05-20 | 2008-10-23 | Chiyoda Ute Co Ltd | Soil modifying material and soil improving method |
| JP2023127725A (en) * | 2022-03-02 | 2023-09-14 | Ube三菱セメント株式会社 | Hydraulic composition, method for producing hydraulic composition, method for producing cured body, and method for suppressing variation in compressive strength |
| JP2023127726A (en) * | 2022-03-02 | 2023-09-14 | Ube三菱セメント株式会社 | Compressive strength enhancer for granulated blast furnace slag |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0339984B2 (en) | 1991-06-17 |
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