JPS602262B2 - Method for producing granulated slag - Google Patents

Method for producing granulated slag

Info

Publication number
JPS602262B2
JPS602262B2 JP52067981A JP6798177A JPS602262B2 JP S602262 B2 JPS602262 B2 JP S602262B2 JP 52067981 A JP52067981 A JP 52067981A JP 6798177 A JP6798177 A JP 6798177A JP S602262 B2 JPS602262 B2 JP S602262B2
Authority
JP
Japan
Prior art keywords
slag
blast furnace
additive
granulated
granulated slag
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
Application number
JP52067981A
Other languages
Japanese (ja)
Other versions
JPS542995A (en
Inventor
征幸 高田
辰雄 広瀬
泉 門奈
由一 長尾
晃 岡本
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.)
Shin Etsu Chemical Co Ltd
Nippon Steel Corp
Original Assignee
Shin Etsu Chemical Co Ltd
Nippon Steel Corp
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 Shin Etsu Chemical Co Ltd, Nippon Steel Corp filed Critical Shin Etsu Chemical Co Ltd
Priority to JP52067981A priority Critical patent/JPS602262B2/en
Publication of JPS542995A publication Critical patent/JPS542995A/en
Publication of JPS602262B2 publication Critical patent/JPS602262B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/04Recovery of by-products, e.g. slag
    • C21B3/06Treatment of liquid slag
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Manufacture Of Iron (AREA)

Description

【発明の詳細な説明】 本発明は、コンクリートモルタル用細骨材などに適する
水砕スラグの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing granulated slag suitable as fine aggregate for concrete mortar.

製鉄事業の発達とともに、高炉から富山生する溶融高炉
スラグの量も増大しているが、その一部分はセメント用
などに有効に利用されているものの、大部分は処理に窮
しているのが実状である。
Along with the development of the steel manufacturing industry, the amount of molten blast furnace slag produced in Toyama from blast furnaces has also increased, but while some of it is effectively used for cement, the majority of it is difficult to dispose of. It is.

かかる溶融高炉スラグの処理には、従来二通りの方法が
行なわれている。その中の一つは、溶融高炉スラグを広
大な敷地に放流して自然冷却後、ブルドーザーなどで掘
り起し、適宜の大きさに破砕してバラスとして利用する
方法である。また他の一つは、溶融藤炉スラグに水を噴
射して急袷破砕して、直径5冊以下のいわゆる水砕スラ
グとなし、高炉セメントの原料とする方法である。とこ
ろで、建築・土木の分野で使用するコンクリート・モル
タルについて、天然砂の不足が指摘されてから久しい。
そこで天然砂に代る人工砂の研究が盛んで、高炉スラグ
のこの方面への適用も考えられているところである。と
ころが、前述のバラスの製造による方法では、主として
粒径の大きなものが得られるので、これを紬骨材とする
ためには、破砕しなければならないが、バラスは強度が
非常に大きいために、細骨材として適する粒度(5側以
下)に破砕することは極めて困難で、かつ不経済である
。また水砕スラグは直径5肋以下の粒径のものが大部分
であるから、粒径としては細骨村に適しているが、軟質
で粗しようなガラス質であるため、紬骨材として使用す
るためには、強度、比重、吸水率等に問題があり、不適
当である。本発明者等は溶融高炉スラグを主として紬骨
材として利用することを目的として研究を進めた結果、
水砕スラグをその製造過程において添加材を加えて重質
繊密化することが最も適当な方法であることを見究め、
その添加材としてセッコウ等の金属硫酸塩、亜硫酸カル
シウム等の金属亜硫酸塩を使用する本発明に到達した。
Conventionally, two methods have been used to treat such molten blast furnace slag. One of these methods is to discharge molten blast furnace slag onto a vast site, allow it to cool naturally, then dig it up with a bulldozer or the like, crush it into appropriate sizes, and use it as ballast. Another method is to inject water into the molten slag and crush it into so-called granulated slag with a diameter of 5 or less, which is used as a raw material for blast furnace cement. By the way, it has been a long time since it was pointed out that there was a shortage of natural sand for concrete and mortar used in the fields of architecture and civil engineering.
Therefore, research into artificial sand as an alternative to natural sand is active, and the application of blast furnace slag in this field is also being considered. However, the above-mentioned method of manufacturing ballast mainly yields large particles, which must be crushed in order to be used as pongee aggregate, but ballast has extremely high strength. It is extremely difficult and uneconomical to crush to a particle size suitable for fine aggregate (5 sides or less). In addition, since most of the granulated slag has a particle size of 5 ribs or less in diameter, it is suitable for small bone villages, but because it is soft and coarsely glassy, it is used as pongee aggregate. However, there are problems with strength, specific gravity, water absorption, etc., and it is inappropriate. The present inventors conducted research aimed at using molten blast furnace slag mainly as pongee aggregate, and as a result,
We determined that the most appropriate method is to add additives to granulated slag during the manufacturing process to make it heavy and granular.
The present invention has been achieved in which a metal sulfate such as gypsum or a metal sulfite such as calcium sulfite is used as the additive.

すなわち、本発明は溶融高炉スラグに金属硫酸塩および
金属亜硫酸塩からなる群から選ばれた少なくとも1種の
添加材を加え、添加材を添加してから水砕化するまでの
時間を添加材が溶融高炉スラグに実質的に溶解するに必
要な最低時間程度として溶融高炉スラグを水砕化するこ
とを特徴とする水砕スラグの製造方法である。
That is, the present invention adds at least one additive selected from the group consisting of metal sulfates and metal sulfites to molten blast furnace slag, and the time from the addition of the additive until granulation is determined by the additive. This is a method for producing granulated slag, characterized by pulverizing molten blast furnace slag for the minimum time required to substantially dissolve it into molten blast furnace slag.

本発明の添加材としては、例えばセッコウ、硫酸ソーダ
、硫酸鉄、硫酸鋼等の金属硫酸塩、亜硫酸カルシウム、
亜硫酸ソーダ等の金属塩があげられ、これは1種または
2種以上を混合して使用してもよい。
Examples of additives used in the present invention include gypsum, sodium sulfate, iron sulfate, metal sulfates such as steel sulfate, calcium sulfite,
Examples include metal salts such as sodium sulfite, which may be used alone or in combination of two or more.

特に好ましい添加材はセッコウであり、セツコウとして
は二水セッコウ(CaS04・2日20)、半水セッコ
ゥ(CaSC4・1/が20)、死焼セッコゥ(CaS
04)のいずれでもよく、乾燥したものでも湿潤状態の
ものでもよい。特に排煙脱硫工程から得られる排脱セッ
コウ、鱗脱亜硫酸カルシウムを使用することができる。
添加材は粉末状ないいま1仇舷以下の粒状であることが
望ましい。セッコゥ等の金属硫酸塩、亜硫酸塩は、水砕
スラグの重質繊密化に役立つが、それは溶融高炉スラグ
に対する溶解時間が短い場合に限られることが判った。
すなわち、添加材を添加してから水砕化するまでの時間
を、添加材が溶融高炉スラグにほぼ完全に溶融するに必
要な最低時間程度とすると、例えばセッコウ5%の添加
で比重において0.6(90%)向上し、客重において
は0.7(70%)向上した。そして、この重質繊密化
した水砕スラグは、客重、並びに比重がともに大きく、
吸水率は4・で、粗粒が多く、円形度も向上していて、
骨材の物理的性質として望ましい性質となる。また、添
加材の溶融高炉スラグに対する溶解時間を長くすると、
上記とは逆に軽質化し、例えばセッコゥ5%添加の場合
で比重が0.4(20%)低下し、客車は0.3(30
%)低下する。この軽質化した水砕スラグは植物栽培養
土壌材、地盤改良材として有用である。童質化と軽質化
とが別れるセッコウ等の添加材の溶解時間は約10分程
度のところである。
Particularly preferred additives are gypsum, and examples of the gypsum include dihydrous gypsum (CaS04, 2 days 20), semihydrous gypsum (CaSC4, 1/20), dead-fired gypsum (CaS
04) may be used, and may be dry or wet. In particular, it is possible to use desulfurized gypsum and desulfite scales obtained from flue gas desulfurization processes.
It is desirable that the additive material be in the form of a powder or granules of less than 1 ship size. It has been found that metal sulfates and sulfites, such as gypsum, are useful for making granulated slag heavy, but only when the dissolution time in molten blast furnace slag is short.
That is, if the time from the addition of the additive until granulation is the minimum time required for the additive to almost completely melt into molten blast furnace slag, for example, the addition of 5% gypsum will result in a specific gravity of 0. 6 (90%), and customer weight improved by 0.7 (70%). This heavy granulated slag has a high customer weight and specific gravity,
The water absorption rate is 4. There are many coarse particles and the circularity has improved.
This is a desirable physical property of aggregate. In addition, if the dissolution time of additives in molten blast furnace slag is increased,
Contrary to the above, the specific gravity decreases by 0.4 (20%) when 5% gypsum is added, and the passenger car becomes lighter by 0.3 (30%).
%)descend. This lightened granulated slag is useful as a nutrient soil material for plant cultivation and as a soil improvement material. The dissolution time of additives such as gypsum, which separates the difference between lightening and lightening, is about 10 minutes.

この溶解時間と各物理的性質との関係を実験によりしら
べた結果を図示する。第1図は繊密さ(絶乾見掛比重/
真比重)、第2図は吸水率、第3図は粗粒率を示し、何
れも実線は溶融時間が10分以内の場合、点線は同じく
20分以上の場合を示す。
The results of an experimental study of the relationship between this dissolution time and each physical property are illustrated. Figure 1 shows the fineness (absolutely dry apparent specific gravity/
(true specific gravity), Figure 2 shows the water absorption rate, and Figure 3 shows the coarse particle ratio, in both of which the solid line shows the case where the melting time is less than 10 minutes, and the dotted line shows the case where the melting time is 20 minutes or more.

何れの場合もセッコウの添加率1ないし5%の範囲で極
端な傾向差が見られる。一般に、添加材の添加率は溶融
高炉スラグに対し0.5〜10重量%の範囲内でよいが
、セッコウの場合は1〜5%の添加で最良の結果が得ら
れる。
In both cases, extreme differences in trends are seen within the range of gypsum addition rates of 1 to 5%. Generally, the addition rate of the additive may be within the range of 0.5 to 10% by weight based on the molten blast furnace slag, but in the case of gypsum, best results are obtained with addition of 1 to 5%.

セツコウ等の添加材の添加が何故水砕スラグの童質繊密
化に効果があるのか明らかではないが、溶解時間を長く
して軽質化する場合は、硫化カルシウムの添加効果と同
じ額向を示すので、おそらく溶解時間が長くなるにした
がって硫化カルシウムが生成し、その還元作用によって
軽質化が起るものと考えられる。本発明は、容易に入手
し易いセツコウ等の添加材の添加と時間調整という簡単
な手段によって、細骨材または地盤改良材として有用な
水砕スラグを製造することができるもので、資源の有効
利用と不足資源の不足の両見地から有用な発明である。
It is not clear why the addition of additives such as slag is effective in making the granulated slag granulated, but if the dissolution time is lengthened to make it lighter, the same amount of effect as the addition of calcium sulfide can be obtained. Therefore, it is thought that as the dissolution time increases, calcium sulfide is formed, and lightening occurs due to its reducing action. The present invention makes it possible to produce granulated slag that is useful as fine aggregate or ground improvement material by simply adding additives such as slag, which are easily available, and adjusting the time, thereby making it possible to use resources efficiently. This invention is useful both from the standpoint of utilization and the scarcity of scarce resources.

つぎに実施例について述べる。Next, examples will be described.

実施例 1 第1表の組成を有する乾燥高炉水砕スラグに外割で5重
量%の各種添加材を混合し、この混合物をカーボンルッ
ボに入れて高周波電気炉中で加熱溶解した。
Example 1 Dry granulated blast furnace slag having the composition shown in Table 1 was mixed with 5% by weight of various additives, and this mixture was placed in a carbon rubbo and heated and melted in a high frequency electric furnace.

溶解温度を1500q0とし、溶融スラグを水砕化試験
装置に導き、吹製水圧力2k9/地、水ノスラグ比10
〜10吹製水温度80qoで水砕化した。また、比較の
ため添加材なしのブランクテストを同機な条件で行なっ
た。第2表に実験結果を示す。スラグが完全に溶解する
に要する時間は20分程度なので表2の各試料は溶解後
1500ooに5〜IQ分間保持されたことになる。第
1表 (単位重量孫) Cの Si02Aと203胸ぬ F30Mn203 r
i02 S41.8 32.7 14.6 6.0
22 05 1.4 1.0第2表実施例
2 実施例1と同様な試験において、スラグのみを溶解し(
溶解時間40分)ついで原料スラグに対し、夫々0、1
、3、5重量%のセツコウ(CaS041犯20)を添
加混合して水砕化して得られた水砕化スラグの繊密さを
第1図、吸水率を第2図、粗粒率を第3図に示す。
The melting temperature was set to 1500q0, the molten slag was introduced into a granulation test device, the blowing water pressure was 2k9/ground, and the water noslag ratio was 10.
It was pulverized at a water temperature of 80 qo. In addition, for comparison, a blank test without additives was conducted under the same conditions. Table 2 shows the experimental results. Since it takes about 20 minutes for the slag to completely dissolve, each sample in Table 2 was held at 1500 oo for 5 to IQ minutes after being dissolved. Table 1 (unit weight) C Si02A and 203 breasts F30Mn203 r
i02 S41.8 32.7 14.6 6.0
22 05 1.4 1.0 Table 2 Examples
2 In a test similar to Example 1, only the slag was dissolved (
(Dissolution time: 40 minutes) Then, 0 and 1 were added to the raw slag, respectively.
Figure 1 shows the fineness of the granulated slag obtained by adding and mixing 3.5% by weight of Setsukou (CaS041 20), Figure 2 shows the water absorption rate, and Figure 2 shows the coarse particle ratio. Shown in Figure 3.

実線は添加後水砕化迄の保持時間1晩ご以内、点線は2
び分以上の場合である。実施例 3 実施例2と同様な試験において、セッコゥの代りに5重
量%の磯セッコゥを溶解スラグに添加して1粉ご放置後
水砕化して得られた水砕スラグの繊密さは0.87、吸
水率は2.2%、粗粒率は4.05であった。
The solid line indicates the retention time after addition until granulation, which is less than 1 night, and the dotted line indicates the retention time after addition until granulation.
This is the case when the amount exceeds the Example 3 In a test similar to Example 2, 5% by weight of Iso gypsum was added to the molten slag instead of gypsum, and the granulated slag was left to stand and then granulated, resulting in a granulated slag with a fineness of 0. .87, water absorption rate was 2.2%, and coarse particle rate was 4.05.

【図面の簡単な説明】[Brief explanation of drawings]

第1図ないし第3図は本発明における試験結果を示すグ
ラフで、夫々第1図は繊密さ、第2図は吸水率、第3図
は粗粒率に関するものである。 第1図第2図 第3図
Figures 1 to 3 are graphs showing the test results of the present invention, with Figure 1 relating to fineness, Figure 2 relating to water absorption, and Figure 3 relating to coarse grain ratio. Figure 1 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】 1 溶融高炉スラグに金属硫酸塩および金属亜硫酸塩か
らなる群から選ばれた少なくとも1種の添加材を加え、
添加材を添加してから水砕化するまでの時間を添加材が
溶融高炉スラグに実質的に溶解する必要な最低時間程度
として溶融高スラグを水砕化することを特徴とする水砕
スラグの製造方法。 2 添加材の添加量が溶融高炉スラグに対し0.1〜1
0重量%である特許請求の範囲第1項記載の水砕スラグ
の製造方法。 3 添加材がセツコウである特許請求の範囲第1項記載
の水砕スラグの製造方法。 4 セツコウの添加量が溶融高炉スラグに対し1〜5重
量%である特許請求の範囲第3項記載の水砕スラグの製
造方法。
[Claims] 1. Adding at least one additive selected from the group consisting of metal sulfates and metal sulfites to molten blast furnace slag,
The granulated slag is characterized in that the molten high-density slag is granulated by setting the time from the addition of the additive to the granulation as the minimum time necessary for the additive to be substantially dissolved in the molten blast furnace slag. Production method. 2 The amount of additive added is 0.1 to 1 to molten blast furnace slag.
The method for producing granulated slag according to claim 1, wherein the content is 0% by weight. 3. The method for producing granulated slag according to claim 1, wherein the additive is slag. 4. The method for producing granulated slag according to claim 3, wherein the amount of slag added is 1 to 5% by weight based on the molten blast furnace slag.
JP52067981A 1977-06-10 1977-06-10 Method for producing granulated slag Expired JPS602262B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52067981A JPS602262B2 (en) 1977-06-10 1977-06-10 Method for producing granulated slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52067981A JPS602262B2 (en) 1977-06-10 1977-06-10 Method for producing granulated slag

Publications (2)

Publication Number Publication Date
JPS542995A JPS542995A (en) 1979-01-10
JPS602262B2 true JPS602262B2 (en) 1985-01-21

Family

ID=13360662

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52067981A Expired JPS602262B2 (en) 1977-06-10 1977-06-10 Method for producing granulated slag

Country Status (1)

Country Link
JP (1) JPS602262B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6158846A (en) * 1984-08-31 1986-03-26 株式会社竹中工務店 Method of foaming molten slag

Also Published As

Publication number Publication date
JPS542995A (en) 1979-01-10

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