JP2014196218A - Method for producing roadbed material - Google Patents
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- JP2014196218A JP2014196218A JP2013073113A JP2013073113A JP2014196218A JP 2014196218 A JP2014196218 A JP 2014196218A JP 2013073113 A JP2013073113 A JP 2013073113A JP 2013073113 A JP2013073113 A JP 2013073113A JP 2014196218 A JP2014196218 A JP 2014196218A
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- 239000000463 material Substances 0.000 title claims abstract description 64
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- 239000002893 slag Substances 0.000 claims abstract description 150
- 239000008187 granular material Substances 0.000 claims abstract description 22
- 230000032683 aging Effects 0.000 claims abstract description 19
- 238000002156 mixing Methods 0.000 claims abstract description 7
- 239000002245 particle Substances 0.000 claims description 45
- 239000010419 fine particle Substances 0.000 claims description 39
- 238000000034 method Methods 0.000 claims description 25
- 229910052782 aluminium Inorganic materials 0.000 claims description 9
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 8
- 238000011282 treatment Methods 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 4
- 238000007922 dissolution test Methods 0.000 claims description 4
- 239000013618 particulate matter Substances 0.000 claims description 4
- 239000011593 sulfur Substances 0.000 claims description 4
- 229910052717 sulfur Inorganic materials 0.000 claims description 4
- 238000004090 dissolution Methods 0.000 claims 1
- 229910001653 ettringite Inorganic materials 0.000 abstract description 24
- 238000010828 elution Methods 0.000 abstract description 19
- 239000002994 raw material Substances 0.000 abstract description 8
- 229910000831 Steel Inorganic materials 0.000 description 16
- 239000010959 steel Substances 0.000 description 16
- 238000010583 slow cooling Methods 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- 239000000047 product Substances 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 7
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 3
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004503 fine granule Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000009628 steelmaking Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- FAYYUXPSKDFLEC-UHFFFAOYSA-L calcium;dioxido-oxo-sulfanylidene-$l^{6}-sulfane Chemical compound [Ca+2].[O-]S([O-])(=O)=S FAYYUXPSKDFLEC-UHFFFAOYSA-L 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 238000005261 decarburization Methods 0.000 description 1
- 150000004683 dihydrates Chemical class 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000007572 expansion measurement Methods 0.000 description 1
- 230000002431 foraging effect Effects 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
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- 238000010998 test method Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000010333 wet classification Methods 0.000 description 1
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- Curing Cements, Concrete, And Artificial Stone (AREA)
- Road Paving Structures (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
本発明は、高炉徐冷スラグを含む複合路盤材の製造方法に関する。 The present invention relates to a method for manufacturing a composite roadbed material including a blast furnace slow cooling slag.
高炉で生成するスラグには、吹製水により急冷した水砕スラグと、ドライピット等で比較的ゆっくりと冷却した徐冷スラグがある。このうち高炉水砕スラグはセメント原料やコンクリート骨材などに利用され、高炉徐冷スラグは主に路盤材に利用されている。高炉スラグ中には1質量%程度のSが含まれており、高炉徐冷スラグについては、それが原因で黄水が発生する場合があるため、粉砕して粒度調整を行った後に、数ヶ月程度のエージング期間を経てSを十分に酸化させてから出荷されている。 The slag generated in the blast furnace includes granulated slag that has been rapidly cooled by blown water and slowly cooled slag that has been cooled relatively slowly by dry pits or the like. Of these, granulated blast furnace slag is used for cement raw materials and concrete aggregates, and blast furnace slow-cooled slag is mainly used for roadbed materials. The blast furnace slag contains about 1% by mass of S, and the blast furnace slow-cooled slag may generate yellow water due to this. It is shipped after sufficiently oxidizing S after a certain aging period.
高炉徐冷スラグを使用した路盤材において、極稀にエトリンガイト(3CaO・Al2O3・3CaSO4・32H2O)生成による膨張が生じることがある。このエトリンガイトは、高炉徐冷スラグから供給される硫酸イオンと、それ自身または、その他の原料や環境下に存在するCa,Alとの反応により生成するものと推定される。
このような問題に対して、特許文献1には、エトリンガイトの生成による膨張を防止するための、鉄鋼スラグなどの路盤材用原料の選別方法として、各原料からの溶出イオンの濃度を測定した結果に基づいて、特定の条件を満たすように選別した材料を組み合わせることが開示されている。
In roadbed material using slowly cooled blast furnace slag, resulting expansion by extremely rare in ettringite (3CaO · Al 2 O 3 · 3CaSO 4 · 32H 2 O) generated. This ettringite is presumed to be produced by the reaction of sulfate ions supplied from the blast furnace slow-cooled slag with Ca or Al present in itself or in other raw materials or environments.
For such a problem, Patent Document 1 discloses a result of measuring the concentration of ions eluted from each raw material as a method for selecting raw materials for roadbed materials such as steel slag to prevent expansion due to the formation of ettringite. Based on the above, it is disclosed to combine materials selected to meet specific conditions.
特許文献1の路盤材用原料の選別方法では、配合の制約条件が厳しく、硫酸イオンやアルミニウムの溶出濃度の高い特定のスラグ種の路盤材への利用が制限されるという問題があった。安定して大きな需要のある路盤材は、鉄鋼スラグの用途として重要なものの一つであり、この路盤材への利用が制限されると、スラグの在庫量が著しく増大してしまう場合がある。硫酸イオンの溶出濃度が製鋼スラグに比べて高い高炉徐冷スラグは、発生量および体積安定性などの特性の面で路盤材に適した鉄鋼スラグであり、最も一般的に路盤材に用いられるスラグ種であることから、これと組み合わせた場合にエトリンガイトを生成し易いアルミニウムの溶出濃度の高いスラグ種は、特に利用が制限されていた。 In the method for selecting a raw material for roadbed material in Patent Document 1, there are problems that the restrictions on the mixing are severe and the use of a specific slag species having a high elution concentration of sulfate ions or aluminum is limited. A roadbed material that is stably in great demand is one of the important applications for steel slag, and if the use for this roadbed material is restricted, the amount of slag stock may increase significantly. Blast furnace annealed slag, whose sulfate ion elution concentration is higher than that of steelmaking slag, is a steel slag that is suitable for roadbed materials in terms of characteristics such as generation amount and volume stability, and is the most commonly used slag for roadbed materials. Since it is a seed, the use of a slag species having a high elution concentration of aluminum that easily produces ettringite when combined with this has been particularly limited.
したがって本発明の目的は、高炉徐冷スラグと他の粒状物(一般に他の鉄鋼スラグ)を原料とする路盤材の製造方法において、当該他の粒状物として、エトリンガイト生成に関わる成分(アルミニウムなど)の溶出濃度が高いものを使用した場合でも、エトリンガイト生成に起因した膨張を生じにくい路盤材を製造することができる路盤材の製造方法を提供することにある。 Accordingly, an object of the present invention is to provide a method for producing roadbed material using blast furnace slow-cooled slag and other granular materials (generally other steel slags) as raw materials, such as other components related to ettringite generation (such as aluminum). An object of the present invention is to provide a method for producing a roadbed material that can produce a roadbed material that is less likely to cause expansion due to ettringite formation even when a material having a high elution concentration is used.
本発明者らは、路盤材原料として最も一般的な鉄鋼スラグである高炉徐冷スラグに着目して、エトリンガイト生成の重要な要素である硫酸イオンの水への溶出量を小さくする方策について検討を行った。その結果、高炉徐冷スラグは、その細粒側に硫酸源が濃化しており、したがって、粉砕及びエージングを行った高炉徐冷スラグから細粒分を除去することにより、高炉徐冷スラグに含まれる硫酸源を効果的に低減させることができ、このため、高炉徐冷スラグと混合する他の粒状物として、エトリンガイト生成に関わる成分(アルミニウムなど)の溶出濃度が高いものを使用した場合でも、エトリンガイト生成に起因した膨張を生じにくい路盤材を製造できることを見出した。 The inventors focused on the blast furnace slow-cooled slag, which is the most common steel slag as a roadbed material material, and examined measures to reduce the elution amount of sulfate ions into water, which is an important element of ettringite formation. went. As a result, the blast furnace slow-cooled slag has a concentrated sulfuric acid source on its fine grain side, and therefore, it is included in the blast furnace slow-cooled slag by removing fine particles from the ground and aged blast furnace slow-cooled slag. The amount of sulfuric acid that can be effectively reduced can be effectively reduced. For this reason, even when a high particulate elution concentration of ettringite (such as aluminum) is used as the other granular material mixed with the blast furnace annealing slag, It was found that a roadbed material that is less prone to expansion due to ettringite formation can be produced.
本発明は、このような知見に基づきなされたもので、以下を要旨とするものである。
[1]溶融状態の高炉スラグを凝固させて得られた高炉徐冷スラグを粉砕する工程(A)と、該工程(A)を経た高炉徐冷スラグをエージングする工程(B)と、該工程(B)を経た高炉徐冷スラグから粒径0.075mm以下の細粒分を除去する工程(C)と、該工程(C)を経た高炉徐冷スラグに高炉徐冷スラグ以外の粒状物を混合する工程(D)を有することを特徴とする路盤材の製造方法。
[2]上記[1]の製造方法において、工程(C)を経た後の高炉徐冷スラグ中に占める粒径0.075mm以下の細粒分の割合が1質量%未満であることを特徴とする路盤材の製造方法。
The present invention has been made on the basis of such knowledge and has the following gist.
[1] A step (A) of pulverizing blast furnace slow-cooled slag obtained by solidifying molten blast furnace slag, a step (B) of aging the blast furnace slow-cooled slag that has undergone the step (A), and the step A step (C) for removing fine particles having a particle size of 0.075 mm or less from the blast furnace slow-cooled slag that has passed through (B), and a particulate matter other than the blast furnace slow-cooled slag that has passed through the step (C) A method for producing a roadbed material comprising the step (D) of mixing.
[2] In the production method of [1] above, the proportion of fine particles having a particle size of 0.075 mm or less in the blast furnace slow cooling slag after the step (C) is less than 1% by mass. Manufacturing method for roadbed material.
[3]上記[1]又は[2]の製造方法において、工程(D)で高炉徐冷スラグに混合する粒状物は、硫黄含有量が0.3質量%以下、アルミニウム溶出量がJIS K0058−1で規定する溶出試験方法に基づく測定値で1.5mg/L以上であることを特徴とする路盤材の製造方法。
[4]上記[1]〜[3]のいずれかの製造方法において、工程(D)を経て得られた路盤材中に占める粒径0.075mm以下の細粒分の割合が2質量%以上であることを特徴とする路盤材の製造方法。
[5]上記[1]〜[4]のいずれかの製造方法において、工程(C)における細粒分を除去する処理が、機械式分級装置による処理を含むものであることを特徴とする路盤材の製造方法。
[6]上記[1]〜[4]のいずれかの製造方法において、工程(C)における細粒分を除去する処理が、湿式の洗浄式分級装置による処理を含むものであることを特徴とする路盤材の製造方法。
[3] In the production method of [1] or [2] above, the particulate matter mixed in the blast furnace slow cooling slag in step (D) has a sulfur content of 0.3 mass% or less and an aluminum elution amount of JIS K0058- A method for producing a roadbed material, wherein the measured value based on the dissolution test method specified in 1 is 1.5 mg / L or more.
[4] In the production method according to any one of [1] to [3], the proportion of fine particles having a particle size of 0.075 mm or less in the roadbed material obtained through the step (D) is 2% by mass or more. A method for producing a roadbed material, characterized in that:
[5] In the manufacturing method according to any one of [1] to [4], the process for removing fine particles in the step (C) includes a process by a mechanical classifier. Production method.
[6] The roadbed according to any one of the above [1] to [4], wherein the treatment for removing the fine particles in the step (C) includes treatment by a wet cleaning type classifier A method of manufacturing the material.
本発明法によれば、原料である高炉徐冷スラグからの硫酸イオンの溶出量を大幅に低減することができるため、高炉徐冷スラグと混合する他の粒状物(一般に他の鉄鋼スラグ)として、エトリンガイト生成に関わる成分(アルミニウムなど)の溶出濃度が高いものを使用した場合でも、エトリンガイト生成に起因した膨張を生じにくい路盤材を製造することができる。このため、エトリンガイト生成による膨張のリスクを回避しつつ、高炉徐冷スラグの路盤材への利用を拡大することができるだけでなく、高炉徐冷スラグと混合する粒状物として、エトリンガイト生成に関与する成分の溶出濃度の高いスラグ種を適用することが可能となり、そのようなスラグ種の利用を拡大することができる。 According to the method of the present invention, since the elution amount of sulfate ions from the blast furnace slow-cooled slag, which is a raw material, can be greatly reduced, as other granular materials (generally other steel slag) mixed with the blast furnace slow-cooled slag Even when an elution concentration of a component (such as aluminum) related to ettringite generation is high, a roadbed material that is less likely to cause expansion due to ettringite generation can be manufactured. For this reason, while avoiding the risk of expansion due to ettringite generation, it is possible not only to expand the use of blast furnace slow cooling slag to roadbed materials, but also as a particulate matter mixed with blast furnace slow cooling slag, components involved in ettringite generation It is possible to apply slag species having a high elution concentration of slag, and the use of such slag species can be expanded.
本発明の路盤材の製造方法は、溶融状態の高炉スラグを凝固させて得られた高炉徐冷スラグを粉砕する工程Aと、この工程Aを経た高炉徐冷スラグをエージングする工程Bと、この工程Bを経た高炉徐冷スラグから粒径0.075mm以下の細粒分を除去する工程Cと、この工程Cを経た高炉徐冷スラグに高炉徐冷スラグ以外の粒状物を混合する工程Dを有する。 The method for producing a roadbed material according to the present invention includes a step A for pulverizing a blast furnace slow-cooled slag obtained by solidifying a molten blast furnace slag, a step B for aging the blast furnace slow-cooled slag after the step A, and A process C for removing fine particles having a particle size of 0.075 mm or less from the blast furnace annealed slag that has undergone the process B, and a process D in which particulates other than the blast furnace annealed slag are mixed with the blast furnace annealed slag that has undergone the process C. Have.
溶融状態の高炉スラグを凝固させて得られた高炉徐冷スラグは、まず、路盤材に適した粒度に粉砕される(工程A)。その粉砕方法や手段は、一般的なものでよい。なお、この粉砕工程では、通常、粉砕された高炉徐冷スラグを篩にかけ、篩上のスラグを再度粉砕ラインに戻すことにより粒度調整を行い、所定の粒度の高炉徐冷スラグを得る。このようにして粉砕された高炉徐冷スラグは、路盤材として使用された際に黄水の発生を抑制するために、エージング処理される(工程B)。エージングには、スラグ中に含まれるS分を酸化する効果があり、S分をチオ硫酸(S2O3)や硫酸(SO4)まで酸化すると、黄水の発生が抑制できる。エージングは、大気エージング、蒸気エージングなどのいずれでもよい。エージング期間は任意であるが、通常、大気エージングでは2〜6ヶ月程度、蒸気エージングでは2日〜1週間程度が目安となる。エージングがされた高炉徐冷スラグは、呈色試験により黄水が生成しないことを確認した後、次工程に移される。 First, the blast furnace slow-cooled slag obtained by solidifying the molten blast furnace slag is pulverized to a particle size suitable for a roadbed material (step A). The pulverization method and means may be general. In this pulverization step, usually, pulverized blast furnace chilled slag is passed through a sieve, and the slag on the sieve is returned to the pulverization line to adjust the particle size, thereby obtaining blast furnace chilled slag having a predetermined particle size. The blast furnace slow cooling slag thus pulverized is subjected to an aging treatment in order to suppress the generation of yellow water when used as a roadbed material (step B). Aging has the effect of oxidizing S contained in the slag, and when the S content is oxidized to thiosulfuric acid (S 2 O 3 ) or sulfuric acid (SO 4 ), the generation of yellow water can be suppressed. The aging may be any of atmospheric aging, steam aging and the like. Although the aging period is arbitrary, it is generally about 2 to 6 months for atmospheric aging and about 2 days to 1 week for steam aging. The blast furnace slow-cooled slag subjected to aging is transferred to the next step after confirming that no yellow water is generated by a color test.
次に、エージングを経た高炉徐冷スラグから粒径0.075mm以下の細粒分を除去する(工程C)。ここで、高炉徐冷スラグから粒径0.075mm以下の細粒分を除去するとは、高炉徐冷スラグ中の当該細粒分の一部を除去する場合を含む。
図1に、エージング後の高炉徐冷スラグ(粒度調整鉄鋼スラグ路盤「MS−25」相当)の粒度別のS含有率(T.S)とSO4含有率を示す。有姿の高炉徐冷スラグのS含有率は0.68質量%、SO4含有率は0.84質量%であり、S全体の41%がSO4になっている。これに対して、粒径0.075mm以下の高炉徐冷スラグは、S含有率が1.84質量%と、有姿の高炉徐冷スラグの2.7倍のSを含有し、また、SO4含有率は4.5質量%であり、S全体の82%がSO4になっている。
Next, fine particles having a particle size of 0.075 mm or less are removed from the aging-cooled blast furnace slag (step C). Here, removing the fine particles having a particle size of 0.075 mm or less from the blast furnace slow-cooled slag includes removing a part of the fine particles in the blast furnace slow-cooled slag.
FIG. 1 shows the S content (TS) and SO 4 content by particle size of the blast furnace slow-cooled slag after aging (corresponding to particle size-adjusted steel slag roadbed “MS-25”). The solid blast furnace chilled slag has an S content of 0.68% by mass, an SO 4 content of 0.84% by mass, and 41% of the total S is SO 4 . On the other hand, the blast furnace annealed slag having a particle size of 0.075 mm or less contains 1.84% by mass of S, 2.7 times as much as the solid blast furnace annealed slag, and SO 4 The content is 4.5% by mass, and 82% of the total S is SO 4 .
上記のように高炉徐冷スラグの細粒分(粒径0.075mm以下)にSO4が濃化しているのは、次のような理由によるものと考えられる。すなわち、チオ硫酸や硫酸は水への溶解度が比較的高いため、高炉徐冷スラグ中のSは、その周囲に存在する水分へ酸化されながら溶解することになる。酸化挙動は、まずチオ硫酸となり、その後硫酸へと進行することになるが、例えば、チオ硫酸カルシウムの溶解度が712g/Lであるに対して、硫酸カルシウムの溶解度は1.76g/L程度であり、酸化が進むことで、2水石膏のようにSO4を含む析出物が生じることになる。そして、その析出物は粒子が小さいので、微粉として存在する形態となることが多い。このため、図1に示されるように、高炉徐冷スラグの細粒分(粒径0.075mm以下)にSO4が濃化することになる。このような細粒分は、路盤材として使用する環境下において、水との新たな接触でSO4分として供給する能力が高い。 The reason why SO 4 is concentrated in the fine particles (particle size of 0.075 mm or less) of the blast furnace slow-cooled slag as described above is considered to be as follows. That is, since thiosulfuric acid and sulfuric acid have a relatively high solubility in water, S in the blast furnace slow-cooled slag dissolves while being oxidized into moisture present around it. The oxidation behavior first becomes thiosulfuric acid and then proceeds to sulfuric acid. For example, the solubility of calcium thiosulfate is about 712 g / L, whereas the solubility of calcium sulfate is about 1.76 g / L. As the oxidation proceeds, a precipitate containing SO 4 is produced like dihydrate gypsum. And since the deposit has small particle | grains, it becomes a form which exists as fine powder in many cases. For this reason, as shown in FIG. 1, SO 4 is concentrated in the fine particles (particle size of 0.075 mm or less) of the blast furnace slow cooling slag. Such fine particles have a high ability to be supplied as SO 4 in a new contact with water in an environment used as a roadbed material.
そこで、本発明では、篩い分けなどにより高炉徐冷スラグの細粒分を削減することで、エトリンガイト生成の主原因となるSO4分を低減させる。これにより、路盤材のエトリンガイト膨張を抑制することができる。
工程Cにおいて、高炉徐冷スラグ中の粒径0.075mm以下の細粒分は、なるべく除去されることが好ましく、工程Cを経た後の高炉徐冷スラグ中に占める粒径0.075mm以下の細粒分の割合は1質量%未満であることが好ましい。一般にエージング後の高炉徐冷スラグには粒径0.075mm以下の細粒分が5〜6質量%程度含まれており、これを1質量%未満まで低減することにより、細粒分に濃化したSO4を十分に低減させることができる。
Therefore, in the present invention, by reducing the fine granule content of the blast furnace annealed slag by sieving or the like, the SO 4 content that is the main cause of ettringite formation is reduced. Thereby, the ettringite expansion of the roadbed material can be suppressed.
In Step C, the fine particles having a particle size of 0.075 mm or less in the blast furnace annealed slag are preferably removed as much as possible, and the particle size of 0.075 mm or less in the blast furnace annealed slag after Step C is removed. The proportion of fine particles is preferably less than 1% by mass. Generally, the blast furnace chilled slag after aging contains about 5 to 6% by mass of fine particles having a particle size of 0.075 mm or less, and by reducing this to less than 1% by mass, the fine particles are concentrated. Thus, SO 4 can be sufficiently reduced.
工程Cにおいて高炉徐冷スラグから粒径0.075mm以下の細粒分を除去する処理は、任意の方法で行うことができるが、一般には、機械式分級装置による処理、湿式の洗浄式分級装置による処理などが行われる。これらの処理は2種以上を併用してもよい。
機械式分級装置による処理では、例えば、高炉徐冷スラグを篩目が0.075mm〜5mm程度の篩を通過させ、その篩上を路盤材原料とする。
湿式の洗浄式分級装置による処理では、水中で高炉水砕スラグを洗浄することで細粒分を洗い流し(細粒分を分離除去する)、沈降するなどして残った粗粒分を回収するものであり、例えば、砂などの洗浄や湿式分級を行う従来装置を利用して行うことができる。
The process of removing fine particles having a particle size of 0.075 mm or less from the blast furnace slow-cooled slag in Step C can be performed by any method, but in general, a process by a mechanical classifier, a wet cleaning classifier Processing by is performed. Two or more of these treatments may be used in combination.
In the treatment by the mechanical classifier, for example, the blast furnace slow cooling slag is passed through a sieve having a sieve mesh of about 0.075 mm to 5 mm, and the sieve top is used as a roadbed material.
In the treatment with a wet cleaning type classifier, the fine granule is washed away by washing the granulated blast furnace slag in water (the fine fraction is separated and removed), and the remaining coarse fraction is recovered by sedimentation. For example, it can be performed using a conventional apparatus that performs sand cleaning or wet classification.
次に、工程Cを経て細粒分が除去された高炉徐冷スラグ(以下、「高炉徐冷スラグx」という)に、高炉徐冷スラグ以外の粒状物(以下、「粒状物y」という)を混合し(工程D)、この混合物を路盤材とする。高炉徐冷スラグxに混合する粒状物yは、路盤材原料として使用できるものであれば、種類などに特別な制限はないが、本発明の効果は、エトリンガイト生成に関わる成分(アルミニウムなど)の溶出濃度が高い粒状物を使用する場合でも、エトリンガイト生成に起因した膨張を生じにくい路盤材が製造できるということなので、アルミニウムの溶出濃度がある程度高い粒状物y、具体的には、アルミニウム溶出量がJIS K0058−1で規定する溶出試験方法に基づく測定値で1.5mg/L以上であるような粒状物yが好ましい。また、当然のことながら、粒状物yは硫黄分が低いことが好ましく、硫黄含有量が0.3質量%以下であることが好ましい。 Next, in the blast furnace slow-cooled slag (hereinafter referred to as “blast furnace slow-cooled slag x”) from which fine particles have been removed through the step C, granular materials other than the blast furnace slow-cooled slag (hereinafter referred to as “granular material y”). (Step D), and this mixture is used as a roadbed material. The granular material y mixed with the blast furnace slow-cooled slag x is not particularly limited as long as it can be used as a roadbed material, but the effect of the present invention is that of components related to ettringite production (such as aluminum). Even when granular materials with high elution concentration are used, it is possible to produce a roadbed material that does not easily cause expansion due to ettringite formation. A granular material y having a measured value based on the dissolution test method specified in JIS K0058-1 is 1.5 mg / L or more is preferable. As a matter of course, the granular material y preferably has a low sulfur content, and preferably has a sulfur content of 0.3% by mass or less.
上記のような条件に合致する粒状物yとしては、Al2O3含有量の高い製鋼スラグ、溶融還元スラグ、高炉水砕スラグなどの鉄鋼スラグや、粗骨材などの砕石製造時に発生する砕砂などが挙げられ、これらの1種以上を用いることができる。製鋼スラグには、溶銑予備処理スラグ(脱燐スラグ、脱珪スラグなど)、転炉脱炭スラグ、電気炉スラグ、二次精錬スラグ、鋳造スラグ、造塊スラグなどがある。これらのなかで、特に鋳造スラグや造塊スラグはAl2O3含有量が10質量%を超えることが多いので、本発明を適用して有効利用するのに適している。
粒状物yの粒度は、高炉徐冷スラグxと混合した後の混合物(路盤材)が所望の粒度となるように選択すればよい。
As the granular material y meeting the above conditions, steel slag having a high Al 2 O 3 content, smelting reduction slag, blast furnace granulated slag and other steel slag, and crushed sand generated during the production of crushed stone such as coarse aggregate One or more of these can be used. Steelmaking slag includes hot metal pretreatment slag (dephosphorization slag, desiliconization slag, etc.), converter decarburization slag, electric furnace slag, secondary refining slag, cast slag, and ingot slag. Among these, in particular, cast slag and ingot slag often have an Al 2 O 3 content exceeding 10% by mass, and thus are suitable for effective use by applying the present invention.
What is necessary is just to select the particle size of the granular material y so that the mixture (roadbed material) after mixing with the blast furnace slow cooling slag x may become a desired particle size.
工程Dを経て得られた路盤材(高炉徐冷スラグxと粒状物yとの混合物)の粒度に特別な制限はないが、JIS A5015には、鉄鋼スラグ路盤材の粒度分布が示されている。これによると、例えば、粒度調整鉄鋼スラグ路盤材である「MS−25」の粒度は、0.075mm以下が2〜10質量%、0.425mm以下が10〜30質量%、2.36mm以下が20〜50質量%である。この粒度調整鉄鋼スラグ路盤材は上層路盤用であり、支持力を確保するために細粒分を含むものである。したがって、本発明法によりこのようなJIS製品を製造する場合、工程Dを経て得られた路盤材中に占める粒径0.075mm以下の細粒分の割合が2質量%以上であることが必要である。この製品は、細粒分が多いため、従来の高炉徐冷スラグを用いた製造方法では、配合によっては膨張しやすく、また固結強度も高いことから膨張した場合に路盤の破損を招きやすい。このため、本発明法を適用して膨張を防止することが特に有効な製品である。 There is no particular limitation on the particle size of the roadbed material (mixture of blast furnace slow-cooled slag x and granular material y) obtained through Step D, but JIS A5015 shows the particle size distribution of the steel slag roadbed material. . According to this, for example, the particle size of “MS-25”, which is a particle size-adjusted steel slag roadbed material, is 2 to 10 mass% for 0.075 mm or less, 10 to 30 mass% for 0.425 mm or less, and 2.36 mm or less. It is 20-50 mass%. This particle size-adjusted steel slag roadbed material is for upper-layer roadbed, and contains fine particles to ensure support. Therefore, when manufacturing such a JIS product according to the method of the present invention, the proportion of fine particles having a particle size of 0.075 mm or less in the roadbed material obtained through Step D needs to be 2% by mass or more. It is. Since this product has a large amount of fine particles, the production method using the conventional blast furnace slow cooling slag tends to expand depending on the blending, and since it has high consolidation strength, it tends to cause damage to the roadbed. Therefore, it is a particularly effective product to prevent expansion by applying the method of the present invention.
本発明法によって、上記のようなJIS製品である粒度調整鉄鋼スラグ路盤材を製造する際に、工程Cで高炉徐冷スラグ中の細粒分(例えば、粒径0.425mm以下の細粒分)の割合が十分に低減した場合には、路盤材として必要な細粒分を、高炉徐冷スラグxに混合する粒状物yの細粒分で補う必要がある。一方、同じJIS製品であるクラッシャラン鉄鋼スラグ(例えば「CS−40」)の粒度は、0.425mm以下の規定がなく、2.36mm以下は5〜25質量%という規定であり、したがって、工程Cで高炉徐冷スラグ中の細粒分(例えば、粒径0.425mm以下の細粒分)の割合が十分に低減した場合でも、特に粒状物yの細粒分で補う必要がない場合もある。
工程Dを経た高炉徐冷スラグxと粒状物yの混合物は、通常、そのまま路盤材として出荷される。
When the grain size-adjusted steel slag roadbed material, which is a JIS product as described above, is produced by the method of the present invention, the fine particles in the blast furnace slow-cooled slag (for example, fine particles having a particle size of 0.425 mm or less) in Step C. ) Is sufficiently reduced, it is necessary to supplement the fine particles necessary for the roadbed material with the fine particles of the granular material y mixed with the blast furnace slow cooling slag x. On the other hand, the particle size of crusheran iron and steel slag (for example, “CS-40”), which is the same JIS product, is not regulated to 0.425 mm or less, and 2.36 mm or less is regulated to 5 to 25% by mass. Even when the proportion of fine particles in the blast furnace slow-cooled slag (for example, fine particles having a particle size of 0.425 mm or less) is sufficiently reduced, it may not be particularly necessary to supplement with the fine particles of the granular material y. .
The mixture of the blast furnace slow cooling slag x and the granular material y which passed through the process D is normally shipped as a roadbed material as it is.
・実施例1(試験例)
高炉徐冷スラグをエージングしたままのスラグa、高炉徐冷スラグをエージングした後、粒径0.075mm以下の細粒分を取り除いたスラグb、鋳造スラグcを各々微粉砕し、粒径0.075mm以下の粉砕品とした。鋳造スラグcは高炉徐冷スラグよりもAlが溶出しやすいスラグである。
スラグa、bの粉砕品に対して、スラグcの粉砕品を3質量%添加して混合し、[試料a+c]、[試料b+c]とした。これらの試料を、50mmφ×40mm高さにプレス成型(2トン/cm2)した後、その成型品を金型に入れ、30℃の水槽内で高さ方向の膨張量を測定した。その結果、10日間での[試料b+c]の膨張量は0.5%未満であったが、[試料a+c]の膨張量は約2%と大きい値であった。
また、膨張測定後の試料に対してX線解析を実施した結果、[試料b+c]ではエトリンガイトは検出されなかったが、[試料a+c]ではエトリンガイトが検出され、エトリンガイトの生成が確認された。
-Example 1 (test example)
After aging the blast furnace slow-cooled slag and the blast furnace slow-cooled slag, the slag b and cast slag c from which fine particles having a particle size of 0.075 mm or less were removed were finely pulverized. The pulverized product was 075 mm or less. The cast slag c is a slag from which Al is more easily eluted than the blast furnace slow-cooled slag.
3% by mass of the slag c pulverized product was added to and mixed with the slag a and b crushed products to obtain [sample a + c] and [sample b + c]. These samples were press-molded to a height of 50 mmφ × 40 mm (2 ton / cm 2 ), and then the molded product was placed in a mold and the amount of expansion in the height direction was measured in a 30 ° C. water tank. As a result, the expansion amount of [Sample b + c] in 10 days was less than 0.5%, but the expansion amount of [Sample a + c] was a large value of about 2%.
Further, as a result of performing X-ray analysis on the sample after the expansion measurement, ettringite was not detected in [Sample b + c], but ettringite was detected in [Sample a + c], and production of ettringite was confirmed.
・実施例2
表1に示す粒度、成分、溶出特性を有するスラグA〜Dを用い、表2に示す路盤材を製造した。表1に示すSO4溶出量とAl溶出量は、JIS K0058−1で規定する溶出試験方法に基づく測定値である。
高炉徐冷スラグは、インパクトクラッシャーにより粉砕した後、粒径25mm以下に粒度調整し、これを3ヶ月間大気エージングした。本発明例で使用したスラグBは、このエージング後の高炉徐冷スラグを湿式の洗浄式分級装置により粒径0.075mm以下の細粒分を除去し、粒径0.075mm超、25mm以下の粒度とした。比較例および参考例で使用したスラグAは、エージングしたままの高炉徐冷スラグである。
Example 2
The roadbed materials shown in Table 2 were manufactured using slags AD having particle sizes, components, and elution characteristics shown in Table 1. The SO 4 elution amount and Al elution amount shown in Table 1 are measured values based on the dissolution test method defined in JIS K0058-1.
The blast furnace slow-cooled slag was pulverized with an impact crusher, adjusted to a particle size of 25 mm or less, and subjected to atmospheric aging for 3 months. The slag B used in the example of the present invention was obtained by removing fine particles having a particle size of 0.075 mm or less from the blast furnace chilled slag after the aging with a wet cleaning type classifier, and having a particle size of more than 0.075 mm and less than 25 mm. Grain size. Slag A used in the comparative example and the reference example is a blast furnace slow-cooled slag as it is aged.
スラグC(製鋼スラグ,S含有量0.02質量%),スラグD(高炉水砕スラグ,S含有量0.8質量%)は、高炉徐冷スラグに混合する粒状物として使用した。
製造された路盤材を、JIS A5015の付属書2に準拠した水浸膨張試験に供した。ただし、温度と測定時間については、30℃で1年間の試験を実施して膨張量を調べた。その結果を表2に示す。No.4及びNo.5の路盤材は、それぞれに占めるスラグCの比率が20質量%となるように、スラグA及びスラグBにスラグCを混合したものである。
表2によれば、比較例の路盤材はエトリンガイトの生成によると考えられる大きな膨張を生じているのに対し、本発明例の路盤材は、スラグA〜Cを単味で用いた路盤材と同様の低膨張性を示している。
Slag C (steel slag, S content 0.02% by mass) and slag D (blast furnace granulated slag, S content 0.8% by mass) were used as granular materials to be mixed with the blast furnace slow-cooled slag.
The manufactured roadbed material was subjected to a water immersion expansion test in accordance with Appendix 2 of JIS A5015. However, for the temperature and measurement time, a one-year test was conducted at 30 ° C. to examine the amount of expansion. The results are shown in Table 2. The roadbed materials of No. 4 and No. 5 are obtained by mixing slag C with slag A and slag B so that the ratio of slag C occupying each is 20 mass%.
According to Table 2, the roadbed material of the comparative example has a large expansion considered to be due to the formation of ettringite, whereas the roadbed material of the present invention example is a roadbed material using slags A to C as a simple substance. The same low expansibility is shown.
・実施例3
本実施例(発明例)で使用した高炉徐冷スラグは、インパクトクラッシャーにより粉砕した後、粒径25mm以下に粒度調整し、これを3ヶ月間大気エージングし、このエージング後の高炉徐冷スラグを篩目が2mmの篩にかけ(粒径0.075mm以下の細粒分を除去)、粒径2mm超、25mm以下の粒度とした。
この高炉徐冷スラグの成分組成は表1と同様であり、SO4溶出量は80mg/L、Al溶出量は1mg/L未満(いずれもJIS K0058−1で規定する溶出試験方法に基づく測定値)であった。また、粒径0.075mm以下の細粒分の比率は0.8質量%であった。
この高炉徐冷スラグに、粒状物として表1のスラグC(製鋼スラグ)を混合して、スラグCを30質量%含有する路盤材とした。この路盤材中の粒径0.075mm以下の細粒分の比率は3.6質量%であった。この路盤材を、実施例2と同様の方法で水浸膨張試験に供し、膨張量を調べた。その結果、膨張量は実施例2の発明例と同様、0.5%未満であった。
Example 3
The blast furnace slow-cooled slag used in this example (invention example) was pulverized by an impact crusher, adjusted to a particle size of 25 mm or less, and subjected to air aging for 3 months. The sieve mesh was passed through a 2 mm sieve (removed fine particles having a particle size of 0.075 mm or less) to obtain a particle size of more than 2 mm and a particle size of 25 mm or less.
The component composition of this blast furnace annealed slag is the same as in Table 1. The SO 4 elution amount is 80 mg / L, and the Al elution amount is less than 1 mg / L (both measured values based on the elution test method specified in JIS K0058-1). )Met. The ratio of fine particles having a particle size of 0.075 mm or less was 0.8% by mass.
The blast furnace slow-cooled slag was mixed with slag C (steel slag) shown in Table 1 as a granular material to obtain a roadbed material containing 30% by mass of slag C. The ratio of fine particles having a particle size of 0.075 mm or less in this roadbed material was 3.6% by mass. This roadbed material was subjected to a water immersion expansion test in the same manner as in Example 2 to examine the amount of expansion. As a result, the amount of expansion was less than 0.5%, similar to the inventive example of Example 2.
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JP2017166311A (en) * | 2016-03-09 | 2017-09-21 | 新日鐵住金株式会社 | Estimation method of allowable generation quantity of ettringite and determination method of allowable content of sulfur |
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JP2011001233A (en) * | 2009-06-19 | 2011-01-06 | Nippon Steel Corp | Non-expansive roadbed material |
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JP2016130187A (en) * | 2015-01-13 | 2016-07-21 | 新日鐵住金株式会社 | Blast furnace slow cooling slag roadbed material, method for manufacturing blast furnace slow cooling slag roadbed material, and method for constructing blast furnace slow cooling slag roadbed material |
JP2017166311A (en) * | 2016-03-09 | 2017-09-21 | 新日鐵住金株式会社 | Estimation method of allowable generation quantity of ettringite and determination method of allowable content of sulfur |
JP2017191089A (en) * | 2016-04-12 | 2017-10-19 | Jfeスチール株式会社 | Method for evaluating corrosive atmosphere of metal iron in iron-containing oxide, and method for producing granular materials |
JP2018024568A (en) * | 2016-07-29 | 2018-02-15 | Jfeスチール株式会社 | Manufacturing method of steel making slag roadbed material |
JP2018124276A (en) * | 2017-02-02 | 2018-08-09 | Jfeスチール株式会社 | Method for measuring expansion rate of iron-containing oxide and method for producing granular material |
JP2019137583A (en) * | 2018-02-10 | 2019-08-22 | Jfeスチール株式会社 | Method for manufacturing steelmaking slag roadbed material |
JP2019137584A (en) * | 2018-02-10 | 2019-08-22 | Jfeスチール株式会社 | Method for manufacturing steelmaking slag roadbed material |
JP2019172557A (en) * | 2018-03-28 | 2019-10-10 | 株式会社神戸製鋼所 | Production method of subbase material for road |
JP7019903B2 (en) | 2018-03-28 | 2022-02-16 | 株式会社神戸製鋼所 | Manufacturing method of roadbed material |
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