JPH03218952A - Method for producing granulated slag powder - Google Patents
Method for producing granulated slag powderInfo
- Publication number
- JPH03218952A JPH03218952A JP2011677A JP1167790A JPH03218952A JP H03218952 A JPH03218952 A JP H03218952A JP 2011677 A JP2011677 A JP 2011677A JP 1167790 A JP1167790 A JP 1167790A JP H03218952 A JPH03218952 A JP H03218952A
- Authority
- JP
- Japan
- Prior art keywords
- granulated slag
- weight
- drying
- slag powder
- roller mill
- 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.)
- Pending
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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ローラーミルを用いて水砕スラグ粉を製造す
る方法に係り、詳しくは、少ない電力消費量で水硬性の
大きい水砕スラグ粉を製造する方法に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for producing granulated slag powder using a roller mill, and more specifically, it relates to a method for producing granulated slag powder with low power consumption and high hydraulic hardness. Relating to a method of manufacturing.
水砕スラグ粉は、高炉で銑鉄を製造する際に副生ずる高
炉スラグを水で急冷破砕して得られる水砕スラグを粉砕
したものであり、高炉セメントの混合材等、水硬性材料
として広く用いられている。Granulated slag powder is obtained by pulverizing blast furnace slag, which is a by-product when producing pig iron in a blast furnace, by quenching and crushing it with water, and is widely used as a hydraulic material such as a mixed material for blast furnace cement. It is being
水砕スラグの粉砕にはチューブミルやローラーミルが用
いられているが、電力消費量の点及び乾燥と粉砕とを同
時に行える点でローラーミルの方が優れており、近年そ
の開発が広くなされている(特開昭62−216, 6
49号公報、特開昭63−166, 444号公報)。Tube mills and roller mills are used to grind granulated slag, but roller mills are superior in terms of power consumption and the ability to dry and grind at the same time, and have been widely developed in recent years. (Unexamined Japanese Patent Publication No. 62-216, 6
49, JP-A-63-166, 444).
ところが、本発明者らがローラーミルで粉砕゛した水砕
スラグ粉とチューブミルで粉砕した水砕スラグ粉との水
硬性について検討したところ、同じ成分組成の水砕スラ
グを原料として用い、同程度のブレーン比表面積に粉砕
した場合、ローラーミルで粉砕した水砕スラグ粉の方が
その水硬性が小さいことが判明した。However, when the present inventors investigated the hydraulic properties of granulated slag powder crushed with a roller mill and granulated slag powder crushed with a tube mill, they found that using granulated slag with the same component composition as raw materials, the hydraulic properties were the same. It was found that when ground to a Blaine specific surface area of
そこで、本発明者らは、このような問題を解決するため
鋭意研究を行った結果、ローラーミルで水砕スラグ粉を
製造する場合、原料として用いる水砕スラグの水分含有
量が、粉砕時の電力消費量及び水砕スラグ粉の水硬性に
密接に関連することを見出し、本発明を完成した。Therefore, the present inventors conducted intensive research to solve such problems and found that when producing granulated slag powder using a roller mill, the water content of the granulated slag used as a raw material during pulverization is The present invention was completed based on the discovery that power consumption is closely related to the hydraulic properties of granulated slag powder.
本発明の目的は、少ない電力消費量で水硬性の大きい水
砕スラク粉を製造する方法を提供することにある。An object of the present invention is to provide a method for producing granulated slurry powder with high hydraulic hardness with low power consumption.
すなわち、本発明は、水砕スラグを水分含有量10重量
%以下に予備乾燥した後に乾燥機能を有するローラーミ
ルを用いて粉砕及び乾燥することを特徴とする水砕スラ
グ粉の製造方法である。また、本発明は、水砕スラグを
水分含有量10重量%以下に予備乾燥した後にトリエタ
ノールアミン、ジエタノールアミン又はジエチレングリ
コールを添加して乾燥機能を有するローラーミルを用い
て粉砕及び乾燥することを特徴とする水砕スラグ粉の製
造方法である。That is, the present invention is a method for producing granulated slag powder, which is characterized in that granulated slag is pre-dried to a water content of 10% by weight or less, and then pulverized and dried using a roller mill with a drying function. Furthermore, the present invention is characterized in that after pre-drying the granulated slag to a water content of 10% by weight or less, triethanolamine, diethanolamine or diethylene glycol is added, and the granulated slag is pulverized and dried using a roller mill having a drying function. This is a method for producing granulated slag powder.
以下、本発明を詳細に説明する。The present invention will be explained in detail below.
本発明で用いる水砕スラグは、高炉で銑鉄を製造する際
に副生ずる溶融状態の高炉スラグを水で急冷破砕したも
のであり、酸化カルシウム、二酸化けい素、酸化アルミ
ニウム、酸化マグネシウム等の成分を含有する。このも
のは、水砕化されたのち、脱水され、屋外に積み上げら
れて、保存され、順次使用される。従って、使用時には
10%を超える水分を含んでいる。The granulated slag used in the present invention is made by quenching and crushing molten blast furnace slag, which is a by-product when producing pig iron in a blast furnace, with water, and contains components such as calcium oxide, silicon dioxide, aluminum oxide, and magnesium oxide. contains. This material is pulverized, dehydrated, piled up outdoors, stored, and used one after another. Therefore, when used, it contains more than 10% water.
本発明では、水砕スラグを水分含有量10重量%以下好
ましくは5〜10重量%に予備乾燥した後に乾燥機能を
有するローラーミルを用いて粉砕及び乾燥する。予備乾
燥した水砕スラグの水分含有量が多いと、得られる水砕
スラグ粉の水硬性が低下し、少な過ぎると粉砕時の電力
消費量が大きくなる傾向がある。また、予備乾燥した水
砕スラグを粉砕する際にトリエタノールアミン、ジエタ
ノールアミン又はジエチレングリコールを添加すると、
粉砕時の電力消費量か小さくなるとともに、得られる水
砕スラグ粉の水硬性が向上する。なお、トリエタノール
アミン、ジエタノールアミン又はジエチレングリコール
を添加して粉砕する場合は水砕スラグを水分含有量2〜
IQ重量%に予備乾燥するのが好ましい。In the present invention, the granulated slag is predried to a moisture content of 10% by weight or less, preferably 5 to 10% by weight, and then pulverized and dried using a roller mill having a drying function. If the moisture content of the pre-dried granulated slag is high, the hydraulic properties of the obtained granulated slag powder will decrease, and if it is too low, the power consumption during pulverization will tend to increase. Also, if triethanolamine, diethanolamine or diethylene glycol is added when crushing pre-dried granulated slag,
The power consumption during pulverization is reduced, and the hydraulic properties of the resulting granulated slag powder are improved. In addition, when grinding with the addition of triethanolamine, diethanolamine or diethylene glycol, the water content of the granulated slag is 2 to 2.
Pre-drying to IQ weight % is preferred.
水砕スラク′の乾燥は、ラピッドドライヤー ロータリ
ードライヤー等、通常の乾燥機により可能である。Drying of the granulated slurk' can be done using a normal dryer such as a rapid dryer or rotary dryer.
予備乾燥した水砕スラクの粉砕に用いるローラーミルは
、竪型遠心力式ローラーミル、竪型ばね式ローラーミル
等、機内に空気分級器が併設され、ミル内に温風や空気
を吹き込みながら分級、粉砕、乾燥する方式のものであ
り、前記、特開昭63−166,444号公報や特開昭
62−2t6, 649号公報に記載されたものが使用
できる。通常、水分含有量が大きい原料を粉砕する際に
は、ミル内に熱風を吹き込むことにより、粉砕と同時に
乾燥を行うことができる。Roller mills used to grind pre-dried granulated slurry include vertical centrifugal force roller mills and vertical spring roller mills, which are equipped with an air classifier inside the machine, and classify while blowing warm air or air into the mill. , pulverization, and drying methods, and those described in JP-A-63-166,444 and JP-A-62-2T6,649 can be used. Normally, when grinding raw materials with a high moisture content, drying can be performed simultaneously with the grinding by blowing hot air into the mill.
本発明においては、予備乾燥した水砕スラグを粉砕する
ので、予備乾燥の程度により、温度70℃以下の冷風を
吹き込みながら粉砕することもできるし、熱風を吹き込
みながら粉砕することもできる。In the present invention, pre-dried granulated slag is pulverized, so depending on the degree of pre-drying, it can be pulverized while blowing cold air at a temperature of 70°C or less, or it can be pulverized while blowing hot air.
本発明で得られる水砕スラグ粉には、強熱減量が小さく
水に分散した液のpHが高いという特徴がある。通常、
700℃での強熱減量が0.5重量%以下好ましくは0
.3重量%以下である。また、蒸留水100重量部に対
して10重量部分散させた液のpHが1)以上である。The granulated slag powder obtained by the present invention has a characteristic that the loss on ignition is small and the pH of the liquid dispersed in water is high. usually,
Loss on ignition at 700°C is 0.5% by weight or less, preferably 0
.. It is 3% by weight or less. Further, the pH of a liquid obtained by dispersing 10 parts by weight in 100 parts by weight of distilled water is 1) or higher.
この強熱減量及びpI−{は、水砕スラグ中の水分と粉
砕雰囲気中の炭酸ガスとに由来する炭酸カルシウム分と
密接に関係するものであり、強熱減量が太き<pHが低
い水砕スラグ粉は水硬性が小さい。This loss on ignition and pI-{ are closely related to the calcium carbonate content derived from water in the granulated slag and carbon dioxide in the pulverizing atmosphere. Crushed slag powder has low hydraulic properties.
本発明で得られる水砕スラグ粉は水硬性が大きく、スラ
グセメントの原料として好適である。スラグセメントと
しては、タリンカー粉及び石膏と配合して得られる高炉
セメント、アルカリ金属やアルカリ土類金属の水酸化物
や炭酸塩やけい酸塩等の硬化刺激剤を配合して得られる
スラグセメントがあり・、モルタルやコンクリートの結
合材として用いると、強度の大きい成形体を得られる。The granulated slag powder obtained by the present invention has high hydraulic properties and is suitable as a raw material for slag cement. Examples of slag cement include blast furnace cement obtained by blending with talinkar powder and gypsum, and slag cement obtained by blending hardening stimulants such as alkali metal and alkaline earth metal hydroxides, carbonates, and silicates. Yes, when used as a binding material for mortar or concrete, a molded product with high strength can be obtained.
本発明者らの知見によれば、水分含有量が10重量%を
超える水砕スラグをそのままローラーミルで粉砕する場
合、ミル内に熱風を吹き込んで乾燥しながら粉砕すると
、水砕スラグ中の水分と熱風中の炭酸ガスとが作用して
水硬性のない炭酸カルシウムの結晶が生成し、水砕スラ
グ粉の水硬性が小さくなる。しかし、水砕スラグ中の水
分含有量を予め10重量%以下まで予備乾燥してこの水
砕スラグを粉砕した場合は、熱風として炭酸ガス濃度の
高い燃焼排ガスを使用しても、水硬性の低下の程度が小
さい。According to the findings of the present inventors, when pulverizing granulated slag with a moisture content of more than 10% by weight using a roller mill, if the granulated slag is pulverized while being dried by blowing hot air into the mill, the water content in the granulated slag will be reduced. The action of this and the carbon dioxide gas in the hot air generates calcium carbonate crystals that have no hydraulic properties, reducing the hydraulic properties of the granulated slag powder. However, if the water content in the granulated slag is pre-dried to 10% by weight or less and the granulated slag is pulverized, even if combustion exhaust gas with a high carbon dioxide concentration is used as the hot air, the hydraulic properties will decrease. The degree of is small.
以下、本発明の実施例について説明する。 Examples of the present invention will be described below.
実施例1
塩基度1.85で水分含有量12重量%の水砕スラグを
、ドライヤーを用い温度1)0℃の条件で乾燥して、水
分含有量を約0重量%とじた乾燥水砕スラグを、ロッシ
ェ型ローラーミルを用いて温度約20℃の大気を吹き込
みながらブレーン比表面積が約4, 0 0 0cr
t/ g又は約6.000ci/gとなる条件で粉砕し
て本発明の水砕スラグ粉を得た。Example 1 Dry granulated slag with a basicity of 1.85 and a water content of 12% by weight was dried using a dryer at a temperature of 1) 0°C to reduce the water content to about 0% by weight. Using a Roche type roller mill, the Blaine specific surface area was reduced to approximately 4,000 cr while blowing air at a temperature of approximately 20°C.
The granulated slag powder of the present invention was obtained by pulverizing the powder under conditions of t/g or approximately 6.000 ci/g.
また、比較例として、水分含有量12重量%の水砕スラ
グを、ロッシェ型ローラーミルを用いて、二酸化炭素濃
度1%で温度130〜150℃の熱風を吹き込みながら
ブレーン比表面積か約4,000cnf/g又は約6,
000cnf/gとなる条件で粉砕して水砕スラグ粉を
得た。In addition, as a comparative example, granulated slag with a water content of 12% by weight was prepared using a Roche type roller mill, and while blowing hot air at a temperature of 130 to 150°C with a carbon dioxide concentration of 1%, the Blaine specific surface area was increased to approximately 4,000 cnf. /g or about 6,
The granulated slag powder was pulverized under the conditions of 000cnf/g to obtain granulated slag powder.
各水砕スラグ粉50重量部に対してブレーン比表面積3
, 2 0 0crl/ gのクリンカー粉47重量
部及び三水石膏3.5重量部を配合して高炉セメントB
種を製造し、JIS−R5201に準じて、得られた高
炉セメントB種のモルタル強度試験を行った。Blaine specific surface area 3 for each 50 parts by weight of granulated slag powder
, 47 parts by weight of clinker powder of 200 crl/g and 3.5 parts by weight of gypsum trihydrate were mixed to make blast furnace cement B.
A seed was produced, and a mortar strength test of the obtained blast furnace cement type B was conducted according to JIS-R5201.
各水砕スラグ粉の強熱減量及び蒸留水100重量部に対
して10重量部をスターラーで60分間攪拌して分散し
た液のpH並びに各高炉セメントB種の材令3日〜28
日のモルタル圧縮強度を示す。The loss on ignition of each granulated slag powder, the pH of the liquid obtained by stirring 10 parts by weight of each granulated slag powder with a stirrer for 60 minutes in 100 parts by weight of distilled water, and the age of each blast furnace cement B type from 3 days to 28 days.
Indicates the mortar compressive strength in days.
第
■
表
実施例2
水分含有量約15重量%の水砕スラグを、ドライヤーを
用い温度1)0℃の条件で乾燥して、水分含有量を0重
量%、4.8重量%、8.7重量%、9.5重量%又は
12.1重量%とじた乾燥水砕スラグを、ロッシェ型ロ
ーラーミルを用いて温度130〜150℃の熱風を吹き
込みながらブレーン比表面積が約9, 0 0 0c
nf/ gとなる条件で粉砕して本発明の水砕スラグ粉
を得た。Table 1 Example 2 Granulated slag with a water content of about 15% by weight was dried using a dryer at a temperature of 1) 0°C to reduce the water content to 0%, 4.8%, 8. Dry granulated slag containing 7% by weight, 9.5% by weight or 12.1% by weight is heated using a Roche type roller mill by blowing hot air at a temperature of 130 to 150°C until the Blaine specific surface area is approximately 9,000c.
The granulated slag powder of the present invention was obtained by pulverization under the conditions of nf/g.
実施例lと同様にして高炉セメン}B種を製造し、モル
タル強度試験を行った。A type B blast furnace cement was produced in the same manner as in Example 1, and a mortar strength test was conducted.
第2表に、予備乾燥した水砕スラグ(乾燥水砕スラグ)
の水分含有量、水砕スラグ粉の強熱減量及び蒸留水10
0重量部に対して10重量部をスターラーで60分間攪
拌して分散した液のpH並びに各高炉セメントB種の材
令3日及び7日のモルタル圧縮強度を示す。Table 2 shows pre-dried granulated slag (dried granulated slag).
Moisture content, ignition loss of granulated slag powder and distilled water 10
The pH of the liquid obtained by stirring and dispersing 10 parts by weight of 0 parts by weight with a stirrer for 60 minutes and the mortar compressive strength at 3 and 7 days of age for each blast furnace cement type B are shown.
第
2
表
実施例3
水分含有量12重量%の水砕スラクを、ドライヤーを用
い温度1)0°Cの条件で乾燥して、水分含有量を約9
重量%とした乾燥水砕スラクを、ロッシエ型ローラーミ
ルを用い、粉砕助剤としてトリエタノールアミンを用い
て温度130〜150℃の大気を吹き込みながら、ロー
ラー加圧力4.7t/ローラー、フィード量70kg/
時、テーブル回転数60回/分、セパレータ一回転数1
,250回/分、風量1)m/分の条件で粉砕して水砕
スラグ粉を得た。Table 2 Example 3 Granulated slurry with a moisture content of 12% by weight was dried using a dryer at a temperature of 1) 0°C to reduce the moisture content to approximately 9%.
Dry granulated slurry made into % by weight was processed using a Rossier-type roller mill, using triethanolamine as a grinding aid and blowing air at a temperature of 130 to 150°C, roller pressing force 4.7 t/roller, feed amount 70 kg. /
time, table rotation speed 60 times/min, separator rotation speed 1
, 250 times/min, and an air flow rate of 1) m/min to obtain granulated slag powder.
実施例lと同様にして高炉セメントB種を製造し、モル
タル強度試験を行った。Blast furnace cement type B was produced in the same manner as in Example 1, and a mortar strength test was conducted.
予備乾燥した水砕スラグl00重量部に対するトリエタ
ノールアミン(T E A)の使用量、各水砕スラグ粉
のブレーン比表面積、強熱減量及び蒸留水100重量部
に対して10重量部をスターラーで60分間攪拌して分
散した液のpH並びに各高炉セメントB種のモルタル圧
縮強度を第3表に示す。The amount of triethanolamine (TEA) used per 100 parts by weight of pre-dried granulated slag, the Blaine specific surface area of each granulated slag powder, the loss on ignition, and 10 parts by weight per 100 parts by weight of distilled water using a stirrer. Table 3 shows the pH of the dispersed liquid after stirring for 60 minutes and the mortar compressive strength of each type B blast furnace cement.
この結果より、粉砕助剤としてトリエタノールアミンを
添加して粉砕した水砕スラグ粉は、ブレーン比表面積が
小さくても、粉砕助剤を用いずに製造した水砕スラグ粉
と同等の水硬性を有することが判る。These results show that granulated slag powder produced with triethanolamine added as a grinding aid has the same hydraulic hardness as granulated slag powder produced without using a grinding aid, even though the Blaine specific surface area is small. It turns out that it has.
第
3
表
〔発明の効果〕
本発明によれば、ローラーミルを用い、少ない電力消費
堡で水硬性の大きい水砕スラグ粉を製造できる。Table 3 [Effects of the Invention] According to the present invention, granulated slag powder with high hydraulic hardness can be produced using a roller mill with less power consumption.
Claims (3)
燥した後に乾燥機能を有するローラーミルを用いて粉砕
及び乾燥することを特徴とする水砕スラグ粉の製造方法
。(1) A method for producing granulated slag powder, which comprises pre-drying granulated slag to a water content of 10% by weight or less, and then pulverizing and drying it using a roller mill with a drying function.
燥した後に乾燥機能を有するローラーミルを用いて粉砕
及び乾燥することを特徴とする水砕スラグ粉の製造方法
。(2) A method for producing granulated slag powder, which comprises pre-drying granulated slag to a moisture content of 5 to 10% by weight, and then pulverizing and drying it using a roller mill with a drying function.
燥した後にトリエタノールアミン、ジエタノールアミン
又はジエチレングリコールを添加して乾燥機能を有する
ローラーミルを用いて粉砕及び乾燥することを特徴とす
る水砕スラグ粉の製造方法。(3) Granulated slag characterized by pre-drying the granulated slag to a moisture content of 10% by weight or less, adding triethanolamine, diethanolamine or diethylene glycol, and pulverizing and drying using a roller mill with a drying function. Method for producing slag powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011677A JPH03218952A (en) | 1990-01-23 | 1990-01-23 | Method for producing granulated slag powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011677A JPH03218952A (en) | 1990-01-23 | 1990-01-23 | Method for producing granulated slag powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03218952A true JPH03218952A (en) | 1991-09-26 |
Family
ID=11784629
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2011677A Pending JPH03218952A (en) | 1990-01-23 | 1990-01-23 | Method for producing granulated slag powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03218952A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6093550A (en) * | 1983-09-29 | 1985-05-25 | シーメンス、アクチエンゲゼルシヤフト | Multiplication mechanism and operation thereof |
| JP2015147711A (en) * | 2014-02-07 | 2015-08-20 | 株式会社日向製錬所 | Slag manufacturing method, slag manufacturing system, and slag |
-
1990
- 1990-01-23 JP JP2011677A patent/JPH03218952A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6093550A (en) * | 1983-09-29 | 1985-05-25 | シーメンス、アクチエンゲゼルシヤフト | Multiplication mechanism and operation thereof |
| JP2015147711A (en) * | 2014-02-07 | 2015-08-20 | 株式会社日向製錬所 | Slag manufacturing method, slag manufacturing system, and slag |
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