JPH0132196B2 - - Google Patents
Info
- Publication number
- JPH0132196B2 JPH0132196B2 JP11511580A JP11511580A JPH0132196B2 JP H0132196 B2 JPH0132196 B2 JP H0132196B2 JP 11511580 A JP11511580 A JP 11511580A JP 11511580 A JP11511580 A JP 11511580A JP H0132196 B2 JPH0132196 B2 JP H0132196B2
- Authority
- JP
- Japan
- Prior art keywords
- ash
- coal ash
- converter slag
- fertilizer
- 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
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 29
- 239000002893 slag Substances 0.000 claims description 24
- 239000010883 coal ash Substances 0.000 claims description 20
- 239000003337 fertilizer Substances 0.000 claims description 15
- 229910052742 iron Inorganic materials 0.000 claims description 15
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 12
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 11
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 9
- 235000012239 silicon dioxide Nutrition 0.000 claims description 9
- 239000002956 ash Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 6
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 5
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 5
- 229910052749 magnesium Inorganic materials 0.000 claims description 5
- 239000011777 magnesium Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 238000009628 steelmaking Methods 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 239000000155 melt Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 5
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 4
- 229910052796 boron Inorganic materials 0.000 description 4
- 239000002440 industrial waste Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 239000000292 calcium oxide Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Landscapes
- Fertilizers (AREA)
Description
本発明は、ともに産業廃棄物である石炭灰と転
炉スラグとから、有用な鉄を回収するとともに、
ケイ酸、マグネシウムおよびリン酸を肥料として
有効な形態で含有するケイ酸肥料を製造する方法
に関する。
石油の需給関係の緊迫化と価格の高謄につれ
て、再び石炭が使用されるようになつて来た。し
かし、石炭は燃焼後に多量の残灰が発生し、その
量は、もちろん石炭の種類によつても異なるが、
もとの石炭の重量の15〜20%にも及ぶのがふつう
である。従つて、その廃棄をどうするかという、
別の問題が重要になりつつある。
一方、製鋼作業に伴つて生じる転炉スラグもま
た、これといつた利用の途をもたない産業廃棄物
であつて、その処分に困つている。
石炭灰中には、ケイ酸、アルミナ、酸化カルシ
ウムおよび酸化鉄のほかに、若干の未燃焼炭素お
よび微量ではあるが、ホウ素などの諸成分が含ま
れている。最近は、燃焼排ガス中のNOx分を抑
制するため、バーナー温度を低目にして操業せざ
るを得ず、未燃焼炭素分は、後に示すように数%
にも及ぶ。また、転炉スラグ中には、多量の酸化
カルシウムのほかに、ケイ酸、酸化鉄、リン酸、
酸化マグネシウムなどが含まれている。
本発明者らは、これらの廃棄物中の有用成分を
再利用することを意図し、協力して研究の結果、
石炭灰中の未燃焼炭素を利用して、灰およびスラ
グ中の酸化鉄をかなりの割合で還元して金属鉄に
できること、および全体をガラス質にすることに
より、マグネシウムおよびリン酸がク溶性の形態
で存在し、かつホウ素が適量含まれたケイ酸質物
が得られることを見出して本発明に至つた。
本発明の産業廃棄物からケイ酸肥料を製造する
方法は、石炭灰と転炉スラグとを混合して溶融
し、灰に含まれている灰素分により灰およびスラ
グ中の酸化鉄の少なくとも一部を金属鉄に還元
し、溶融物を水冷することによつて、ケイ酸、マ
グネシウムおよびリン酸を肥料として有効な形態
で含有するガラス質物を粉砕された状態で得、そ
れから金属鉄を分離回収することからなる。
石炭灰と転炉スラグとの配合割合は、それぞれ
に含まれている有用成分の割合、および得ようと
する製品の特性の関連に従つて決定する。実際上
は、処理すべき廃棄物として発生する両者の量比
が、重要な因子となるかもしれない。一般には、
重量比で8:2〜2:8、好ましくは6:4
4:6の範囲からえらぶとよく、とくにこの好
ましい量比の場合には、溶融物の粘度が低くな
り、比較的低温で溶融しタツプすることができて
有利である。
混合物の溶融は、上記のように原料の配合割合
にもよるが、一般に1300゜〜1600℃の温度におい
て行なう。このための装置としては、高温を得や
すいアーク炉が適当である。
転炉スラグは、製鋼工程が終つたところで溶融
状態で得られるから、その保有する顕熱および潜
熱を利用することが得策であつて、転炉から直
接、たは一旦とりべに受けた溶融スラグを、上記
のアーク炉に移注し、そこで若干の電力を使つて
温度を高め、石炭灰との反応を行なう態様が、本
発明にとつては実用的である。スラグと石炭灰と
の混合は、上記の移注に際して溶融スラグ流に石
炭灰を投入して流下とともに撹拌させるか、また
はアーク炉中にあらかじめ石炭灰を装入してお
き、その上から溶融スラグを注入することにより
撹拌効果を生じさせるかするとよい。
石炭灰と転炉スラグとの混合溶融により、酸化
鉄はその少なくとも50%、操業が好ましく行なわ
れた場合には60〜70%、またはそれ以上が還元さ
れ、金属鉄になる。溶融物の水冷粉砕に際して、
この鉄は粒状体となり、ガラス物質とはほぼ完全
に別々になるので、磁力選鉱等の手法により、容
易に回収できる。この回収鉄は、もちろん製鋼原
料として再利用可能である。
溶融物の水冷粉砕は、たとえば高炉スラグの水
砕において確立された技術に従つて行なえばよ
い。
金属鉄の粒子を分離したガラス質物は、水砕条
件によつても多少異なるが、川砂程度の粒子であ
つて、そのままケイ酸肥料として施用できる。周
知のとおり、ケイ酸質肥料、通称ケイカル肥料
は、重要な普通肥料の一つである。ケイカル肥料
としてみたとき、本発明によるものは、転炉スラ
グ中のCaOとSiO2との量比では後者が不足する
ところを、石炭灰からのSiO2がこの不足を補う
ので、バランスのとれたものとなる。また、転炉
スラグ中のマグネシウムやリン酸(その一部は灰
からも加わる)がク溶性の形態となつて有効化さ
れており、かつ石炭灰中のホウ素などの微量成分
が利用できる。このケイ酸肥料はまた、土壌改良
資材としても有用である。
このように、本発明は、処理に困る産業廃棄物
から有用なケイ酸肥料を製造するとともに、金属
鉄を回収して資源のより効率的な利用を実現す
る。
実施例
下記の組成をもつ(重量%)、火力発電所から
排出される石炭灰であるフライアツシユと、普通
鋼の製鋼に際して発生した転炉スラグとを、原料
として使用した。
The present invention recovers useful iron from coal ash and converter slag, both of which are industrial waste, and
The present invention relates to a method for producing a silicate fertilizer containing silicic acid, magnesium, and phosphoric acid in a form effective as a fertilizer. As the supply-demand relationship for oil becomes increasingly tense and prices rise, coal is once again being used. However, after coal burns, a large amount of residual ash is generated, and the amount varies depending on the type of coal, but
It typically weighs as much as 15-20% of the original coal weight. Therefore, what should be done about its disposal?
Another issue is becoming important. On the other hand, converter slag produced during steelmaking operations is also an industrial waste that has no other use, and it is difficult to dispose of it. In addition to silicic acid, alumina, calcium oxide, and iron oxide, coal ash contains various components such as some unburned carbon and a trace amount of boron. Recently, in order to suppress the NO
It also extends to In addition to large amounts of calcium oxide, converter slag also contains silicic acid, iron oxide, phosphoric acid,
Contains magnesium oxide. The present inventors intended to reuse useful components in these wastes, and as a result of collaborative research,
By using unburned carbon in coal ash, a considerable proportion of iron oxide in ash and slag can be reduced to metallic iron, and by making the whole glassy, magnesium and phosphoric acid are The present inventors have discovered that it is possible to obtain a silicic acid material that exists in the form of boron and contains an appropriate amount of boron, leading to the present invention. The method of producing silicate fertilizer from industrial waste according to the present invention involves mixing and melting coal ash and converter slag, and using the ash contained in the ash to absorb at least one part of the iron oxide in the ash and slag. A vitreous material containing silicic acid, magnesium and phosphoric acid in a form useful as fertilizer is obtained by reducing the fraction to metallic iron and cooling the melt with water, from which the metallic iron is separated and recovered. consists of doing. The blending ratio of coal ash and converter slag is determined in accordance with the ratio of useful components contained in each and the characteristics of the product to be obtained. In practice, the ratio of the amounts of the two generated as waste to be treated may be an important factor. In general,
It is preferable to select from the range of 8:2 to 2:8 in terms of weight ratio, preferably 6:4 to 4:6. Particularly in the case of this preferable weight ratio, the viscosity of the melt is low and the melt can be melted at a relatively low temperature. It is advantageous to be able to tap. The mixture is generally melted at a temperature of 1,300 DEG to 1,600 DEG C., although it depends on the blending ratio of the raw materials as described above. As a device for this purpose, an arc furnace is suitable because it can easily obtain high temperatures. Since converter slag is obtained in a molten state at the end of the steelmaking process, it is a good idea to utilize the sensible and latent heat it possesses. It is practical for the present invention to transfer the coal into the above-mentioned arc furnace, raise the temperature there using some electric power, and carry out the reaction with the coal ash. Mixing of slag and coal ash can be done either by adding coal ash to the molten slag flow during the above transfer and stirring it as it flows down, or by charging coal ash into the arc furnace in advance and pouring the molten slag onto it. It is recommended to create a stirring effect by injecting . The combined melting of coal ash and converter slag reduces the iron oxide to metallic iron by at least 50%, and in preferred operations, 60-70% or more. When water-cooling the molten material,
This iron becomes granular and is almost completely separated from the glass material, so it can be easily recovered by methods such as magnetic separation. Of course, this recovered iron can be reused as a raw material for steelmaking. The water-cooled pulverization of the melt may be carried out, for example, in accordance with established techniques for pulverization of blast furnace slag. The vitreous material obtained by separating metallic iron particles has particles the size of river sand and can be applied as is as a silicate fertilizer, although this varies somewhat depending on the granulation conditions. As is well known, silicic acid fertilizer, commonly known as silicic acid fertilizer, is one of the important ordinary fertilizers. When viewed as a calcic fertilizer, the one according to the present invention has a well-balanced ratio of CaO and SiO 2 in converter slag, where the latter is insufficient, but SiO 2 from coal ash makes up for this deficiency. Become something. Additionally, magnesium and phosphoric acid in the converter slag (some of which is also added from the ash) are effective in their soluble form, and trace components such as boron in the coal ash can be utilized. This silicate fertilizer is also useful as a soil improvement material. In this manner, the present invention not only produces useful silicate fertilizer from industrial waste that is difficult to process, but also recovers metallic iron to realize more efficient use of resources. Example Fly ash, which is coal ash discharged from a thermal power plant, and converter slag generated during the manufacturing of ordinary steel, having the following composition (wt%), were used as raw materials.
【表】
* 原子吸光法 〓
〓により測定
** バナドモリブデン酸法〓
上記の原料を種々の割合で混合して高周波炉を
用いて溶解し、溶融物を水中に投入して急冷し
た。
(1) 石炭灰600g、転炉スラグ175g(77:23)を
混合、1585℃で溶融した。溶融物は粘く、流動
性が低かつた。
水砕により、砂状の生成物560gを得た。
その成分および溶出分はつぎのとおりである。[Table] * Atomic absorption method 〓
Measured by 〓
** Vanadomolybdic acid method〓
The above raw materials were mixed in various proportions and melted using a high frequency furnace, and the melt was poured into water and rapidly cooled. (1) 600g of coal ash and 175g of converter slag (77:23) were mixed and melted at 1585℃. The melt was viscous and had low fluidity. By water grinding, 560 g of a sandy product was obtained. Its components and eluate are as follows.
【表】
(2) 石炭灰480g、転炉スラグ320g(6:4)を
混合、1450℃に昇温して溶融したが、溶融物は
低粘度で、1300℃でもタツピング可能であつ
た。
水砕により得られた砂状物中に球状の金属鉄
が混在していたので、磁力により選別した。
得られた生成物は、ガラス質物705g、金属
鉄32gであつた。ガラス質物の組成と溶出分と
を、下に示す。[Table] (2) 480 g of coal ash and 320 g of converter slag (6:4) were mixed and melted at a temperature of 1450°C, but the molten material had a low viscosity and could be tapped even at 1300°C. Since spherical metallic iron was found mixed in the sandy material obtained by water pulverization, it was sorted by magnetic force. The products obtained were 705 g of glassy material and 32 g of metallic iron. The composition of the glassy material and the eluted content are shown below.
【表】
(3) 石炭灰320g、転炉スラグ480g(4:6)を
混合し、1450℃まで昇温した。この場合も溶融
物は低粘度で、1300℃においても易動性であつ
た。
水砕生成物中に、かなりの量の金属鉄の粒子
が見受けられ、その量は32g、また生成ガラス
質物は670gであつた。[Table] (3) 320g of coal ash and 480g of converter slag (4:6) were mixed and heated to 1450℃. In this case as well, the melt had a low viscosity and was mobile even at 1300°C. A considerable amount of metallic iron particles was found in the granulated product, amounting to 32 g, and 670 g of glassy material produced.
【表】
(4) 石炭灰120g、転炉スラグ480g(2:8)を
混合し、溶融した。溶融物の粘度はいく分高
く、1450℃でタツピングを行なつた。
砂状のガラス質物510g、および粒状の金属
鉄42gを得た。[Table] (4) 120 g of coal ash and 480 g of converter slag (2:8) were mixed and melted. The viscosity of the melt was somewhat high and tapping was carried out at 1450°C. 510 g of sandy glassy material and 42 g of granular metallic iron were obtained.
Claims (1)
に含まれている炭素分より灰およびスラグ中の酸
化鉄の少なくとも一部を金属鉄に還元し、溶融物
を水冷することによつて、ケイ酸、マグネシウム
およびリン酸を肥料として有効な形態で含有する
ガラス質物を粉砕された状態で得、それから金属
鉄を分離回収することからなる産業廃棄物からケ
イ酸肥料を製造する方法。 2 石炭灰と転炉スラグとを、重量比で8:2〜
2:8、好ましくは6:4〜4:6の範囲内の割
合で混合して溶融する特許請求の範囲第1項のケ
イ酸肥料を製造する方法。 3 製鋼工程から溶融状態で得た転炉スラグをア
ーク炉に移注し、そこで石炭灰とともに溶融させ
る特許請求の範囲第1項のケイ酸肥料を製造する
方法。[Claims] 1. Coal ash and converter slag are mixed and melted, at least a portion of the iron oxide in the ash and slag is reduced to metallic iron from the carbon content in the ash, and the molten product is A vitreous material containing silicic acid, magnesium and phosphoric acid in a form useful as a fertilizer is obtained in a crushed state by cooling with water, from which metallic iron is separated and recovered. A method of producing fertilizer. 2 Coal ash and converter slag in a weight ratio of 8:2~
2. A method for producing a silicic acid fertilizer according to claim 1, comprising mixing and melting in a ratio of 2:8, preferably 6:4 to 4:6. 3. A method for producing a silicate fertilizer according to claim 1, which comprises transferring converter slag obtained in a molten state from the steelmaking process to an arc furnace and melting it together with coal ash there.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11511580A JPS5738388A (en) | 1980-08-20 | 1980-08-20 | Manufacture of silicate fertilizer from industrial waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11511580A JPS5738388A (en) | 1980-08-20 | 1980-08-20 | Manufacture of silicate fertilizer from industrial waste |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5738388A JPS5738388A (en) | 1982-03-03 |
JPH0132196B2 true JPH0132196B2 (en) | 1989-06-29 |
Family
ID=14654607
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11511580A Granted JPS5738388A (en) | 1980-08-20 | 1980-08-20 | Manufacture of silicate fertilizer from industrial waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5738388A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6161662U (en) * | 1984-09-25 | 1986-04-25 | ||
JPS6396784A (en) * | 1986-10-13 | 1988-04-27 | Hitachi Maxell Ltd | Disk cartridge |
JPH09270161A (en) * | 1996-01-31 | 1997-10-14 | Mitsubishi Electric Corp | Storage and recording medium cartridge |
CR20190160A (en) * | 2017-06-28 | 2019-05-16 | Nippon Steel & Sumitomo Metal Corp | Steelmaking slag for use as fertilizer starting material, method for producing steelmaking slag for use as fertilizer starting material, method for producing fertilizer, and fertilization method |
CR20190159A (en) * | 2017-06-28 | 2019-05-16 | Nippon Steel & Sumitomo Metal Corp | Steelmaking slag for use as fertilizer starting material, method for producing steelmaking slag for use as fertilizer starting material, method for producing fertilizer, and fertilization method |
-
1980
- 1980-08-20 JP JP11511580A patent/JPS5738388A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5738388A (en) | 1982-03-03 |
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