JPS6244990Y2 - - Google Patents
Info
- Publication number
- JPS6244990Y2 JPS6244990Y2 JP4066583U JP4066583U JPS6244990Y2 JP S6244990 Y2 JPS6244990 Y2 JP S6244990Y2 JP 4066583 U JP4066583 U JP 4066583U JP 4066583 U JP4066583 U JP 4066583U JP S6244990 Y2 JPS6244990 Y2 JP S6244990Y2
- Authority
- JP
- Japan
- Prior art keywords
- scale
- hydrochloric acid
- oil
- mill scale
- 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.)
- Expired
Links
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 68
- 239000002699 waste material Substances 0.000 claims description 20
- 238000004090 dissolution Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 8
- 238000005554 pickling Methods 0.000 claims description 5
- 238000007885 magnetic separation Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 16
- 238000000034 method Methods 0.000 description 13
- 238000005406 washing Methods 0.000 description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 238000007667 floating Methods 0.000 description 8
- 238000002844 melting Methods 0.000 description 8
- 230000008018 melting Effects 0.000 description 8
- 239000007788 liquid Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229910000859 α-Fe Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004069 wastewater sedimentation Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【考案の詳細な説明】
本考案は塩酸溶液によるミルスケールの溶解装
置に関し、特に鋼材酸洗ラインの塩酸酸洗廃液
(以下廃塩酸と称す)から塩酸を回収する際に発
生する濃縮廃塩酸によつてミルスケールを溶解す
る装置を提案するものである。[Detailed description of the invention] The present invention relates to a device for dissolving mill scale using a hydrochloric acid solution, and is particularly applicable to concentrated waste hydrochloric acid generated when recovering hydrochloric acid from the hydrochloric acid pickling waste liquid (hereinafter referred to as waste hydrochloric acid) in a steel material pickling line. Therefore, we propose a device for dissolving mill scale.
一般に鋼材の酸洗ラインより発生する廃塩酸は
塩酸回収設備に送られ、ここで熱分解して塩酸が
回収される。この塩酸回収処理は、廃塩酸中の水
分を焼結炉より流入する熱風により中間ワツシヤ
ーで蒸発させて濃縮廃塩酸とし、この濃縮廃塩酸
を焙焼炉の頂部よりスプレーするものであるが、
濃縮廃塩酸の組成は全鉄分と全塩酸分より成り立
つており、全塩酸分中には遊離塩酸分を含有して
いて、この濃縮廃塩酸を焙焼処理することで、塩
酸を回収すると共に一定量の酸化第2鉄が生成さ
れる。この酸化鉄は、またフエライト用原料とし
て有効利用される。このフエライト用酸化第2鉄
を既知設備を増設することなく増産する最良の方
法は、前述の遊離塩酸分にミルスケールを溶解さ
せ、全鉄分濃度を増加させることにある。このミ
ルスケール等の溶解装置の技術は公知であるが、
この溶解過程において、ミルスケールに付着して
いる油分と軽質なスケール分が溶解液に同伴する
結果、次のような種々の問題点を生じる。 Generally, waste hydrochloric acid generated from a steel pickling line is sent to a hydrochloric acid recovery facility, where it is thermally decomposed and hydrochloric acid is recovered. In this hydrochloric acid recovery process, water in the waste hydrochloric acid is evaporated in an intermediate washer using hot air flowing from a sintering furnace to form concentrated waste hydrochloric acid, and this concentrated waste hydrochloric acid is sprayed from the top of the roasting furnace.
The composition of concentrated waste hydrochloric acid consists of total iron and total hydrochloric acid, and the total hydrochloric acid contains free hydrochloric acid.By roasting this concentrated waste hydrochloric acid, the hydrochloric acid is recovered and a constant amount is amount of ferric oxide is produced. This iron oxide is also effectively used as a raw material for ferrite. The best way to increase the production of ferric oxide for ferrite without adding any existing equipment is to dissolve mill scale in the aforementioned free hydrochloric acid to increase the total iron concentration. The technology of this melting device such as mill scale is well known, but
During this dissolution process, oil and light scale components adhering to the mill scale are entrained in the dissolving solution, resulting in various problems as described below.
(i) 充填塔・槽類内に付着ならびに浮遊し、操業
状態を悪化させる。(i) It adheres and floats inside packed towers and tanks, worsening operational conditions.
(ii) 配管内に付着ならびに沈着し、通液不良とな
る。(ii) It adheres and settles inside the piping, causing poor fluid flow.
(iii) ポンプ類の揚液を不良とする。(iii) The liquid pumped by pumps is defective.
以上のような、設備上の問題点を防止するため
には、ミルスケール中の浮遊性のある軽質スケー
ル分ならびに付着油分等を溶解装置に装入充填す
る前に除去しなければならない。従来はこの場
合、撹拌が可能な温水洗滌槽にミルスケールを装
入し、撹拌しながら加温した後、浮遊スケールな
らびに油分を分離する方法が一般に採用されてい
た。ここでは、分離した浮遊スケールおよび油分
は排水沈降処理設備を経て、浮遊スケール分は鉄
源へ、油分はスカム油として回収される。また温
水洗滌したミルスケールは、テルフアークレーン
で溶解装置へ装入充填する。 In order to prevent the above-mentioned problems with the equipment, floating light scale components and attached oil components in the mill scale must be removed before charging into the melting device. Conventionally, in this case, a method has generally been adopted in which mill scale is placed in a hot water washing tank that can be stirred, heated while being stirred, and then the floating scale and oil are separated. Here, the separated floating scale and oil pass through wastewater sedimentation treatment equipment, where the floating scale is returned to the iron source and the oil is recovered as scum oil. The mill scale that has been washed with hot water is then charged to the melting equipment using a Telfu crane.
第1図は従来ミルスケール溶解装置の1例を示
したものであつて、温水洗滌槽1にミルスケール
2を投入し、内部に洗滌水3を給水する。温水洗
滌槽内底部に配設されたヒーター4により、洗滌
水を加熱すると共に加圧空気または動力撹拌5に
よりミルスケールを撹拌すると、ミルスケール中
の軽質スケールと油分6は温水洗滌槽内表面に浮
遊する。この浮遊分は排水ポンプ7により排水処
理設備へ送つて処理する。脱油したミルスケール
はテルフアークレーン8で溶解装置9に充填し、
濃縮廃塩酸溶媒10により溶解する。 FIG. 1 shows an example of a conventional mill scale dissolving apparatus, in which mill scale 2 is placed in a warm water washing tank 1, and washing water 3 is supplied inside. When the cleaning water is heated by the heater 4 installed at the bottom of the hot water washing tank and the mill scale is stirred by pressurized air or power stirring 5, the light scale and oil content 6 in the mill scale are transferred to the inner surface of the hot water washing tank. Float. This suspended matter is sent to a wastewater treatment facility by a wastewater pump 7 for treatment. The deoiled mill scale is loaded into a melting device 9 using a Telfu crane 8.
Dissolve with concentrated waste hydrochloric acid solvent 10.
以上のように従来技術では、ミルスケールは溶
解前に清浄化するものであつて、このような温水
洗滌装置では工程も複雑であり、従つて設備投資
費ならびに操業、維持費が高くなり、また保守も
困難である。 As described above, in the conventional technology, mill scale is cleaned before it is dissolved, and the process for such hot water washing equipment is complicated, resulting in high equipment investment costs, operation and maintenance costs, and Maintenance is also difficult.
なお別のミルスケールの清浄方法としては、バ
ーナー加熱による油分焼却法もあるが、この方法
も温水洗滌方法と同様に処理経費は割高である。 Another method for cleaning mill scale is a method of incinerating oil by heating with a burner, but this method is also expensive in processing costs, as is the case with the hot water washing method.
本考案は以上に説明したような従来技術の問題
点を解消するものであつて、ミルスケールの溶解
に当つて、溶解装置に装入する以前に温水洗滌な
どの清浄処理を施すことなく、軽質スケールおよ
び油の付着したままのミルスケールを溶解装置へ
装入し、濃縮廃塩酸を連続供給して溢流する溶解
液中に軽質スケールおよび油分を遊離同伴させ、
これら浮遊スケールおよび油を容易に分離除去す
る装置を提供するものである。 The present invention solves the problems of the conventional technology as explained above, and when melting mill scale, it eliminates the need for cleaning treatment such as hot water washing before charging into the melting equipment. The mill scale with scale and oil still attached is charged into the dissolving device, and concentrated waste hydrochloric acid is continuously supplied to free and entrain the light scale and oil in the overflowing dissolving solution.
The object of the present invention is to provide a device that easily separates and removes these floating scales and oil.
本考案者はミルスケールの溶解工程において、
その合理化を図るべく徹底した検討を行なつたと
ころ、従来から実施されているミルスケールの溶
解前の温水洗滌における軽質スケールおよび油の
分離除去の効率が悪くてコスト高となつているこ
とを見出し、種々研究・試験を重ねた結果、ミル
スケールの溶解に使用される遊離塩酸を含有する
濃縮廃塩酸は90℃以上の高温であり、従来の温水
洗滌の前処理に代えて、直接濃縮廃塩酸に接触さ
せるようにすれば、理論的に云つても反応熱もプ
ラスされ高温酸洗の効果があり、実験結果からも
ミルスケールに付着している油分・軽質スケール
は容易に分離した溶解液中に同伴されることを確
認することが出来たので、このようなミルスケー
ルの溶解処理によつて油分・軽質スケールを分離
除去するようにすれば極めて有利であり、本考案
の目的が達成されることを知見した。 In the process of dissolving mill scale, the inventor of the present invention
When we conducted a thorough study to streamline this process, we discovered that the traditional method of separating and removing light scale and oil during hot water washing before dissolving mill scale was inefficient and costly. As a result of various research and tests, we found that the concentrated waste hydrochloric acid containing free hydrochloric acid used to dissolve mill scale has a high temperature of 90℃ or more, and instead of the conventional pretreatment of hot water washing, we can directly use concentrated waste hydrochloric acid. Theoretically speaking, if the mill scale is brought into contact with the mill scale, the heat of reaction will be added and high-temperature pickling will be effective, and the experimental results also show that the oil and light scale adhering to the mill scale can be easily separated into the dissolved solution. It has been confirmed that the oil and light scales are separated and removed through such mill scale dissolution treatment, which would be extremely advantageous and achieve the purpose of the present invention. I found out that.
本考案は、この知見に基づいてなされたもので
あつて、軽質スケールおよび油分が付着したまま
のミルスケールを装入充填しこれに濃縮廃塩酸を
連続供給してミルスケールを溶解する溶解装置
と、この溶解装置から排出される溶解液に同伴す
る軽質スケールおよび油分を分離除去する連続マ
グネツト分離槽と油分離槽とからなる分離装置と
で構成された、軽質スケールおよび油分が付着し
たままのミルスケールを直接連続溶解することを
特徴とするミルスケールの溶解装置である。 The present invention was developed based on this knowledge, and includes a dissolving device that charges and fills mill scale with light scale and oil still attached, and continuously supplies concentrated waste hydrochloric acid to dissolve the mill scale. , a separation device consisting of a continuous magnetic separation tank and an oil separation tank that separates and removes light scale and oil accompanying the solution discharged from the dissolution device, and a mill to which light scale and oil remain attached. This is a mill scale melting device that directly and continuously melts scale.
以下に、本考案の装置を好適実施例の図面につ
いて説明する。第2図はその溶解装置の説明図で
あつて、ミルスケールをテルフアークレーンによ
り溶解装置9に直接装入充填し、下部より濃縮廃
塩酸の溶媒10を上向きに供給し、溶解装置内の
ミルスケールを溶解しながら溶解装置から溶解液
11としてオーバーフローする。この溶解液には
ミルスケールに付着していた油分を軽質なスケー
ルが同伴している。これらの分離は、最初に連続
マグネット分離槽12で浮遊スケール分を除去す
るが、この時一部の油分もこれに付着して除去さ
れる。次に油分離槽13に流入して、溶解液表面
に浮遊する油分14を比重差で排出し、その後マ
グネツトで溶解液中に残存するスケールを除去す
る(図示なし)。 In the following, the device of the present invention will be described with reference to the drawings of preferred embodiments. FIG. 2 is an explanatory diagram of the dissolving apparatus, in which mill scale is directly charged and filled into the dissolving apparatus 9 using a Telfu crane, a solvent 10 of concentrated waste hydrochloric acid is supplied upward from the bottom, and the mill scale in the dissolving apparatus is While dissolving the scale, it overflows from the dissolving device as a dissolving solution 11. This solution contains light scale, which is the oil that had adhered to the mill scale. In these separations, floating scale is first removed in a continuous magnetic separation tank 12, but at this time, some of the oil that adheres thereto is also removed. Next, the oil flows into the oil separation tank 13, and the oil 14 floating on the surface of the solution is discharged based on the difference in specific gravity, and then the scale remaining in the solution is removed using a magnet (not shown).
なお別法として濾過方法等もあるが、この方法
は溶媒液の液性状によつては採用も可能である。
また上記実施例では、溶媒を下部より上向流で連
続供給する例であるが、上部より下向流で溶媒を
連続供給することも出来る。 There is also a filtration method as an alternative method, but this method can be adopted depending on the liquid properties of the solvent liquid.
Further, in the above embodiment, the solvent is continuously supplied from the bottom in an upward flow, but it is also possible to continuously supply the solvent in a downward flow from the top.
なお、本考案の装置で溶解処理するミルスケー
ルとは純鉄・酸化第2鉄・四三酸化鉄等の金属粉
および錆であり、溶媒とは塩酸・浮遊塩酸を含有
する塩化鉄等のスケール溶解性液である。 The mill scale that is dissolved in the device of this invention is metal powder such as pure iron, ferric oxide, and triiron tetroxide, and rust, and the solvent is scale such as hydrochloric acid and iron chloride containing suspended hydrochloric acid. It is a soluble liquid.
以上の説明で明らかなように、本考案のミルス
ケール溶解装置おいては、充填塔にはミルスケー
ル溶解の進行に応じて、必要量の軽質スケールや
油分の付着したままのミルスケールを補足充填す
ればよいのであつて、従来方式(第1図参照)の
ような温水洗滌と充填塔との間の工程の進行状態
を管理する必要はない。また原料のミルスケール
の清浄化の点でも、本考案では熱濃縮廃塩酸で行
なうものであるから極めて効率がよく、しかも溶
解装置から溢流する油分・軽質スケールを伴つた
溶解液から浮遊スケールや油分の分離は第2図か
らも理解できるように連続・自動化も可能であ
り、本考案の効果は極めて顕著なものである。 As is clear from the above explanation, in the mill scale dissolving apparatus of the present invention, the packed tower is supplemented with the necessary amount of light scale and mill scale with oil attached, as mill scale dissolution progresses. There is no need to control the progress of the process between the hot water washing machine and the packed tower as in the conventional method (see FIG. 1). In addition, in terms of cleaning mill scale, which is a raw material, the present invention uses heat-concentrated waste hydrochloric acid, which is extremely efficient, and removes floating scale from the dissolved solution containing oil and light scale that overflows from the dissolving device. As can be seen from Figure 2, oil separation can be carried out continuously and automatically, and the effects of the present invention are extremely remarkable.
第1図は従来のミルスケール溶解装置の模式
図、第2図は本考案実施例のミルスケール溶解装
置の概略図面である。
1……温水洗滌槽、2……ミルスケール、3…
…洗滌水、4……ヒーター、5……撹拌装置、6
……軽質スケールと油分、7……排水ポンプ、8
……テルフアークレーン、9……溶解装置、10
……濃縮廃塩酸、11……溶解液、12……連続
マグネツト分離槽、13……油分離槽、14……
油分、15……スケール、15′……軽質スケー
ル。
FIG. 1 is a schematic diagram of a conventional mill scale dissolving device, and FIG. 2 is a schematic diagram of a mill scale dissolving device according to an embodiment of the present invention. 1...Hot water washing tank, 2...Mill scale, 3...
...Washing water, 4...Heater, 5...Stirring device, 6
...Light scale and oil, 7...Drain pump, 8
... Telfah Crane, 9 ... Melting equipment, 10
... Concentrated waste hydrochloric acid, 11 ... Dissolved liquid, 12 ... Continuous magnetic separation tank, 13 ... Oil separation tank, 14 ...
Oil content, 15...scale, 15'...light scale.
Claims (1)
濃縮廃塩酸によるミルスケールの連続溶解装置に
おいて、軽質スケールや油分が付着したままのミ
ルスケールを装入充填し上記濃縮廃塩酸を連続供
給して該ミルスケールを溶解する溶解装置と、該
溶解装置からの排出溶解液に同伴する軽質スケー
ルおよび油分を分離除去する連続マグネツト分離
槽と油分離槽とからなる分離装置とで構成された
ミルスケール溶解装置。 In a continuous mill scale dissolution device using concentrated waste hydrochloric acid generated when hydrochloric acid is recovered from hydrochloric acid pickling waste, mill scale with light scale and oil still attached is charged and filled, and the concentrated waste hydrochloric acid is continuously supplied. A mill scale dissolution device consisting of a dissolution device for dissolving the mill scale, and a separation device consisting of a continuous magnetic separation tank and an oil separation tank for separating and removing light scale and oil accompanying the dissolved solution discharged from the dissolution device. Device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4066583U JPS59149969U (en) | 1983-03-23 | 1983-03-23 | Mill scale melting equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4066583U JPS59149969U (en) | 1983-03-23 | 1983-03-23 | Mill scale melting equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59149969U JPS59149969U (en) | 1984-10-06 |
JPS6244990Y2 true JPS6244990Y2 (en) | 1987-11-30 |
Family
ID=30171275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4066583U Granted JPS59149969U (en) | 1983-03-23 | 1983-03-23 | Mill scale melting equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59149969U (en) |
-
1983
- 1983-03-23 JP JP4066583U patent/JPS59149969U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59149969U (en) | 1984-10-06 |
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