JPS5973439A - Production of iron oxide from waste hydrochloric acid liquor for pickling - Google Patents

Production of iron oxide from waste hydrochloric acid liquor for pickling

Info

Publication number
JPS5973439A
JPS5973439A JP18333282A JP18333282A JPS5973439A JP S5973439 A JPS5973439 A JP S5973439A JP 18333282 A JP18333282 A JP 18333282A JP 18333282 A JP18333282 A JP 18333282A JP S5973439 A JPS5973439 A JP S5973439A
Authority
JP
Japan
Prior art keywords
waste liquor
iron oxide
hydrochloric acid
roasting
ultrafiltrate
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.)
Granted
Application number
JP18333282A
Other languages
Japanese (ja)
Other versions
JPS61289B2 (en
Inventor
Yasutaka Tejima
手島 康隆
Kiyoshi Kimura
木村 喜好
Kiyotaka Saito
清孝 斉藤
Koichi Matsumoto
紘一 松本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TETSUGEN KK
Asahi Kasei Corp
Nippon Steel Corp
Asahi Chemical Industry Co Ltd
Original Assignee
TETSUGEN KK
Nippon Steel Corp
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TETSUGEN KK, Nippon Steel Corp, Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical TETSUGEN KK
Priority to JP18333282A priority Critical patent/JPS5973439A/en
Publication of JPS5973439A publication Critical patent/JPS5973439A/en
Publication of JPS61289B2 publication Critical patent/JPS61289B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/36Regeneration of waste pickling liquors

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Iron (AREA)

Abstract

PURPOSE:To obtain economically a low-Si iron oxide which is a raw material for high- class ferrite, by roasting or crystallizing a waste liquor obtained by ultrafiltering a waste liquor after pickling a steel material with hydrochloric acid. CONSTITUTION:A waste liquor produced by acid washing of a steel material with hydrochloric acid such as steel plates, molds, rods, wire materials, etc. with the hydrochloric acid is ultrafiltered to reduce the SiO2 content to 2-10ppm. The resultant ultrafiltrate is then roasted and crystallized to give the aimed low-Si iron oxide. In a schematic drawing of an example, the above-mentioned waste liquor of acid washing charged into a waste liquor tank 1 is passed through a preliminary filtration apparatus 3 to a module 4 consisting of ultrafiltration membranes. The resultant ultrafiltrate obtd. in the filtration apparatus 3 is passed through a solenoid valve 5 to a filtrate tank 6. The concentrated solution is then returned to the waste liquor tank 1 and recirculated therethrough. The ultrafiltrate is suitably taken out of an extraction pipe 7, fed to a roasting apparatus and passed through a roasting stage to prepare iron oxide. The back washing necessary for the ultrafiltration is carried out by using a counterflow pump 8 and a check valve 9.

Description

【発明の詳細な説明】 本発明は鋼材即ち鋼板や型、棒、線材などを塩酸酸洗し
几際に発生する塩酸酸洗廃液(以下単に酸洗廃液と云う
)から酸化鉄を製造する方法に関する。
Detailed Description of the Invention The present invention is a method for producing iron oxide from the hydrochloric acid pickling waste liquid (hereinafter simply referred to as pickling waste liquid) generated during hydrochloric acid pickling of steel materials, that is, steel plates, molds, rods, wire rods, etc. Regarding.

周知の通り鋼材特に熱間圧延帯鋼については表面のスケ
ールを塩酸酸洗し清浄化する手段が広く採用されている
As is well known, for steel materials, particularly hot-rolled steel strips, a method of cleaning scale on the surface by pickling with hydrochloric acid is widely employed.

ところで、この際発生する酸洗廃液には多量のpe と
小量の非鉄金属やsio、のような金属酸化物がたとえ
ば第1表に示す如く含まれている。
Incidentally, the pickling waste liquid generated at this time contains a large amount of PE and small amounts of metal oxides such as non-ferrous metals and SIO, as shown in Table 1, for example.

第1表 従って、前記pe 分を酸化鉄として回収するため、通
常焙焼法や結晶化法が用いられ、それらの方法で得られ
た酸化鉄はフェライト原料、顔料。
Table 1 Accordingly, in order to recover the pe component as iron oxide, roasting methods and crystallization methods are usually used, and the iron oxides obtained by these methods are used as ferrite raw materials and pigments.

充填剤など多方面に利用されている。It is used in many ways, including as a filler.

ところで、前記方法で得られた酸化鉄は8j(h含有量
が前記第1表に示す通シ多いので、磁性材料として高級
な用途には適当でないと云う難点がある。
However, the iron oxide obtained by the above method has a high 8j (h content) as shown in Table 1 above, so it has the disadvantage that it is not suitable for high-grade applications as a magnetic material.

そこで1本発明者等は前記sho、含有量を減少させる
ため種々研究の結果、酸洗廃液を限外濾過することによ
って前記s i ox含有量を2〜ioppmまでに減
少させることに成功し、目的とする高級フェライト原料
である酸化鉄を得た。
Therefore, as a result of various studies to reduce the sho content, the present inventors succeeded in reducing the siox content to 2 to ioppm by ultrafiltering the pickling waste liquid, The desired high-grade ferrite raw material, iron oxide, was obtained.

周知の通り限外濾過とは溶液に圧力をかけ、高分子物、
質やコロイド状物質を半透膜によって濾過し、水および
水に含まれる低分子物質を半透膜の膜面に無数に存在す
る微細な孔を通して透過させる手段であって、前記限外
−過を実施するための濾過膜として種々のものが市販さ
れているが1本発明では無化成工業(抹)製のモジュー
ル5IP−3013(実機用)、(商品名)を用いた。
As is well known, ultrafiltration involves applying pressure to a solution to remove polymers,
A means for filtering substances and colloidal substances through a semi-permeable membrane, and allowing water and low-molecular substances contained in the water to permeate through countless fine pores existing on the membrane surface of the semi-permeable membrane. Various types of filtration membranes are commercially available for carrying out this process, and in the present invention, Module 5IP-3013 (for actual equipment) (trade name) manufactured by Mukasei Kogyo Co., Ltd. was used.

従来、酸洗廃液について限外−過が試みられ九ことが無
かったのは、限外濾過しても品質の向上が計られるよう
な成分のものではないと見られていたためであ!5. 
を九酸洗廃液、から高級なフェライト原料となる酸化鉄
は得られないとの猟識があったためである。
In the past, ultrafiltration of pickling waste liquid had never been attempted because it was not considered to be a component whose quality could be improved by ultrafiltration! 5.
This was because they had the foresight to know that iron oxide, which is a raw material for high-grade ferrite, could not be obtained from the nine pickling waste liquid.

さて、酸洗廃液を焙焼処理して酸化鉄を作る操業にたず
されっていた本発明者等は、酸洗廃液に含まれるsio
、が磁的特性を低くする主要原因の1つであることを知
ったが、何分にも廃棄物に近い性状と組成を有するもの
であるため、その特性向上に多額の設備費を投するには
難があシ、より経済的で効率の高い方法を長年にわたシ
研究した結果1本発明の方法を開発したものである。
Now, the present inventors, who were involved in an operation to produce iron oxide by roasting pickling waste liquid, discovered that sio contained in pickling waste liquid
I learned that , is one of the main causes of low magnetic properties, but since it has properties and composition that are very similar to waste, it is necessary to spend a large amount of equipment costs to improve its properties. However, as a result of many years of research into more economical and efficient methods, the method of the present invention was developed.

第1図は本発明の方法を実施するための装置の1実施例
概要図で、塩酸敗洗装置(図示していな・い)から得ら
れ几酸洗廃液は廃液タ°ンクIK装入され、ポンプ2か
ら予備濾過装置3を経て限外濾過膜からなるモジュール
4に達して、ここでV遇された液(以下F液と太う)は
電磁弁5を経てp液タンク6に入る。濃縮液は再び廃液
タンク1に戻り、再び循環する。この間酸洗廃液は適宜
補給される。FMは適宜な抽出管7から取り出され、焙
焼装置(図示していない)に送られ、焙焼工程を経て酸
化鉄が製造される。
FIG. 1 is a schematic diagram of one embodiment of the apparatus for carrying out the method of the present invention, in which the pickling waste liquid obtained from the hydrochloric acid waste washing apparatus (not shown) is charged into the waste liquid tank IK. From the pump 2, the liquid passes through the preliminary filtration device 3 and reaches the module 4 consisting of an ultrafiltration membrane, where the V-treated liquid (hereinafter referred to as the F liquid) enters the P liquid tank 6 via the electromagnetic valve 5. The concentrated liquid returns to the waste liquid tank 1 again and is circulated again. During this time, the pickling waste liquid is replenished as appropriate. FM is taken out from a suitable extraction tube 7 and sent to a roasting device (not shown), where iron oxide is produced through a roasting process.

前記焙焼装置としては、周知の7ラツシング法さて、限
外濾過には適宜な逆洗が必要であって。
The torrefaction equipment may be used by the well-known 7 lashing method. Ultrafiltration requires appropriate backwashing.

ポンプ8は逆洗用ポンプ、9は逆止弁、10〜12は圧
力針を示す。
Pump 8 is a backwash pump, 9 is a check valve, and 10 to 12 are pressure needles.

ところで、かかる限外濾過によって得られたp液を分析
すると、 sio、が2〜10 ppmとなり、他のF
e、 Mn、 Na、 K4Iには変化が見られない、
何故にSin! のみが減少するのか理由は明らかでは
ないが、数多くの実験によって5ins  含有量カニ
激減することは実証できた。
By the way, when the p liquid obtained by such ultrafiltration was analyzed, the sio was found to be 2 to 10 ppm, and other F
No changes were observed in e, Mn, Na, and K4I.
Why Sin! Although it is not clear why only the 5ins content decreases, it has been demonstrated through numerous experiments that the 5ins content decreases dramatically.

前記V液を焙焼して得られた酸化鉄はFet os力;
99%以上で、前記Slowは0.005X以下の高品
質のものであハフエライト原料として好適なものであっ
た。
The iron oxide obtained by roasting the V liquid is Fetos;
It was 99% or more, and the Slow was 0.005X or less, of high quality and suitable as a haferite raw material.

以上説明した通9、本発明は酸性廃液から高級なフェラ
イト原料である酸化鉄をよシ経済的に製造する有用な手
段を提供するものでおる。
As explained above, the present invention provides a useful means for economically producing iron oxide, which is a high-grade ferrite raw material, from acidic waste liquid.

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

第1図は本発明の方法を実施するための装置にかかる概
略ブロック線図でおる。 1・・・・・・廃液タンク、4・・・・・・そ4ニー/
l/、  6・・・・・・P液夕/り。 代理人 弁理士 秋 沢 政 光 他2名 1m
FIG. 1 is a schematic block diagram of an apparatus for carrying out the method of the present invention. 1... Waste liquid tank, 4... So4 knee/
l/, 6...P liquid evening/ri. Agent: Patent attorney Masamitsu Akizawa and 2 others 1m

Claims (1)

【特許請求の範囲】[Claims] (1)鋼材の塩酸酸洗廃液を限外濾過して得た酸洗廃液
を焙焼または結晶化処理して低Si酸化鉄を得ることを
特徴とする塩酸酸洗廃液から酸化鉄を製造する方法。
(1) Low-Si iron oxide is obtained by roasting or crystallizing the pickling waste obtained by ultrafiltration of the hydrochloric acid pickling waste of steel materials.Producing iron oxide from the hydrochloric acid pickling waste. Method.
JP18333282A 1982-10-19 1982-10-19 Production of iron oxide from waste hydrochloric acid liquor for pickling Granted JPS5973439A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18333282A JPS5973439A (en) 1982-10-19 1982-10-19 Production of iron oxide from waste hydrochloric acid liquor for pickling

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18333282A JPS5973439A (en) 1982-10-19 1982-10-19 Production of iron oxide from waste hydrochloric acid liquor for pickling

Publications (2)

Publication Number Publication Date
JPS5973439A true JPS5973439A (en) 1984-04-25
JPS61289B2 JPS61289B2 (en) 1986-01-07

Family

ID=16133859

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18333282A Granted JPS5973439A (en) 1982-10-19 1982-10-19 Production of iron oxide from waste hydrochloric acid liquor for pickling

Country Status (1)

Country Link
JP (1) JPS5973439A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3841590A1 (en) * 1987-12-10 1989-06-22 Nippon Kokan Kk METHOD FOR REFINING IRON-CONTAINING ACID SOLUTION
JPH02164725A (en) * 1988-12-17 1990-06-25 Kemiraito Kogyo Kk Production of iron oxide powder
US5032367A (en) * 1988-10-17 1991-07-16 Chemirite, Ltd. Method for producing powdered iron oxide
FR2670508A1 (en) * 1990-12-13 1992-06-19 Siderurgie Fse Inst Rech PROCESS FOR SEPARATING THE SILICON COMPOUNDS CONTAINED IN A HYDROCHLORIC STRIPPING BATH OF PARTS, PARTICULARLY STEEL SHEETS.
FR2916205A1 (en) * 2007-05-16 2008-11-21 Siemens Vai Metals Tech Sas INSTALLATION AND PROCESS FOR TREATING SILICON STEEL BAND REMOVAL SOLUTIONS
CN111373075A (en) * 2017-12-21 2020-07-03 安赛乐米塔尔公司 Method for pickling steel sheets

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4915359A (en) * 1972-03-24 1974-02-09
JPS5131236A (en) * 1974-09-11 1976-03-17 Fujitsu Ltd KADENSHIRYUSEIGYOSOCHI
JPS54120219A (en) * 1978-03-13 1979-09-18 Hitachi Metals Ltd Recovery of iron component within waste acid

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4915359A (en) * 1972-03-24 1974-02-09
JPS5131236A (en) * 1974-09-11 1976-03-17 Fujitsu Ltd KADENSHIRYUSEIGYOSOCHI
JPS54120219A (en) * 1978-03-13 1979-09-18 Hitachi Metals Ltd Recovery of iron component within waste acid

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3841590A1 (en) * 1987-12-10 1989-06-22 Nippon Kokan Kk METHOD FOR REFINING IRON-CONTAINING ACID SOLUTION
US4889697A (en) * 1987-12-10 1989-12-26 Nkk Corporation Method of refining ferrous ion-containing acid solution
US5032367A (en) * 1988-10-17 1991-07-16 Chemirite, Ltd. Method for producing powdered iron oxide
JPH02164725A (en) * 1988-12-17 1990-06-25 Kemiraito Kogyo Kk Production of iron oxide powder
FR2670508A1 (en) * 1990-12-13 1992-06-19 Siderurgie Fse Inst Rech PROCESS FOR SEPARATING THE SILICON COMPOUNDS CONTAINED IN A HYDROCHLORIC STRIPPING BATH OF PARTS, PARTICULARLY STEEL SHEETS.
US5250275A (en) * 1990-12-13 1993-10-05 Sollac Process for separating silicon compounds contained in a hydrochloric bath used for pickling
FR2916205A1 (en) * 2007-05-16 2008-11-21 Siemens Vai Metals Tech Sas INSTALLATION AND PROCESS FOR TREATING SILICON STEEL BAND REMOVAL SOLUTIONS
WO2008141716A1 (en) * 2007-05-16 2008-11-27 Siemens Vai Metals Technologies Sas Equipment and method for processing pickling solutions for silicon steel strips
CN111373075A (en) * 2017-12-21 2020-07-03 安赛乐米塔尔公司 Method for pickling steel sheets
US11879174B2 (en) 2017-12-21 2024-01-23 Arcelormittal Method for pickling steel sheets

Also Published As

Publication number Publication date
JPS61289B2 (en) 1986-01-07

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