[go: up one dir, main page]

KR940010114B1 - Method for the preparation iron oxide microparticles - Google Patents

Method for the preparation iron oxide microparticles Download PDF

Info

Publication number
KR940010114B1
KR940010114B1 KR1019910022606A KR910022606A KR940010114B1 KR 940010114 B1 KR940010114 B1 KR 940010114B1 KR 1019910022606 A KR1019910022606 A KR 1019910022606A KR 910022606 A KR910022606 A KR 910022606A KR 940010114 B1 KR940010114 B1 KR 940010114B1
Authority
KR
South Korea
Prior art keywords
waste
iron oxide
steel
generated during
mixing
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 - Lifetime
Application number
KR1019910022606A
Other languages
Korean (ko)
Other versions
KR930012588A (en
Inventor
김영삼
Original Assignee
김영삼
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 김영삼 filed Critical 김영삼
Priority to KR1019910022606A priority Critical patent/KR940010114B1/en
Publication of KR930012588A publication Critical patent/KR930012588A/en
Application granted granted Critical
Publication of KR940010114B1 publication Critical patent/KR940010114B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Processing Of Solid Wastes (AREA)
  • Compounds Of Iron (AREA)

Abstract

내용 없음.No content.

Description

내열성 흑갈색 합성산화철 미립자 제조방법Heat-resistant dark brown synthetic iron oxide fine particle manufacturing method

본 발명은 강의 산세 폐액과 크롬 도금 폐기스러지를 합성하여 내열성 흑갈색 합성산화철 미립자를 제조하는 방법에 관한 것이다. 제강업계에서는 제품의 물성을 향상시킬 목적으로 강을 가공하기 전에 강제표면의 산화철을 제거하여야 하는 바 이에는 산세 처리방식이 널리 이용하고 있으며, 여기에서 발생하는 산세폐액은 다음 방정식으로 생성되어 식수, 지하수 또는 해수등을 오염시키는 원인이 되고 있다.The present invention relates to a method for producing heat-resistant dark brown synthetic iron oxide fine particles by synthesizing pickling waste liquid and chromium plating waste of steel. In the steel industry, it is necessary to remove iron oxide from the steel surface before machining steel for the purpose of improving the properties of the product. The pickling treatment method is widely used. It causes pollution of groundwater or seawater.

Fe-산화물+…………………………………(1)Fe-oxide + … … … … … … … … … … … … … (One)

Fe-산화물+…………………………………(2)Fe-oxide + … … … … … … … … … … … … … (2)

강의 산세 처리시 주로(1)식과 같이 반응하며 극히 소량이 (2)식과 같이 반응하는데 보통 8-12%철을 용해한 폐액이 발생한다. 더욱이 이때 반응이 정 방향으로 촉진시켜 산세속도를 향상시키기 위하여 과잉의 산이 요구되므로 보통의 경우 과잉의 산이 8-10% 잔존하여 폐액이 발생한다. 한편 강재의 수명 연장을 위하여 강재표면에 크롬도금을 실시하는 업계에서는 6가크롬을 산성용액중에 사용한다. 그러나 도금이 진행되는 동안 크롬 도금액중에 피도금체 성분 Fe등이 용해 혼입되기 쉬우며 그 혼입량이 일정치 이상이 되면 도금의 성능은 곤란하게 된다.During the pickling process of steel, it reacts mainly in the formula (1) and very small amount reacts in the formula (2). Moreover, since the acid is required in order to accelerate the reaction in the forward direction and improve the pickling rate, in general, 8 to 10% of the excess acid remains and waste liquid is generated. On the other hand, hexavalent chromium is used in acid solution in the industry where chromium plating is applied to steel surface to extend the life of steel. However, the plating component Fe and the like are easily dissolved and mixed in the chromium plating solution during the plating process, and the plating performance becomes difficult when the amount of the mixture is more than a predetermined value.

이러한 과정에서 6가크롬 및 피도금체 성분인 Fe등이 용해된 도금 폐액이 발생된다. 이 도금 폐액중 6가 크롬은 극도로 위험한 독극성이 있으므로 다음(3),(4),(5)식과 같이 수용액중에서 아황산 가스, 아황산 소다등과 같은 환원제로 크롬을 6가에서 3가로 환원한 다음 NaOH, Ca(OH)2등과 같은 알카리로 반응시켜 크롬을 Cr(OH)3의 크롬수산화물로 철을 Fe(OH)2로 침전 분리시켜 스러지 상태의 폐기물이 발생한다.In this process, a plating waste liquid in which hexavalent chromium and Fe, which is a component to be plated, are dissolved, is generated. Since hexavalent chromium is extremely dangerous in this plating waste, chromium was reduced from hexavalent to trivalent by reducing agents such as sulfurous acid gas and sodium sulfite in aqueous solution as shown in the following formulas (3), (4) and (5). Next, by reacting with alkali such as NaOH, Ca (OH) 2 and the like, chromium is precipitated and separated into Fe (OH) 2 with chromium hydroxide of Cr (OH) 3 to generate waste of sludge.

H2Cr2O7+3Na2SO3+3H2SO4………Cr2(SO4)3+3Na2SO4+4H2O ……(3)H 2 Cr 2 O 7 +3 Na 2 SO 3 + 3H 2 SO 4 ... … … Cr 2 (SO 4 ) 3 +3 Na 2 SO 4 + 4H 2 O... … (3)

Cr2(SO4)3+6NaOH …………………2Cr(OH)3+3Na2SO4……………(4)Cr 2 (SO 4 ) 3 +6 NaOH. … … … … … … 2Cr (OH) 3 + 3Na 2 SO 4 ... … … … … (4)

Fe(SO4)+2NaOH ……………………Fe(OH)2+Na2SO4………………(5)Fe (SO 4 ) + 2 NaOH... … … … … … … … Fe (OH) 2 + Na 2 SO 4 ... … … … … … (5)

이 폐기스러지에는 (3), (4), (5)식과 같이 Cr이 2-6%, Fe가 1-3%, 수분이 80-92%이 함유되어 발생한다. 이와 같이 주로 (1), (2), (3), (4), (5)식과 같이 생성된 강의 산세폐액과 크롬 도금 폐기 스러지는 중금속 공해의 원인이 된다.This waste is generated by containing 2-6% of Cr, 1-3% of Fe and 80-92% of water as in the formulas (3), (4) and (5). Thus, pickling liquor and chromium plating waste of steel produced as in the following formulas (1), (2), (3), (4) and (5) mainly cause heavy metal pollution.

본 발명은 위와 같은 강의 산세폐액과 크롬도금폐기스러지에 의한 중금속 공해를 방지하고 이들 폐기물들을 합성 가공하여 부가가치가 높은 내열 흑갈색의 합성산화철 미립자를 제조하는 방법에 관한 것이다. 강의 산세폐액에는 주로 2가 Fe 이온과 극히 일부의 3가 Fe 이온으로 구성되어 있으며 크롬도금 폐기스러지에는 주로 Cr(OH)3와 일부의 Fe(OH)2로 구성되어 있다. 이 두 폐기물을 혼합함에 있어 Cr/Fe 성분비를 중량비로 12-25%이 되도록 혼합교반한 후 KOH, NaOH 및 Ca(OH)2, NH4OH등의 알카리(OH-) 용액을 첨가하여 pH 7-8로 조절하여 위 두 폐기물중 중금속 성분을 침전분리 한다. 침전물을 대기중에서 20-90℃의 낮은 온도로 가열, 연소 및 건조를 행함으로서 극미립의 내열성 흑갈색의 합성산화철 미립자를 얻는다. 이상과 같이 얻어진 미립자는 1,000℃까지 흑갈색이 변색되지 않는 내열성을 갖으며 흑갈색의 파장 680-700㎚에서 11.0-12.5%의 반사율을 갖는다. 그 입도는 0.08-0.30㎛의 범위를 갖는다.The present invention relates to a method for producing heavy added heat-resistant dark brown synthetic iron oxide fine particles by preventing heavy metal pollution caused by pickling waste liquid and chromium plating waste of steel as described above and by synthetically processing these wastes. The pickling liquor of steel consists mainly of divalent Fe ions and very few trivalent Fe ions, while the chromium plating waste consists mainly of Cr (OH) 3 and some Fe (OH) 2 . After being stirred mixture so that the two waste as it mixed with 12-25% of the Cr / Fe ratio by weight component ratio KOH, NaOH and Ca (OH) 2, NH 4 OH , such as alkali (OH -) in a pH 7 by addition of a solution Set to -8 to sediment and separate heavy metals from the two wastes. The precipitate is heated, burned, and dried in the air at a low temperature of 20-90 ° C. to obtain ultrafine heat resistant dark brown synthetic iron oxide fine particles. The microparticles | fine-particles obtained as mentioned above have heat resistance which does not discolor black-brown to 1,000 degreeC, and has the reflectance of 11.0-12.5% at the wavelength of 680-700 nm of black-brown. The particle size is in the range of 0.08-0.30 µm.

여기서 두 폐기물을 혼합할 때 Cr/Fe비가 12% 이하는 최종침전물의 갈색이 쇄퇴하여 적색이 되기 쉽고 25% 이상은 갈색이 쇄퇴하여 녹색이 되기 쉽다. 그리고 두 폐기물 혼합 후 pH 7 이하에서는 Fe,Cr이 용해, pH 8 이상에서는 Cr이 용해하기 쉬워 수질 오염의 공해문제를 다시 발생할 수 있다.When mixing the two wastes, brown of the final precipitate having a Cr / Fe ratio of 12% or less decays and becomes red, and 25% or more of brown decays and green. After mixing the two wastes, Fe and Cr are dissolved at a pH below 7 and Cr is easily dissolved at a pH above 8, which may cause pollution problems of water pollution.

본 발명은 강의 산세폐액과 크롬도금폐기 스러지를 혼합가공하여 부가가치가 높은 내열성 흑갈색의 합성 산화철 미립자 소재로 제조함으로서 폐기물 발생기업의 폐기물 처리를 강화할 수 있을 뿐만 아니라 외국으로부터 수입에 의존하고 있는 내열성 흑갈색 산화철 미립자를 국산화함으로서 외화 절감효과도 얻을 수 있을 뿐만아니라 날로 심각하게 부상하고 있는 국내의 환경 보전의 문제중 중금속 오염의 공해문제를 근본적으로 해결할 수 있는 매우 유용한 발명인 것이다.The present invention is made of a high value-added heat-resistant dark brown synthetic iron oxide fine particles by mixing and processing steel pickling waste liquid and chromium-plated waste sludge, which not only enhances waste treatment of waste generating companies but also relies on imports from foreign countries. Localization of the fine particles not only can reduce foreign currency, but it is also a very useful invention that can fundamentally solve the pollution problem of heavy metal pollution among the problems of environmental preservation in Korea.

[실시예]EXAMPLE

강의 산세폐액과 크롬도금 폐기 스러지를 혼합함에 있어서 Cr/Fe의 혼합비를 중량비로 18% 되도록 혼합 교반시킨 후 KOH, NaOH, 및 Ca(OH)2, NH4OH등의 알카리(OH-) 용액을 첨가하여 pH 7로 조절하여 이들 폐기물중 중금속 성분을 침전 분리한다. 침전물을 200℃에서 대기중 가열 연소하여 내열성 흑갈색의 합성 산화철 미립자를 얻는다.In mixing the pickling liquid of the steel and the chromium plating waste sludge, the mixing ratio of Cr / Fe is mixed to 18% by weight, followed by stirring with alkaline (OH ) solutions such as KOH, NaOH, Ca (OH) 2 , and NH 4 OH. By adding to pH 7 to precipitate and separate heavy metals from these wastes. The precipitate is heated and burned in air at 200 ° C. to obtain heat-resistant dark brown synthetic iron oxide fine particles.

이 미립자는 1,000℃까지 흑갈색이 변색되지 않는 내열성을 갖으며 흑갈색의 파장 700㎚에서 11.0-12.5%의 반사율을 갖는다.These fine particles have heat resistance that black brown does not discolor until 1,000 ° C., and has a reflectance of 11.0-12.5% at a wavelength of 700 nm of black brown.

그 입도는 0.08-0.30㎛의 미립자가 얻어진다. 한편 이때 생성된 상등액중의 잔유 중금속 성분은 표1에 표시한 바와 같이 정화되었으며 그외의 금속성분은 검출되지 않았다. 이 결과는 표1의 밑에 표시한 현행 환경보전상의 허용치 보다 훨씬 낮은 값으로 우수하게 수질을 정화할 수 있다. 따라서 본 방법에 의해 생성되는 방류수는 환경 보전에 문제점이 없다.Particle size of 0.08-0.30 µm is obtained. Meanwhile, the residual heavy metal component in the supernatant produced was purified as shown in Table 1, and no other metal components were detected. This result is excellent in purifying water quality to a value much lower than the current environmental conservation allowances indicated in Table 1 below. Therefore, the effluent produced by the present method has no problem of environmental conservation.

[표 1] 상등액중의 잔류 중금속 함량(ppm)Table 1 Residual Heavy Metal Content in Supernatant (ppm)

수질환경보전법상의 허용치(환경관련 벌령집 제40조, 방류수 수질기준, 1995년 12월 31일까지 허용)Permissible value under the Water Quality Preservation Act

Claims (1)

강의 가공시 발생되는 산세폐액과 크롬도금시 발생되는 폐기스러지를 혼합할 때 Cr/Fe의 혼합비를 중량비로 12-25%로 조절하여 교반 혼합하고 여기에 KOH, NaOH 및 Ca(OH)2, NH4OH등의 알카리(OH-) 용액을 첨가하여 PH 7-8로 조절하여 중금속 성분을 침전 분리시킨 다음 그 침전물을 대기중에서 20-90℃의 낮은 온도로 가열, 연소 및 건조하므로서 극미립의 내열성, 흑갈색, 파장 700㎚에서 11.0-12.5%의 반사율을 갖는 1,000℃에서도 변색 되지 않는 입도 0.08-0.30㎛의 내열성 흑갈색의 합성산화철 미립자를 제조하는 방법.When mixing pickling waste liquid generated during processing of steel and waste waste generated during chromium plating, the mixing ratio of Cr / Fe is adjusted to 12-25% by weight ratio and stirred and mixed, followed by KOH, NaOH and Ca (OH) 2 , NH 4 OH, etc. of alkali (OH -) solution was added to adjust to PH 7-8 by separating the precipitated heavy metal components and then to the precipitate in air heated to a temperature of 20-90 ℃, burning and drying of the polar fine heat resistance hameuroseo And black brown, a method for producing heat-resistant dark brown synthetic iron oxide fine particles having a particle size of 0.08-0.30 μm that does not discolor even at 1,000 ° C. having a reflectance of 11.0-12.5% at a wavelength of 700 nm.
KR1019910022606A 1991-12-11 1991-12-11 Method for the preparation iron oxide microparticles Expired - Lifetime KR940010114B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019910022606A KR940010114B1 (en) 1991-12-11 1991-12-11 Method for the preparation iron oxide microparticles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019910022606A KR940010114B1 (en) 1991-12-11 1991-12-11 Method for the preparation iron oxide microparticles

Publications (2)

Publication Number Publication Date
KR930012588A KR930012588A (en) 1993-07-20
KR940010114B1 true KR940010114B1 (en) 1994-10-21

Family

ID=19324516

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019910022606A Expired - Lifetime KR940010114B1 (en) 1991-12-11 1991-12-11 Method for the preparation iron oxide microparticles

Country Status (1)

Country Link
KR (1) KR940010114B1 (en)

Also Published As

Publication number Publication date
KR930012588A (en) 1993-07-20

Similar Documents

Publication Publication Date Title
US4260491A (en) Chrome removal waste treatment process
US5298168A (en) Ferrous dithionite process and composition for removing dissolved heavy metals from water
DE4013974C1 (en)
US4090888A (en) Production of black iron oxide pigments
FI75616C (en) FOERFARANDE FOER AOTERVINNING AV EN ALKALI- ELLER JORDALKALIMETALLOXID ELLER HYDROXID.
US5389262A (en) Process for removing heavy metals from solutions with ferrous dithionite and hydroxide
US5462670A (en) Process for removing oils and greases from aqueous solution
CN110981031A (en) Chemical nickel waste water treatment method
US5200088A (en) Removal of hexavalent chromium from waste material
KR940010114B1 (en) Method for the preparation iron oxide microparticles
CN112516507A (en) Harmless treatment method for arsenic-containing waste residue of ternary precursor
US5259975A (en) Method for stabilizing metals in wastewater sludge
JP3355281B2 (en) Treatment agent and treatment method for metal-containing acidic wastewater
CN114466824B (en) High-concentration iron-based flocculant and its production method
US2505304A (en) Lignin compounds and method for making same
CN113562877A (en) A kind of treatment method of wastewater containing EDTA-Ni
US5242874A (en) Process for whitening kaolin
JPS6135133B2 (en)
SU1794059A3 (en) Method for purifying waste water
CN111204895A (en) Surface electroplating waste liquid purification process
KR900002547B1 (en) Process for production of ferroso-ferric oxide
RU1798324C (en) Method of sewage sediments from galvanic industry treatment
SU969674A1 (en) Method for processing chromate slurries
KR100401990B1 (en) A method for preparing chromic oxide from electroplating wastewater including hexavalent chrome
KR900001490B1 (en) Method of manufacturing magnetic iron oxide for magnetic recording

Legal Events

Date Code Title Description
A201 Request for examination
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 19911211

PA0201 Request for examination

Patent event code: PA02012R01D

Patent event date: 19911211

Comment text: Request for Examination of Application

PG1501 Laying open of application
E902 Notification of reason for refusal
PE0902 Notice of grounds for rejection

Comment text: Notification of reason for refusal

Patent event date: 19940713

Patent event code: PE09021S01D

G160 Decision to publish patent application
G160 Decision to publish patent application
PG1605 Publication of application before grant of patent

Comment text: Decision on Publication of Application

Patent event code: PG16051S01I

Patent event date: 19940928

Comment text: Decision on Publication of Application

Patent event code: PG16051S01I

Patent event date: 19940924

E701 Decision to grant or registration of patent right
PE0701 Decision of registration

Patent event code: PE07011S01D

Comment text: Decision to Grant Registration

Patent event date: 19950110

NORF Unpaid initial registration fee
PC1904 Unpaid initial registration fee