• 환경위생공학
• /
• 제16권4호
• /
• pp.62-68
• /
• 2001

The advantages of hydrogen peroxide dissolution method were no discharge of noxious matter when dissolution of iron wire which used as the center supporter, reactions occur in room temperature and easy to recover dissolved iron. This study was aimed at gathering the basic data of iron wire dissolution- recovery process and proposes the reaction condition of iron wire dissolution- recovery process rind the factors influencing those reactions. The results were as follows : 1 . Hydrogen peroxide dissolution method used hydrochloric acid as the catalyst. 1. In the dissolution of iron wire(1.668 g), the condition of reaction was E1702(30 ml), HCI(20 ml) and $H_2O$(200 ml) ; time of the reaction was 18 min. P.W.(Piece weight) was 7.75 mg, and C.R. was $2.34{\;}{\Omega}$ 2. In the dissolution of iron wire(1.529 g), the condition of reaction was H7O2(30 ml), HCI(20 ml) and $H_2O$(200 ml), time of the reaction was 21 min., P.W.(Piece weight) was 7.73 mg, and C.R. was $2.35{\;}{\Omega}$. Hydrogen peroxide dissolution method used sulfuric acid as the catalyst. 1. In the dissolution of iron wire(0.834 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and 1702(5 ml) ; time of the reaction was 5 min.30 sec, P.W.(Piece weight) was 7.74 mg, and C.R. was $2.33{\;}{\Omega}$ 2. In the dissolution of iron wire(1.112 g), the condition of reaction was $H_2O$(65 ml), $H_2SO_4$(5 ml) and $H_2O_2$(5 ml) ; time of the reaction was 4 min.30 sec, P.W.(Piece weight) was 7.75 mg, and C.R. was $2.33{\;}{\Omega}$. Hydrogen peroxide dissolution method used hydrochloric acid and sulfuric acid as the catalyst confirmed a clean technology, because there were not occurred a pollutant discharged in the existing method.

• 한국표면공학회지
• /
• 제36권5호
• /
• pp.364-372
• /
• 2003

In continuous galvanizing process, dissolution of iron into molten zinc results in a fairly great amount of dross. In order to decrease dross, the amount of dissolved iron of strip in molten zinc was investigated in the range of 0∼0.22%Al content, 440∼$470^{\circ}C$ strip temperature and 3∼60 sec dipping time. Uniform Fe-Al-Zn inhibition layer was formed in the coating layer/strip interface not only in the grain boundary but also in the grain of substrate with the increase of Al content in the zinc pot, while the amount of iron dissolution was decreased. Inhibition layer was unstable as the dipping time and strip temperature increased and the amount of iron dissolution increased.

• Corrosion Science and Technology
• /
• 제4권2호
• /
• pp.45-50
• /
• 2005

A 3% NaCl solution of 1 $dm^3$ circulated with 1.5 $dm^3/min$ by a pump for 24 h in the presence of magnetic field. An iron plate immersed in a $100cm^3$ of test solution for 24 h. The rest potential and pH on surface fixed after 3 h. Containing 0~120 ppm of Fe(II) ion, the dissolution in the magnetically treated solution rose comparing with that in the non-magnetically treated solution. The dissolution amount reached to maximum at 50 ppm, then fixed in the non-magnetically treated solution. When Fe(II) ion existed in the magnetically treated solution, dissolution accelerated a little. In the non-magnetic treated solution containing 10~125 ppm of Fe(III) ion existed, the dissolution accelerated. The dissolution amounts reached to maximum at 50 ppm, then decreased from maximum value. In the magnetically treated solution, the dissolution amounts reached to minimum until 50 ppm, then increased from minimum value. The dissolution amounts affected larger with increasing of magnetic flux density. Fe(II), Fe(III) ions and magnetic treatment affected to formation of $Fe(OH)_2$ and/or $Fe_3O_4$ films. The magnetically treated effects memorized about one month.

• Korean Chemical Engineering Research
• /
• 제55권5호
• /
• pp.711-717
• /
• 2017

A fundamental study was conducted on the dissolution of North Korean magnesite using hydrochloric acid to understand the dissolution behavior of the magnesium and impurities. The influence of the acid concentration, particle size of the magnesite, reaction temperature, and pulp density on the dissolution of magnesium, iron, calcium, aluminum, and silicon dioxide was studied. The experimental results showed that 98.5% of magnesium, 86.9% of iron, 87.3% of calcium, 23.6% of aluminum, and 20.4% of silicon dioxide were dissolved when magnesite particle sizes within the range of $75{\sim}105{\mu}m$ were reacted using 3 M HCl solution under 6% pulp density at 363 K for 3 h. The residues that remained after the dissolution were silicon dioxide, talc, and clinochlore.

• 한국표면공학회지
• /
• 제9권2호
• /
• pp.1-7
• /
• 1976

The dissolving and growth kinetics of intermetallic compounds for the reaction between solid iron and molten zinc were studied under nitorgen atmosphere over the temperature range between470$^{\circ}C$ and 680$^{\circ}C$. The rates of dissolution of solid iron into molten zinc were obtained under a static conditon, The amount of dissolution of sold iron and the growth of intermetalic compounds could be determined by means of microscopy. The thickness of intermetallic compound at a given temperature increases with increasing time, whereas for a given time decreases with increasing temperature . The rate of dissolution is controlled by the diffusion process of iron in the effective boundary layer of molten zinc over the temperature range 470$^{\circ}$-530$^{\circ}C$, 570$^{\circ}$-620$^{\circ}C$, and 650$^{\circ}$-665$^{\circ}C$, while by the surface reaction over the range 530$^{\circ}$-570$^{\circ}C$ and 620$^{\circ}$-650$^{\circ}C$.

• 동아시아식생활학회지
• /
• 제9권4호
• /
• pp.483-488
• /
• 1999

산성조미료로 곡물식초.쌀식초의 주성분인 아세트산, 감귤류와 과즙에 함유되어 있는 구연산, 사과산을 이용하여 조리할 때, 철 냄비로부터 철이 얼마나 용출 되는지를 조사한 결과는 다음과 같다. 1. 아세트산, 사과산 및 구연산에 대한 철의 용출량은 사과산, 구연산, 아세트산 순이었으며 산농도에 비례하여 증가하였다. 그 중에서도 사과산을 첨가한 것이 철의 용출량이 매우 많았다. 2. 온도에 의한 철 냄비로부터의 철의 용출은 5$^{\circ}C$. 실온에서도 용출되었으며 온도가 상승함에 따라 현저한 용출을 볼 수 있었다. 3. 가열시간에 따른 철 냄비로부터 용출하는 철은 일정한 시간까지는 가열시간에 비례하여 증가하였다. 4. 냄비의 사용횟수에 따른 철 용출량의 변화는 사용횟수에 비례하여 증가하였다. 5. 철의 용출량은 오래 사용한 냄비보다 새 냄비가 많이 용출되었다. 이상의 결과에서 철 냄비에 산성조미료를 첨가하여 조리하는 것은 철을 섭취하는데 효과가 있음을 알 수 있었다.

• 한국지하수토양환경학회지:지하수토양환경
• /
• 제23권1호
• /
• pp.85-91
• /
• 2018

Arsenic (As) usually is bound to amorphous iron oxides in the soils, and it can be removed via dissolution of iron oxides. Inorganic acid and chelating agent are widely used to extract As in the soil washing. However, the overall performance is highly dependent on the state of As fractionation. In this study, oxalic acid and inorganic acids (HCl, $H_2SO_4$, and $H_3PO_4$) were applied to enhance the dissolution of iron oxides for remediation of As-contaminated soils. Oxalic acid was most effective to extract As from soils and removal of As was two times greater than other inorganic acids. Additionally, 75% of As bound to amorphous iron oxides was removed by 0.2 M oxalic acid. Arsenic removal by oxalic acid was directly proportional to the sum of labile fractions of As instead of the total concentration of As. Therefore, the oxalic acid could extract most As bound to amorphous iron oxides.

• 한국방재학회:학술대회논문집
• /
• 한국방재학회 2008년도 정기총회 및 학술발표대회
• /
• pp.807-810
• /
• 2008

영가철(ZVI)를 사용하는 투수성 반응벽체(PRB, Permeable reactive barrier)는 TCE(Trichloroethylene)와 같은 난분해성 유기물질이 포함된 지하수를 처리하는데 사용될 수 있다. 여기서 ZVI(Zero-valent iron)가 Ferric iron으로 산화되면서 TCE를 ethene으로 환원시킨다. Ferric iron으로 변화된 iron은 환원과정을 통해 Ferrous iron으로 다시 재생을 시켜야 PRB의 처리수명을 연장시킬 수 있다. Ferric iron을 Ferrous iron으로 환원시키기 위해서 철환원 박테리아(IRB, Iron-reducing bacteria)를 이용한다. 이번 연구에서는 IRB가 Ferric iron을 환원시키기 위해서 Ferric iron을 용해를 한다는 concept으로 실험을 해보았다. 실험은 증류수(DI water, De-ionized water), DI-water에 배지를 포함한 용액, 그리고 DI-water에 배지 및 IRB가 포함된 용액, 이 3가지 조건으로 수행했다. 실험결과 $Fe^{3+}$의 용해가 IRB가 포함된 용액, 배지가 포함된 용액, 증류수 순으로 잘 되는 것으로 나타났다.

• 한국산학기술학회논문지
• /
• 제3권3호
• /
• pp.198-202
• /
• 2002

암모니아 대신 에탄올아민은 원자력 발전소 2차계통수에서 pH를 증가시켜 철 부식을 억제하고, 증기발생기 전열관의 건전성을 제고하기 위해 사용하고 있다. 에탄올아민은 암모니아와 물리화학적 성질이 다르므로, 증기발생기에 유입되는 부식생성물의 용해와 흡착, 이온성 불순물의 잠복현상에 미치는 영향이 다르다. 본 연구에서는 온도가 증가함에 따라 암모니아와 에탄올아민이 부식생성물에 대한 용해와 흡착, 이온성 불순물의 잠복현상에 미치는 영향을 조사하였다. 2차 계통수의 pH제어제로서 에탄올아민은 암모니아보다 증기발생기 슬러지의 철산화물에 많이 흡착되어 철산화물의 용해도를 증가시키므로 퇴적된 슬러지의 양을 감소시키며, 또한 슬러지에 홉착된 불순물의 양을 감소시켜 잠복 현상을 억제할 것으로 판단된다.

• Corrosion Science and Technology
• /
• 제23권4호
• /
• pp.310-314
• /
• 2024

The corrosion behavior of high chromium white cast iron was studied in 0.5 mol dm^-3 H₂SO₄ + 0.01 mol dm^-3 HCl solution over time through electrochemical and immersion experiments. Potentiodynamic and potentiostatic polarizations revealed active-passivation transition behavior, with critical current densities observed at -0.27 V_SSE and 0.00 V_SSE, repectively. The former potential showed preferential dissolution of primary γ phases, while the latter one showed preferential dissolution of eutectic γ phases. Immersion tests showed an exponential increase in corrosion rate, with significant acceleration observed around 1000 seconds due to the onset of eutectic γ phase dissolution. Over a 24-hour immersion period, both γ phases exhibited extensive corrosion, leaving carbides largely intact. These findings elucidate distinct corrosion behaviors of high chromium white cast iron in acidic environments, providing critical insights into material performance evaluation. Understanding these mechanisms is essential for predicting the longevity and durability of materials in corrosive conditions, thereby informing better material design and application strategies.