• 자원리싸이클링
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• 제21권3호
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• pp.15-20
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• 2012

본 논문에서는 연료전지 막전극접합체에서 막분리 및 염산침출법을 이용하여 백금과 루테늄을 침출하는 연구를 하였다. 증류수, 10 vol.% 부탄올 용액, 15 vol.% 양이온 계면활성제(Koremul-LN-7)를 이용하여 연료전지 막전극접합체의 전해질막과 확산층을 침지법으로 촉매입자의 분산 없이 분리하였다. 그리고 질산 또는 과산화수소를 산화제로 하고 사용하는 염산에 의해 분리된 가스확산층의 촉매에 함유된 백금과 루테늄 금속을 침출하는 연구를 하였다. 과산화수소를 산화제로 사용하였을 때 백금과 루테늄의 침출율이 더 높았으며 최적 조건은 $90^{\circ}C$에서 염산 농도 8 M, 과산화수소 첨가량 5 M, 침출시간 6시간이었다. 이 조건에서 백금의 침출률은 98%, 루테늄의 침출율은 71.5%였다.

• 자원리싸이클링
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• 제27권3호
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• pp.93-99
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• 2018

본 연구에서는 디스플레이 산업의 백금 폐스크랩을 용해, 용매추출을 통하여 백금족 성분을 효율적으로 추출하고, 추출된 백금용액을 디젤자동차 배가스 정화촉매용 전구체 용액으로서 제조하고, 그 촉매활성을 실험하였다. 용액화학적 이론 연구를 통하여 백금 화학종의 수용액상 거동을 조사하였고, 화학종들의 존재영역 및 거동을 근거로 추출 및 분리 가능방안을 수립하였다. 전기화학적 방법에 의해 폐스크랩을 용해시킴으로써, 용해시간 단축 및 추출효율을 높였으며, 로듐 성분을 분리 제거, TBP에 의한 용매추출, 염산에 의한 탈거 공정을 거쳐 Pt-Chloride-$H_2O$ 계 백금용액을 용액을 제조하고, 이 용액을 원료로 액상 아민화 반응을 통해 아민산 백금용액을 제조한 다음, 카본블랙의 연소반응에 대한 촉매 활성을 실험함으로써, 백금족 폐스크랩으로부터 고부가 백금족 화합물의 제조가능성을 연구하였다.

• Journal of Pharmaceutical Investigation
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• 제25권1호
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• pp.37-46
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• 1995

The experiment was designed to investigate the sustained release dosage form of silymarin (SL) from chitosan (CS) carrier. Solid dispersed system was prepared by mixing the drug with chitosan. This solid dispersed system was cross-linked by glutaraldehyde, formaldehyde, acetaldehyde and butylaldehyde, respectively. The dissolution rates of these preparations were compared with each other in vitro. The silymarin was mired with anionic alginate gel and bead was prepared by dropping this mixture to cationic chitosan solution including calcium chloride. Chitosan encapsulated alginate bead after drying in the oven was investigated for the dissolution rate. The dissolution rate of SL-CS mixture was delayed with increase in the amounts of CS and the concentration of aldehyde. The effect on the delay of dissolution rate was in the increasing order of formaldehyde, glutaraldehyde, acetaldehyde, butylaldehyde. The dissolution rate of chitosan encapsulated alginate bead was parallel with the concentration of chitosan in diluted hydrochloric acid solution and delayed with increase in the concentration of chitosan in phosphate buffer solution.

• 한국염색가공학회지
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• 제13권1호
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• pp.38-44
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• 2001

The adsorption ability of dyes on chitin, a natural polymer was investigated for decolorization of dye wastewater. Chitin was manufactured in lab by decalcification in dilute aqueous hydrochloric acid solution and deproteination in dilute aqueous sodium hydroxide solution with shrimp shells. Absorbance of residue solution of dyebaths after dye adsorptions of chtin were measured in varieties of dye concentration and dipping periods. Three kinds of Direct dyes -C.I. Direct Red 81 (red 81), C.I. Direct Brown l(brown 1) and C.I. Direct Green 26(green 26) - were used. Red 81 and brown 1 have smaller molecular weight than green 26. The results from experimentals were of]tamed as follows: 1) Adsorption of green 26 was improved in dyebath by addition of salt, but red 81 and brown 1 were not found any improvements. 2) Smaller size of chitin particles could be absorbed much more speedy. In this experiments, the smallest range of chitin particle size was $250\mu{m}$ and less. 3) The most efficient amount of chitin for 20m1 of dyebath was 0.2g, 4) Both of red 81 and brown 1 showed good and speedy adsorption abilities as dyestuffs of over 90 percent in just one minute in dyebath of 0.01% dye concentration. But green 26 was absorbed slowly because of its large molecular weight. It took 40minutes to absorb dyestuffs of over 90 percent in dyebath of 0.01% dye concentration.

• Membrane and Water Treatment
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• 제5권3호
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• pp.207-219
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• 2014

Fouling is one of the critical factors associated with the application of membrane technology in treating palm oil mill effluent (POME), due to the presence of high concentration of solid organic matter, oil, and grease. In order to overcome this, chemical cleaning is needed to enhance the effectiveness of membranes for filtration. The potential use of sodium hydroxide (NaOH), sodium chloride (NaCl), hydrochloric acid (HCl), ethylenediaminetetraacetic acid (EDTA), and ultrapure water (UPW) as cleaning agents have been investigated in this study. It was found that sodium hydroxide is the most powerful cleaning agent, the optimum conditions that apply are as follows: 3% for the concentration of NaOH, $45^{\circ}C$ for temperature solution, 5 bar operating pressure, and solution pH 11.64. Overall, flux recovery reached 99.5%. SEM images demonstrated that the membrane surface after cleaning demonstrated similar performance to fresh membranes. This is indicative of the fact that NaOH solution is capable of removing almost all of the foulants from PES membranes.

• Journal of Electrochemical Science and Technology
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• 제10권1호
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• pp.69-81
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• 2019

The corrosion inhibiting mechanism of Vietnam orange peel essential oil (OPEO) for mild steel in 1 N HCl solution was investigated elaborately. Corrosion inhibition ability of OPEO was characterized by electrochemical polarization, electrochemical impedance spectroscopy (EIS), and weight loss method. In the corrosive solution, OPEO worked as a mixed inhibitor and the inhibition efficiency of OPEO increased with the increase of its concentration. High inhibition efficiencies over 90% were achieved for the concentration of 3 - 4 g/L OPEO, comparable to that of 3.5 g/L urotropine (URO), a commercial corrosion inhibitor for acid media used in industry. By using adsorption isotherm models (Langmuir, Temkin and Frumkin), thermodynamic parameters of adsorption were calculated. The obtained results indicated physical adsorption mechanism of OPEO on the steel surface. The components responsible for the corrosion inhibition activity of OPEO were not only D-limonene, but also other compounds, which contain C=O, C=C, O-H, C-O-C, -C=CH and C-H bonding groups in the molecules.

• 한국세라믹학회지
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• 제47권6호
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• pp.613-617
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• 2010

Ferro-Nickel slag is one of the by-products in Ferro-Nickel manufacturing process. The slag is composed of $SiO_2$, MgO, $Fe_2O_3$ and others. But the slag has been buried at landfill despite having valuable elements. This study tried to extract Mg ion and fabricate Mg compound from ferro-nickel slag using hydrochloric acid solution. Mg ion was extracted with Si, Fe and other ions in HCl solution. So reprocess was needed for gaining high purity Mg ion. It was thought that Si ion or $SiO_2$ precipitated in HCl solution and removed from solution in filtering process. Fe ion converted into $Fe(OH)_3$ after reacted with $NH_4OH$ and precipitated in HCl solution. After these process, the filtrate was composed of high purity Mg ion. $MgCl_2{\cdot}NH_4Cl{\cdot}6H_2O$ was obtained through drying of filtrate and this product was changed into MgO by burning process ($600^{\circ}C$-30 min). That is, 1st material or solution for manufacturing 2nd product was fabricated using acid dissolution method and other treatments.

• 자원리싸이클링
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• 제26권3호
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• pp.26-31
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• 2017

LIX 63 은 6 M의 염산용액에서 백금(IV), 이리듐(IV) 및 로듐(III)에 비해 팔라듐(II)에 대한 선택성이 크다. 또한 염산용액의 농도는 이리듐과 LIX 63간에 일어나는 산화-환원반응에 큰 영향을 미친다. 따라서 상기 4개의 백금족 금속을 함유한 3 M의 염산용액에서 LIX 63에 의한 분리성을 검토하였다. 3 M의 염산용액에서 LIX 63은 오직 팔라듐만을 추출했으며, 6 M의 염산용액에 비해 추출율이 높았다. TBP를 사용하면 팔라듐 추출여액으로부터 백금만을 추출하는 것이 가능하였다. 백금 추출후 $NaClO_3$로 추출여액에 함유된 이리듐을 산화시킨 다음 Aliquat 336를 접촉시키면 이리듐만이 추출되었다. 각각의 용매추출단계에 대해 최적의 탈거조건을 구했다. 본 논문의 공정으로 4개의 백금족 금속을 3 M의 염산용액에서 분리하는 것이 가능하였다.

• 한국재료학회지
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• 제11권2호
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• pp.76-81
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• 2001

전자산업 폐기물의 산침출 용액으로부터 전해채취법에 의해 Au와 Pd를 선택적으로 회수하기 위하여, 염산수용액 중에서 Au와 Pd의 전기화학적 거동을 voltammetry방법에 의해 조사하였다. Au단독 전해욕에서 Au의 환원전위는 약 800mV이었고 환원한계전류는 약 470mV에서 나타났으며, Pd 단독 전해욕에서 Pd의 환원전위는 약 500mV이었고 환원한계전류는 약 150mV에서 나타났다. 그러나, Au-Pd혼합 전해용액에서, Au의 환원전위 및 환원한계전위 값은 전해욕 중 Pd의 농도가 증가함에 따라 감소하였고, Au와 Pd의 환원한계전위 값은 Au-Pd 전해욕 중 Pd 전해용액의 함유량이 30vo1%일 때 가장 가까운 값을 나타내었다

• 한국결정성장학회지
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• 제32권1호
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• pp.40-44
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• 2022

35 % 농도의 염산 용액을 이용하여 α-Ga₂O₃ epitaxy 박막의 습식 식각을 수행하였다. 35 % 염산 용액의 온도가 증가함에 따라 α-Ga₂O₃ epitaxy 박막의 식각 속도가 증가하였고, 본 연구에서 시도한 가장 높은 온도인 75℃에서 119.6 nm/min의 식각 속도를 나타내었다. 식각 반응의 활성화 에너지는 0.776 eV로 계산되었고, HCl 용액에서의 습식 식각은 reaction-limited 반응 기구에 의해 지배됨을 확인하였다. 각 온도에서 식각된 표면들의 AFM 분석결과 식각 용액의 온도가 증가함에 따라 식각된 표면의 표면조도가 증가함을 알 수 있었다.