• 한국표면공학회지
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• 제45권5호
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• pp.198-205
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• 2012

The corrosion properties of anodized films on aluminium 6070 alloy in a sulfuric acid have been studied. Comparison to evaluate the anodized A6070 and pure 6070 specimen, corrosion tests in $HNO_3$ vapor environment of the 20 wt.% were performed up to 72 hours. Characteristics of film formation and surface morphology were examined by optical microscopy, FE-SEM, and EDS. The oxide film anodized in the sulfuric acid solution contained 5 to 10 wt.% of sulfur. In the initial stages of corrosion, anodized specimens exhibited corrosion resistance than the pure specimen. However, the corrosion conditions in 24 hours, corrosion was far more anodized specimen than pure specimen. Therefore, anodized films contained sulfur, nitric acid vapor in the environment is thought to stimulate corrosion.

• Asian Journal of Atmospheric Environment
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• 제4권1호
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• pp.55-61
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• 2010

The sensitivity of aerosol light extinction coefficient to the aerosol chemical composition change is estimated by (1) calculating the aerosol water content and chemical concentrations by a gas/particle equilibrium model and (2) calculating the aerosol light extinction coefficient by a Mie theory based optical model. The major chemical species are total (gas and particle phase) sulfuric acid, total nitric acid, and total ammonia which are based on the measurement data at Seoul and Gosan. At Seoul, since there were enough ammonia to neutralize both total sulfuric acid and total nitric acid, the dry ionic concentration is most sensitive to the variation of the total nitric acid level, while the total mass concentration (ionic concentration plus water content) and thus, the aerosol light extinction coefficient are primarily determined by the total sulfuric acid. At Gosan, since the concentration of ambient sulfuric acid was the highest among the inorganic species, sulfate salts determined aerosol hygroscopicity. Thus, both ionic and total mass concentration, and resultant aerosol light extinction coefficient are primarily determined by the sulfuric acid level.

• 청정기술
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• 제28권2호
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• pp.103-109
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• 2022

Nd-Fe-B 폐영구자석 스크랩에는 희토류가 약 20~30% 함유되어 있고 철이 약 60~70% 함유되어 있으며, 황산침출 및 분별결정법을 통하여 희토류 및 철 성분을 회수하고자 하였다. 희토류와 철을 분리·회수하기 위하여 산화배소를 하지 않고 황산농도 및 광액농도비를 변수로 하여 침출특성을 확인하였다. 황산침출은 농도별로 3시간 동안 침출을 진행하였고 침출된 고상을 X-ray diffraction (XRD) 및 XRF (X-ray florescence spectrometry) 분석으로 결정상 및 조성 및 정량적 성분을 확인하였으며, 여액은 ICP 분석을 시행하였다. 3M 황산농도에서 침출했을 경우 네오디뮴 황산화물로 형성되었고 철 성분이 가장 적으며 회수율이 높았다. 남은 여액은 증발농축을 통하여 분별결정법을 하였으며 네오디뮴 성분은 7.0배 농축되었고 철 성분은 2.8배 농축되었다. 본 논문에서 폐영구자석의 산화배소 공정단계 없이 황산침출 및 분별결정법을 통한 희토류 성분의 회수율은 약 99.4%로 확인되었다.

• 공업화학
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• 제7권1호
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• pp.51-58
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• 1996

Ethylphenylcarbamate(EPC)와 포름알데히드를 산 촉매 하에서 축합하여 생성한[(ethoxycarbonyl)phenylaminomethyl phenylcarbamic acid ethyl esters(N-benzyl화합물)를 $90^{\circ}C$, 황산, 황산-무수에탄올 용매계, 황산-니트로벤젠 용매계, 3플루오르화 붕소 촉매 하에서 재배열반응에 의해 methylenediphenyldiurethane(MDU)의 합성조건을 검토한 결과 니트로벤젠 용매하에서 반응시킨것이 MDU 생성율이 64%로 가장 높은 생성율을 나타내었고 4,4'-MDU의 생성율도 전체 MDU의 58%를 차지하여 가장 높았다. EPC와 포름알데히드를 $70^{\circ}C$, 몇 가지 다른 양의 황산, 트리플루오르아세트산, 3플루오르화 붕소 촉매 하에서 축합과 재배열반응을 동시에 일으키기 위한 반응조건을 검토한 결과 촉매로서 황산의 양을 EPC 30mmol에 대해서 황산 17mmol을 첨가한 경우가 MDU의 생성율이 가장 높았으나 별도의 재배열 반응을 통한 합성보다 생성율이 낮았다.

• 분석과학
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• 제19권2호
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• pp.121-130
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• 2006

In this study, silver pre-treated activated carbons are transformed using sulfuric acid. From the results of adsorption, each isotherm shows a distinct knee band, which is characteristic of microporous adsorbents with capillary condensation in micropores. In order to reveal the causes of the differences in adsorption capacity and specific surface area after the samples were washed with various strengths of sulfuric acid, surface morphology and external pore structure were investigated by SEM. X-ray diffraction patterns indicated that Ag-activated carbons show better performance for silver and silver compounds removal by post-treatment with acid. The FT-IR spectra of silver-activated carbon samples show that the acid post-treatment was consequently associated with the removal of silver with an increased surface functional group containing oxygen of the activated carbon. The type and quality of oxygen groups are determined on the method proposed by Boehm. For the chemical composition microanalysis of silver-activated carbons transformed by post-treatment with sulfuric acid, samples were analyzed by EDX.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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• pp.179.1-179.1
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• 2011

Pretreatment of cellulosic biomass is necessary before enzymatic saccharification and fermentation. The objective of this study was to evaluate the effect of combined aqueous ammonia-dilute sulfuric acid treatment on cellulosic biomass. Miscanthus was pretreated using aqueous ammonia and dilute sulfuric acid solution under high temperature and pressure conditions to be converted into bioethanol. Aqueous ammonia treatment was performed with 15 %(w/w) ammonia solution at $150^{\circ}C$ of reaction temperature and 20 minutes of reaction time. And then, dilute sulfuric acid treatment was performed with 1.0 %(w/w) sulfuric acid solution at $150^{\circ}C$ of reaction temperature and 10 minutes of reaction time. The compositional variations of this combined aqueous ammonia-dilute sulfuric acid treatment resulted in 68.0 % of cellulose recovery and 95.7 % of hemicellulose, 81.3 % of lignin, 89.1 % of ash removal respectively. The enzymatic digestibility of 90.5 % was recorded in the combined pretreated Miscanthus sample and it was 14.7 times higher than the untreated sample. The ethanol yield in the Simultaneous Saccharification and Fermentation was 90.4 % of maximum theoretical yield based on cellulose content of the combined pretreated sample and it was about 98 % compared to the ${\alpha}$-cellulose ethanol yield.

• 한국융합학회논문지
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• 제7권5호
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• pp.169-173
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• 2016

알루미늄의 양극산화는 황산법, 수산법과 황산과 수산을 활용한 혼산법 등이 있다. 산업체에서 만들어지는 양극산화는 황산법으로 전해액속의 황산농도가 15~20 wt %이다. 연질 양극산화피막을 생성할 경우는 전해액의 온도가 $20{\sim}30^{\circ}C$ 범위에서 생산되고 있으며, 생산 전압은 직류전압으로 13~15 V 이내가 가장 많이 사용된다. 경질 양극산화피막을 생성할 경우는 전해액의 온도가 $0{\sim}-5^{\circ}C$에서 생산되어지고 있다. 본 연구에서는 황산법과 수산법을 이용하여 $50{\mu}m$ 두께의 양극산화피막(알루미나)를 제작하였다. 황산법과 수산법에 의해 시편을 제조하여 열 피로시험을 수행하였다. 황산법과 수산법의 균열발생온도는 $500^{\circ}C$와 $600^{\circ}C$이었다. 황산법의 균열발생온도는 수산법의 균열발생온도보다 낮았다. 시험결과 수산법의 열 피로는 황산법의 열 피로 특성보다 좋았다. 그 이유를 알루미늄과 알루미나의 열팽창계수와 제조온도로 설명하였다. 고온에서 사용되는 양극산화제품의 제조방법을 여기서의 융합 연구를 통해 제안 가능하게 되었다.

• 대한화학회지
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• 제45권6호
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• pp.546-548
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• 2001

클로로술폰산을 실리카겔과 반응시키면 실리카겔 표면에 황산이 공유결합으로 고정된 실리카황산을 얻게 된다. 무용매 조건하에서 마이크로웨이브를 쪼여주면서 실리카 황산과 젖은 $SiO_2$를 함께 사용하게 되면 아세탈을 화합물로 변화시키는 효과적인 탈아세탈 시약으로 사용할 수 있다.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.478-481
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• 2001

The spent petrochemical catalyst used in the manufacturing process of terephthalic-acid contains valuable metals such as cobalt and manganese. To recover these metals, sulfuric acid leaching was performed with hydrogen peroxide as a reducing agent. Low extractions of Mn, Co and Fe were obtained by sulfuric acid leaching without reducing agent. With adding hydrogen peroxide as a reducing agent, the high extraction of these metals could be obtained. Different from general leaching experiment, the extraction rates of metal components were decreased with increasing reaction temperature in this case. Under the optimum condition, the extraction rates of Mn, Co and Fe were 93.0%, 87.0% and 100% respectively.

• 한국재료학회지
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• 제21권1호
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• pp.1-7
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• 2011

Methods of producing hydrogen include steam reforming, electrochemical decomposition of water, and the SI process. Among these methods, the Sulfur iodine process is one of the most promising processes for hydrogen production. The thermochemical sulfur-iodine (SI) process uses heat from a high-temperature-gas nuclear reactor to produce $H_2$ gas; this process is known for its production of clean energy as it does not emit $CO_2$ from water. But the SI-process takes place in an extremely corrosive environment for the materials. To endure SI environments, the materials for the SI environment will have to have strong corrosion resistance. This work studies the corrosion resistances of the Fe-Si, Ni-Ti and Ni Alloys, which are tested in SI-process environments. Among the SI-process environments, the conditions of boiling sulfuric acid and decomposed sulfuric acid are selected in this study. Before testing in boiling sulfuric acid environments, the specimens of Fe-4.5Si, Fe-6Si, Ni-4.5Si, Ni-Ti-Si-Nb and Ni-Ti-Si-Nb-B are previously given heat treatment at $1000^{\circ}C$ for 48 hrs. The reason for this heat treatment is that those specimens have a passive film on the surface. The specimens are immersed for 3~14 days in 98wt% boiling sulfuric acid. Corrosion rates are measured by using the weight change after immersion. The corrosion rates of the Fe-6Si and Ni-Ti-Si-Nb-B are found to decrease as the time passes. The corrosion rates of Fe-6si and Ni-Ti-Si-Nb-B are measured at 0.056 mm/yr and 0.16 mm/yr, respectively. Hastelloy-X, Alloy 617, Alloy 800H and Haynes 230 are tested in the decomposed sulfuric acid for one day. Alloy 800H was found to show the best corrosion resistance among the materials. The corrosion rate of Alloy 800H is measured at -0.35 mm/yr. In these results, the corrosion resistance of materials depends on the stability of the oxide film formed on the surface. After testing in boiling sulfuric acid and in decomposed sulfuric acid environments, the surfaces and compositions of specimens are analyzed by SEM and EDX.