• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.432-436
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• 2001

In this study, calcium sulfate(gypsum) powder was obtained using waste sulfuric acid and stainless refinery sludge by- produced from chemical reagent and the iron industry, by the neutralization of waste sulfuric acid. As variables for the experiment the mole ratio of the H$_2$SO$_4$ : Ca(OH)$_2$, the pH, the reaction temperature and time, the amount of catalyst were used. The crystal shape and microstructure of obtained powder were observed by XRD and SEM, and the thermal property was investigated by DTA. As the NaCl is added 0~20wt% as a catalyst to the H$_2$SO$_4$ : Ca(OH)$_2$, system it can be found that the crystal shape goes through the processes as follows : gypsum dihydratlongrightarrowgypsum hemihydrate＋gypsum dihydratelongrightarrowgypsum hemihydrate. And gypsum hemihydrate is $\beta$-type as the result of DTA. As waste sulfuric acid and stainless refinery sludge were used, the pH of reacted solution (which was 0.8) was rapidly raised up to 8~9 by the addition of stainless sludge and gypsum dihydrate was produced as a by-product. Therefore, it was found that stainless refinery sludge is sufficiently applicable for the neutralization of waste sulfuric acid.

• Journal of the Korean Wood Science and Technology
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• 제41권2호
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• pp.87-99
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• 2013

Waste paper stands for the major biodegradable organic fraction of most of municipal solid waste. The potential of waste paper for glucose production was investigated in this current work. The pretreatment was accomplished by first subjecting waste paper to disintegration time (30 s), followed by ink removal of disintegrated waste paper using an deinking agent. Concentrated acid hydrolysis of waste paper with sulfuric acid was optimized to maximize glucose conversion. The concentrated acid hydrolysis conditions for waste paper (disintegrated time: 30 s, deinking agent loading : 15 ml) were optimized by using central composite design and response surface methodology. The optimization process employed a central composite design, where the investigated variables were acid concentration (60~80%), loading sulfuric acid (1~5 ml) and reaction time (1~5 h). All the tested variables were identified to have significant effects (p < 0.05) on glucose conversion. The optimum concentrated acid hydrolysis conditions were acid concentration of 70.8%, loading sulfuric acid of 3.2 ml and a reaction time of 3.6 h. This research of concentrated acid hydrolysis was a promising method to improve glucose conversion for waste paper.

• 자원리싸이클링
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• 제29권3호
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• pp.61-74
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• 2020

본 연구에서는 폐형광등 처리 공정의 경제성 확보를 위하여 수행되었으며, 폐형광등 유리의 글래스비드용 원료로서의 사용 가능성, 폐형광체 분말로부터 희토류의 침출, 희토류 침출액으로부터 희토류의 용매추출 가능성 등을 검토하였다. 폐형광체는 산화이트륨 28.9%, 산화세륨이 3.46%, 산화유로퓸 1.95%, 산화터븀 1.76%, 산화란탄 1.43% 순으로 함유되어 있어 회수 및 정제 시 경제성이 충분할 것으로 판단되었다. 폐형광등 유리를 사용하여 글래스비드를 시험 생산 한 결과 그 생산수율과 품질이 우수하여 폐형광등 유리를 글래스비드용 원료로 사용할 수 있을 것으로 판단되었다. 소다배소한 폐형광체를 수침출하면 알루미늄과 규소성분 및 잔류 탄산나트륨 등이 용해하며, 이 수용액에 탄산가스를 불어 넣어 pH를 7 정도로 떨어뜨리면 NaAl₂(CO₃)(OH)₂와 SiO₂ 등이 침전하였다. 자이렌을 희석제로 사용하는 cyanex272-hydrochloric acid, cyanex272-sulfuric acid, D2EHPA-hydrochloric acid, D2EHPA-sulfuric acid, lonquest290-hydrochloric acid, lonquest290-sulfuric acid, p507-hydrochloric acid 조합의 용매추출에서 Y, Eu, Ce, La, Tb의 추출률이 100%에 가깝다. 그러나 동일 조건에서의 원소별 추출률의 차이, 즉 선택성은 16% 이하이다.

• 시멘트
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• 통권30호
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• pp.44-50
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• 1969

To manufacture portland cement and sulfuric acid from gypsum has long been established in Europe. As sulfur, more Precisely sulfuric acid, is getting around shortage, it boosts hunt for alternate sources and for new fertilizer process. As the result, all

• 한국염색가공학회지
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• 제7권2호
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• pp.9-16
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• 1995

When alkaline waste water of PET fabric is treated with sulfuric acid, undegradable material, crude TPA sludge is generated, so that treatment has a serious problem. The result of DMT synthesis using crude TPA sludge generated from PET alkaline waste water were as follows: 1. When crude TPA generated from alkaline waste water is reactioned with methanol under catalyst of sulfuric acid, pure DMT can be obtained. 2. In DMT synthesis from crude TPA, addition of copper sulfate can increase yield, and increasing the amount of sulfuric acid can shorten reaction time.

• 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.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.421-426
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• 2001

The pneumatic classification and acidic leaching behaviors of phosphor sludge have been examined to establish the recycling system of rare earth components contained in waste fluorescent lamp. At first, separation characteristic of rare earth components and calcium phosphate in phosphor sludge was investigated by pneumatic classification. After pneumatic classification of phosphor sludge, rare earth components were leached in various acidic solutions and sodium hydroxide solution. For recovery of soluble component in leaching solution, rare earth components were separated as hydroxide and oxalate precipitations. The experimental results obtained are summarized as follows: (1) In classification process, rare earth components in phosphor sludge were concentrated to 29.3% from 13.3%, and its yield was 32.9%. (2) In leaching process, sulfuric acid solution was more effective one as a leaching solvent of rare earth component than other solutions. Y and Eu components in phosphor sludge were dissolved in sulfuric acid solution of 1.5 k㏖/㎥, and other rare earth components were rarely dissolved in leaching solution. Leaching degrees of Y and Eu were respectively 92% and 98% in the following optimum leaching conditions; sulfuric acid concentration is 1.5 k㏖/㎥ , leaching temperature 343 K, leaching time 3.6 ks and pulp concentration 30 kg/㎥. (3) Y and Eu components of phosphor sludge contained in waste fluorescent lamp were, effectively recovered by three processes of pneumatic classification, sulfuric acid leaching and oxalate precipitation methods. Their recovery was finally about 65 %, and its purity was 98.2%.

• 자원리싸이클링
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• 제16권5호
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• pp.3-7
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• 2007

알루미늄 지금 및 스크랩 용해시 발생되는 알루미늄 폐드로스를 사용하여 황산알루미늄(Alum)과 폴리염화알루미늄(pooly Aluminium Chloride: PAC)을 제조하였다. 알루미늄 폐드로스를 황산과 반응시켜 폐드로스 중에 잔류하는 금속알루미늄을 용액 중으로 침출시켜 황산알루미늄 용액으로 제조하였으며, 알루미늄 폐드로스를 염산과 반응시켜 PAC 용액으로 제조하여 수처리응집제로 재활용하고자 하였다. 이와 같이 알루미늄 폐드로스를 재활용함으로써 수산화알루미늄을 원료로 사용하여 황산알루미늄과 PAC를 제조하는 종래의 방법에 비해 제품의 원료비를 줄일 수 있고, 매립 등으로 폐기시켜야 할 폐드로스의 양을 줄이는 효과가 있었다.

• 한국콘크리트학회:학술대회논문집
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• 한국콘크리트학회 2004년도 추계 학술발표회 제16권2호
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• pp.719-722
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• 2004

Resins using recycled PET offer the possibility of a lower source cost of materials for making useful polymer concrete products. The purposed of this paper is to form a part of reducing the damage of sulfuric acid, through investigating recycled PET polymer concrete, . immersed at sulfuric acid solution for 84 days. Recycled PET PC is excellent chemical resistance, resulting in the role of unsaturated polyester resin which consists of polymer chain structure accomplishes bond of aggregates and filler strongly. Also, Recycled PET PC, used fly-ash as filler, is stronger resistance of sulfuric acid corrosion than $CaCO_3$, because it is composed of $SiO_2$ and very strong glassy crystal structure. Therefore, Recycled PET PC, used fly-ash as filler, is available under corrosion circumstances like sewer pipe or waste disposal plant.

• 자원리싸이클링
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• 제15권6호
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• pp.16-24
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• 2006

본 연구에서는 소각비산재의 습식 처리에 관한 기초 자료를 얻을 목적으로 소각비산재의 물성, 황산에 의한 소각비산재의 중화과정, 황산에 의한 소각비산재의 탈염소 반응, 소각비산재와 황산의 반응에 의하여 생성한 이수석고의 결정성장 및 미립 중금속의 분리 둥에 관하여 조사하였다. 소각비산재와 황산을 반응시켜 염산을 회수하고 그 잔류물의 대부분을 차지하는 석고 성분을 선택적으로 결정성장 시켜 결정성이수석고와 중금속으로 분리하는 일련의 공정에서 100g의 소각비산재위 85g의 진한 황산을 사용하는 경우 35% 염산 52.6g, 순도가 98%이상인 결정질 이수석고 116.9g을 회수할 수 있으며, 이 과정에서 2.65g의 활성탄을 주로하는 조립불순물과 7.85g의 중금속함유 미립자들이 분리되었다.