• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 2006년도 춘계임시총회 및 제27회 학술발표대회
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• pp.47-55
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• 2006

실리콘웨이퍼 제조공정에서 발생되는 초산, 불산 및 질산을 함유한 3성분계 폐혼산으로부터 각 산을 분리하여 무기산으로 재활용하기 위하여 용매추출법을 적용하였다. 이러한 산을 선택적으로 분리하기 위해 추출제로 초산의 경우는 EHA(2-Ethylhexlalcohol)를 사용 하였으며 질산과 불산의 경우에는 TBP(Tri -butlyphosphate)를 사용하여 추출과정과 탈거과정에 대한 공정설계를 위한 기초 실험을 실시하였다. 3성분계 페혼산에서 먼저 초산을 추출 분리하고, 추출여액중 질산 및 불산을 순차적으로 연속 분리 할 수 있는 공정개발을 위하여 McCabe-Thiele해석을 통해 최적 투입유량비(O/A), 소요단수(Stage) 등을 결정하였다. 분석 결과 혼산으로부터 초산의 회수율은 90%이상 이었으며 초산추출여액에서 질산의 회수율은 90%이상, 최종 추출잔류액에서 불산의 회수율은 67%이상 이었다.

• 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%.

• 한국자원리싸이클링학회:학술대회논문집
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• 한국자원리싸이클링학회 2006년도 춘계임시총회 및 제27회 학술발표대회
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• pp.78-85
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• 2006

In textile industries, waste effluent containing zinc is generated during the manufacture of rayon yarn from the wood pulp or cotton linters. Due to the strict environmental regulations and the presence of toxic metallic and other constituents, the discharge of industrial effluents in the sewage or disposal of solid sludge as landfill is restricted. Before recycling of zinc as zinc sulphate solution to the spinning-bath of the rayon manufacturing plant the zinc sulphate solution must be free from calcium, which is deleterious to the process as gypsum precipitates with the increase in concentration and forms scale in the bath. In the present work an attempt has been made to develop a process following solvent extraction technique using thiophosphinic extractants, Cyanex 272 and 302 modified with isodecanol and diluted in kerosene to recover zinc from rayon effluent. Various process parameters viz. extraction of zinc from different concentration of solution, distribution ratio, selective extraction, O/A ratio on extraction and stripping from the loaded organic, complex formation in the organic phase etc. have been studied to see the feasibility of the process. The extractant Cyanex 302 has been found selective for the recovery of 99.99% of zinc from the effluent above equilibrium pH 3.4 maintaining the O/A ratio of 1/30 leaving all the calcium in the raffinate. It selectively extracted zinc in the form of complex $[R_{2}Zn.3RH]_{org}$ and retained all the calcium in the aqueous raffinate. The zinc from the loaded Cyanex 302 can be stripped with 10% sulphuric acid at even O/A ratio of 10 without affecting the stripping efficiency. The stripped solution thus obtained could be recycled in the spinning bath of the rayon plant. The raffinate obtained after the recovery of zinc could be disposed safely without affacting environment.

• 한국응용과학기술학회지
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• 제34권2호
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• pp.289-295
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• 2017

현 국제해사기구(IMO)에서의 선박엔진에서 발생되는 NOx와 SOx 등의 연소 가스 배출에 대한 규제 강화에 따라, 발트 해 연안을 지나는 모든 선박들은 배출되는 연소가스 저감장치를 장착해야 된다. 국내에서도 IMO의 규제에 따른 NOx와 SOx를 저감장치를 개발하고 있으며, 그중에 대표적인 장치인 Scrubber는 세정액으로 암모니아수와 요소수를 사용하게 되고 사용된 폐 세정액에는 NOx와 SOx와 반응한 질산암모늄과 황산암모늄이 포함되어 있다. 본 연구에서는 폐 세정액이 포함하고 있는 유용한 부산물을 유기용매를 사용하는 염석법을 적용하여 회수하였다. 질산암모늄과 황산암모늄의 회수방법과 질안석회를 추출 후 회수된 부산물의 정성분석을 위하여, FT-IR 분석을 통하여 물질의 정성적 특성과 화학적 조성을 평가해 보았다. 한편 응집제를 투입하여 질안석회를 침전시켜 비료상의 물질로 회수하였다. $FeSO_4$ 응집제와 $CaCl_2$를 응집보조제로 사용하고 입자의 크기를 키우기 위해 $CaCO_3$를 사용하였다.

• 청정기술
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• 제23권4호
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• pp.393-400
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• 2017

본 연구에서는 염화제이철의 재생공정으로 기존 용매추출법에서 사용하고 있는 용매인 TBP 및 Alamine336 대신에 새로운 용매를 통해 용액 내에 존재하는 Ni과 Fe를 분리 및 회수하는 공정을 개발하였다. Lab 실험을 통하여 실험조건을 최적화하였으며, 이를 바탕으로 상업화를 위한 $10L\;h^{-1}$급 파일럿 설비를 구축하였다. 또한 파일럿 실험을 통하여 양산을 위한 공정 데이터를 확보하였으며, 제조된 염화제이철의 부식실험을 통하여 사용할 수 있는 제품 품질에 문제없음을 확인하였다.

• Journal of the Korean Wood Science and Technology
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• 제19권4호
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• pp.80-84
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• 1991

Lignocellulosic biomass including acetosolv ricestraw and spruce lignin were liquefied and converted into liquid hydrocarbons by catalytic hydroliquefaction reaction. These experimental works were carried out in 1-liter-capacity autoclave using 50% tetralin and m-cresol solution respectively as soluble solvent and Ni. Pd. Fe and red mud as catalyst. $H_2$ gas was supplied into the reactor for escaltion of deoxhydroenolysis reaction. Catalyst concentrations were 1 % of raw material based on weight. The ratio between raw materials and soluble solvent are 1g and 10cc. The reaction conditions are 400-$700^{\circ}C$ of reaction temperature, 10-50 atms of reaction pressure. The highest yield of hydrocarbon, so called "product oil" showed 32% and 5.5% of lowest char formation when red mud was used as catalyst. The product oil yields from those of other catalysts were in the range of 20-29%. The influence of different initial hydrogen pressures was examined in the range d 30-50 atms. A minimum pressure of 35 atms was necessary to obtain a complete recovery of souble solvent for recycling.

• Korean Chemical Engineering Research
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• 제53권2호
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• pp.137-144
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• 2015

The present paper deals with the extractive separation and selective recovery of nickel and lithium from the sulfate leachate of cathode scrap generated during the manufacture of LIBs. The conditions for extraction, scrubbing and stripping of nickel from lithium were optimized with an aqueous feed containing $2.54kg{\cdot}m^{-3}$ Ni and $4.82kg{\cdot}m^{-3}$ Li using PC-88A. Over 99.6% nickel was extracted with $0.15kmol{\cdot}m^{-3}$ PC-88A in two counter-current stages at O/A=1 and pH=6.5. Effective scrubbing Li from loaded organic was systematically studied with a dilute $Na_2CO_3$ solution ($0.10kmol{\cdot}m^{-3}$). The McCabe-Thiele diagram suggests two counter-current scrubbing stages are required at O/A=2/3 to yield lithium-scrubbing efficiency of 99.6%. The proposed process showed advantages of simplicity, and high purity (99.9%) nickel sulfate recovery along with lithium to ensure the complete recycling of the waste from LIBs manufacturing process.

• 한국응용과학기술학회지
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• 제34권2호
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• pp.210-216
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• 2017

선박엔진에서 발생하는 NOx 및 SOx 제거용 스크러버 폐세정액에 포함되어 있는 저농도상의 질산 및 황산이온을 비료상 물질로 회수하고자 하였다. 본 연구에서는 네 가지 유기용매를 적용하여 선택적으로 추출하여 회수하는 방법을 시험하였다. 아세톤과 메틸알콜을 이용하여 추출한 질산암모늄과 디에틸에테르와 에틸알콜을 적용한 황산암모늄의 시료를 적외석흡수분광법(IR)을 이용하여 분석한 결과, 상용제품과 거의 동일한 구성성분으로 나타났다. 이때 폐수로부터의 회수율은 최대 89%와 80%까지 각각 얻을 수 있었다. 따라서 배기가스 스크러버에 잔존해있는 질산이온과 황산이온에 대한 회수는 사용하는 용매의 선택도 및 용해도가 핵심적인 요소인 것으로 판단된다.

• 분석과학
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• 제37권2호
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• pp.123-129
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• 2024

We present a rapid method for the determination of Cs, Sr, and Ba, heat generators found in highly active liquid wastes, by gas-pressurized extraction chromatography (GPEC) using a column containing a cation-exchange resin. GPEC is a microscale column chromatographic technique that uses a constant flow rate of solvent (0.07 mL/min) with pressurized nitrogen gas supplied through a valve. In particular, because this method uses a small sample volume (a few hundred microliters), it produces less chemical waste and allows for faster separation compared to traditional column chromatography. In this study, we evaluated the separation of Cs, Sr, and Ba using GPEC. The eluate from the column (GPEC or conventional column chromatography) was quantitatively analyzed using inductively coupled plasma-mass spectrometry to measure the column recovery and precision. The column reproducibility of the proposed GPEC system (RSDs of recoveries) ranged from 2.7 to 4.1 %, and the column recoveries for the three elements ranged from 72 to 98% when aqueous HCl was used as the eluent. The GPEC results are slightly different in efficiency and separation resolution compared to those of conventional column chromatography because of the differences in the eluent flow rate as well as the internal diameter and length of the column. However, the two methods had similar recoveries for Cs and Sr, and the precision of GPEC was improved by two-fold. Remarkably, the solvent volume required for GPEC analysis was five times lower than that of the conventional method, and the total analysis time was 11 times shorter.

• 청정기술
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• 제26권2호
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• pp.116-121
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• 2020

본 연구에서는 유가금속 회수를 한 전기차 폐배터리 부산물의 재활용에 관하여 연구하였다. 폐배터리 부산물에는 희토류들이 남아있으나, 부산물의 형태로는 소재로서의 가치가 없기에 정제과정을 거쳐 희토류 산화물로 회수하였다. 희토류침전분말 형태의 부산물을 30% 수산화나트륨을 이용하여 가공이 편한 수산화물로 변환한 뒤, 옥살산의 용해도 차이를 이용하여 남아 있는 불순물을 정제한 뒤, D2EHPA (Di-(2-ethylhexyl) phosphoric acid)를 사용하여 이트륨을 분리하였다. 과망가니즈산 칼륨을 이용하여 세륨을 분리 후, PC88A (2-ethylhexylphosphonic acid mono-2-ethylhexyl ester)를 사용하여 란타넘과 네오디뮴을 분리하였다. 그 후 800 ℃의 온도에서 소성하여 란타넘, 네오디뮴 산화물로 재생하는 방법을 확인하였다.