• 청정기술
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• 제14권4호
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• pp.248-255
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• 2008

초임계이산화탄소의 존재 하에서 세 가지 이온성액체(IL)의 부피팽창을 압력 32 MPa까지, 온도 313.15에서 333.15 K까지 뷰셀(view cell) 내에서 측정하였다. 이미다졸유도체 이온성액체인 육불화 1-부틸-3-메틸이미다졸([bmim][$PF_6$]), 사불화 1-부틸-3-메틸이미다졸([bmim][$BF_4$]), 사불화 1-옥틸-3-메틸이미다졸([omim][$BF_4$])을 연구에 사용하여, 압력, 온도, 양이온과 음이온의 성질, 그리고 수분 함량이 $CO_2$의 흡수에 의한 이온성액체의 부피팽창에 미치는 영향을 실험적으로 조사하였다. 부피팽창은 긴 양이온 알킬그룹을 가지고 있는 이온성액체 및 음이온 극성이 작은 이온성액체에서 크게 나타났다. 수분함량이 적을수록, 온도가 낮을수록, 그리고 압력이 높을수록 이온성액체상의 부피는 더 크게 나타났다.

• 한국분무공학회지
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• 제23권4호
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• pp.227-233
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• 2018

An automobile is composed of a combination of a lot of parts, and it is difficult to maintain the same performance from a new car until it's scrapped. Greenhouse gases included in automobile emissions are typically carbon dioxide and methane. It is expected that this greenhouse gas will change depending on the aging (cumulative mileage) of the automobile However, the greenhouse gas characteristics by cumulative mileage lack of actual data due to time and economic difficulties. Therefore, in this paper, we selected automobile with high sales by displacement in korea and carbon dioxide and methane were measured by using method of the related law. The cumulative mileage is as follows; within 160 km (Statutory mileage by 2010), 6500 km (current statutory mileage), 15000 km (approximately 1-year average mileage of Non-business passenger vehicle). As a result of the test, the emission of carbon dioxide and methane was the smallest at 6,500 km, and increased in order of 15000 km, within 160 km. Also, it was confirmed that the $CO_2$ emission change of a large displacement automobile is more smaller at each mileage. Although the greenhouse gas tends to increase as the mileage of the vehicle, it is thought that additional confirmation is required of since 15,000 km as well, because it can occur deviations due to taming process or mechanical friction of the automobile.

• Bulletin of the Korean Chemical Society
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• 제19권12호
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• pp.1351-1355
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• 1998

A simple apparatus for adding a modifying solvent to supercritical CO2 extractant was described. Small, fixed volumes (typically 100 μL) of liquid modifying solvents were delivered during the extraction process by use of an in-line high pressure loop injector and an air pump. Without disconnecting the extraction cell from the supercritical fluid extraction system, the modifying solvent was repeatedly delivered. The solvent modification device was optimized during the extraction of carbaryl and bis(acetylacetonato) copper(Ⅱ). Extraction recoveries from spiked filter paper and soil samples ranged between 22% and 109%, depending on the analyte and matrix components. The addition of polar modifying solvents were necessary to improve the extractability of the nonpolar CO2.

• Korean Chemical Engineering Research
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• 제53권5호
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• pp.557-564
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• 2015

기존의 초임계 이산화탄소를 이용하여 식각 및 건조하는 공정은 고압 건조기 외부에서 용매를 이용하여 웨이퍼를 식각한 후 고압 건조기로 이동시켜 초임계 이산화탄소를 이용하여 세정 및 건조 하는 2단계 공정으로 구성되어 있다. 이 공정을 이용하여 본 연구에서 실험을 수행한 결과 점착 없이 식각, 세정 및 건조가 가능함은 확인되었지만, 반복 실험 결과 재현성이 떨어지는 것을 확인하였다. 이것은 외부에서 식각한 후 건조기로 이동할 때 식각용 용매가 기화하여 구조물이 점착되는 문제가 발생하기 때문이었다. 본 연구에서는 이 문제를 개선하기 위하여 웨이퍼를 이동시키지 않고, 고압 건조기 내에서 초임계 이산화탄소를 이용하여 미세전자기계시스템 웨이퍼의 식각, 세정 및 건조공정을 연속적으로 수행하고자 하였다. 또한, 연속공정 수행 시 식각 공정에서 사용하는 이산화탄소의 상태(기체, 액체, 초임계상태)에 따른 영향을 알아보고자 하였다. 기체 이산화탄소를 이용하여 식각하는 경우(3 MPa, $25^{\circ}C$)에는 점착 없는 식각, 세정 및 건조를 할 수 있었고 반복 실험을 통하여 공정의 최적화 및 재현성을 확인하였다. 또한 기존의 2단계로 이루어진 공정에 비해 세정용 용매의 양을 절감 할 수 있었다. 액체 이산화탄소를 이용하여 식각하는 경우(3 MPa, $5^{\circ}C$) 액체 이산화탄소와 식각용 공 용매(아세톤)간의 층 분리가 일어나 완전한 식각이 이루어지지 않았다. 초임계 이산화탄소를 이용하여 식각 하는 경우(7.5 MPa, $40^{\circ}C$) 점착 없는 식각, 세정 및 건조를 할 수 있었고 기존 2단계 공정에 비해 세정용 용매의 절감 뿐 아니라 기체 이산화탄소를 이용한 연속공정에 비하여 공정시간도 단축시킬 수 있었다.

• 청정기술
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• 제14권2호
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• pp.110-116
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• 2008

원자력산업이 발생하는 방사성폐기물은 고체, 액체 그리고 기체상으로 구분된다. 특히 기체상 방사성폐기물인 방사성 메틸요오드는 활성탄을 이용하여 흡착된다. 이때 활성탄에는 방사성 메틸요오드를 보다 효율적으로 포집하기 위해 5 wt%의 트리에틸렌다이아민 (Trietylenediamine; 1,4-diazania-bicycle[2.2.2]octane, TEDA)이 첨착되어 있다. 일반적으로 대기중에서 TEDA와 메틸요오드($CH_3I$)는 I-TEDA(TEDA와 메틸요오드 결합물)를 형성하게 된다. 방사성 요오드를 포집한 방사성 폐 활성탄을 재사용하기 위해서는, 이러한 형태의 I-TEDA를 제거해야 하는데, 현재는 아세토나이트릴을 이용한 습식재활용법이 개발되었다. 그러나 이러한 습식재활용법은 다량의 2차폐기물을 발생하는 문제점이 있기 때문에, 본 연구에서는 I-TEDA를 제거하기 위한 방법으로 초임계이산화탄소를 기본용매로써 사용하였으며, 수정미량저울(Quartz Crystal Microbalance, QCM)을 이용하여 I-TEDA의 제거율을 측정하였다. 실험결과 I-TEDA를 제거하기 위해 추출을 위한 첨가용액으로 메탄올이 가장 적합하였고, 최적화된 온도, 압력 및 추출용매의 유량조건을 찾아내었다. 이러한 결과를 바탕으로 하여 방사성 폐활성탄으로부터 I-TEDA를 제거할 수 있는 가능성에 대한 검토를 하였다.

• Membrane and Water Treatment
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• 제7권5호
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• pp.463-476
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• 2016

In this study, application of polypropylene hollow fiber membrane contactors for $CO_2$ removal from water in liquid-liquid extraction (LLE) mode was simulated. For this purpose, a steady state 2D mathematical model was developed. In this model axial and radial diffusion was considered to $CO_2$ permeation through the hollow fibers. $CO_2$ laden water is fed at a constant flow rate into the lumen side, permeated through the pores of membrane and at the end of this process, $CO_2$ solution in the lumen side was extracted by means of aqueous diethanolamine (DEA) and chemical reaction. The simulation results were validated with the experimental data and it was found a good agreement between them, which confirmed the reliability of the proposed model. Both simulation and experimental results confirmed the reduction in the percentage of $CO_2$ removal by increment of feed flow rate.

• 한국응용과학기술학회지
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• 제30권4호
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• pp.770-778
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• 2013

In this study, a liquid carbonation method was applied for producing precipitate calcium carbonate by liquid-liquid reaction. We recycled the recycling water of ready-mixed concrete, one of construction waste for use source of carbonate ion. A supernatant separated from the recycling water of ready-mixed concrete, as a result of ICP analysis of a cation, $Ca^{2+}$ was contained up to 1100 ppm. We used MEA as a $CO_2$ absorbent for the liquid carbonation. A precipitate $CaCO_3$ was produced at more than MEA 20 wt%. The precipitate $CaCO_3$ as a final product was separated and dried. The result of XRD was confirmed the generation of $CaCO_3$ to calcite structure.

• Membrane and Water Treatment
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• 제8권1호
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• pp.35-50
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• 2017

The theoretical membrane gas absorption module treatments in a hollow fiber gas-liquid membrane contactor using Happel's free surface model were obtained under countercurrent-flow operations. The analytical solutions were obtained using the separated variable method with an orthogonal expansion technique extended in power series. The $CO_2$ concentration in the liquid absorbent, total absorption rate and absorption efficiency were calculated theoretically and experimentally with the liquid absorbent flow rate, gas feed flow rate and initial $CO_2$ concentration in the gas feed as parameters. The improvements in device performance under countercurrent-flow operations to increase the absorption efficiency in a carbon dioxide and nitrogen gas feed mixture using a pure water liquid absorbent were achieved and compared with those in the concurrent-flow operation. Both good qualitative and quantitative agreements were achieved between the experimental results and theoretical predictions for countercurrent flow in a hollow fiber gas-liquid membrane contactor with accuracy of $6.62{\times}10^{-2}{\leq}E{\leq}8.98{\times}10^{-2}$.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2011년도 추계학술대회 초록집
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• pp.122.1-122.1
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• 2011

The motivation for this work was the potential of hydrophobic amino acids such as glycine, L-alanine, and L-valine to be applied as thermodynamic hydrate inhibitors (THIs). To confirm their capabilities in inhibiting the formation of gas hydrates, three-phase (liquid-hydrate-vapor) equilibrium conditions for carbon dioxide hydrate formation in the presence of 0.1 to 3.0 mol% amino acid solutions were determined in the range of 273.05 to 281.45 K and 14.1 to 35.2 bar. From quantitative analyses, the inhibiting effects of the amino acids (on a mole concentration basis) decreased in the following order: L-valine > L-alanine > glycine. The application of amino acids as THIs has several potential advantages over conventional methods. First, the environmentally friendly nature of amino acids as compared to conventional inhibitors means that damage to ecological systems and the environment could be minimized. Second, the loss of amino acids in recovery process would be considerably reduced because amino acids are non-volatile. Third, amino acids have great potential as a model system in which to investigate the inhibition mechanism on the molecular level, since the structure and chemical properties of amino acids are well understood.

• 한국재료학회지
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• 제19권5호
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• pp.270-275
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• 2009

Lotus-type porous nickel with cylindrical pores was fabricated by unidirectional solidification under an Ar gas atmosphere using the thermal decomposition method of the compounds such as sodium hydroxide, calcium hydroxide, calcium carbonate, and titanium hydride. The decomposed gas does form the pores in liquid nickel, and then, the pores become the cylindrical pores during unidirectional solidification. The decomposed particles from the compounds do play a rule on nucleation sites of the pores. The behavior of pore growth was controlled by atmosphere pressure, which can be explained by Boyle's law. The porosity and pore size decreased with increasing Ar gas pressure when the pores contain hydrogen gas decomposed from calcium and sodium hydroxide and titanium hydride, ; however it they did not change when the pores contain containing carbon dioxide decomposed from calcium carbonate. These results indicate that nickel does not have the solubility of carbon dioxide. Lotus-type porous metals can be easily fabricated by the thermal decomposition method, which is superior to the conventional fabrication method used to pressurized gas atmospheres.