• 환경위생공학
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• 제17권3호
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• pp.99-109
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• 2002

Charcoal $tube/CS_2$ method are more popularly used than any other in the measurement of the working environment for the exposure evaluation of organic solvent, but it is some weak points that the lower accuracy can be obtained on the polar materials and within the range of the low concentration. Thus solvent desorption method has been developed to make accuracy higher and to overcome some weak points. However, because of high price of adsorption tube for thermal desorption and the short of study on its application to the working environment, it is not popularly used in the domestic industrial hygiene fields. This dissertation aims to develop thermal desorption and adsorption tubes for measuring organic solvents in the working environment, by comparing and analyzing breakthrough condition and adsorption capacity with ACF. Specific surface area of ACF used in this study is wider than the one of AC and micropore of ACF related with adsorption has been developed, and adsorption velocity and adsorption amount are very excellent by linking a pore of surface and an inside well into micropore. 1. Result of analysis on physical characteristics of adsorbent, the specific surface area of ACF was 1.3 times higher than that of AC. Distribution ratio of micropore related to adsorption was 94% on ACF and AC. Result of SEM, micropore of the AC is opened to the surface. In contrast, ACF shows that extremely fast adsorption speed. Because of micropore are exposed on the surface and penetrate through each other. 2. Breakthrough characteristics of adsorbents was not different from slop of breakthrough curve. The effluent concentration reaches 10% of initial concentration($C_{out}/C_{in}=0.1$, break point) of ACF was 30~316min longer than that of AC. Therefore, the adsorption capacities of ACF was 1.1~4.6 times higher than that of AC. ACF can be used as a proper adsorbent for measurement of organic solvent.

• 공업화학
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• 제19권4호
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• pp.445-451
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• 2008

마이크로파를 이용하여 휘발성유기화합물(VOCs; Volatile Organic Compounds)로 오염된 활성탄을 재생하기 위하여, 절연물질로서 활석(Talc)과 Ni-Zn ferrite를 각각 활성탄에 코팅하여 벤젠의 흡착 및 탈착 특성을 조사하였다. 절연물질이 코팅된 활성탄의 물리적 특성 및 표면상태는 질소가스 흡착장치와 주사전자현미경(SEM)을 이용하여 각각 확인하였다. 비표면적과 벤젠에 대한 흡착량은 비례관계를 보였고, 활성탄에 활석이나 Ni-Zn ferrite를 코팅하면 마이크로파에 의한 불꽃방전을 억제할 수 있었다. 활성탄에 절연물질을 코팅하기 위해 사용한 바인더는 PS (potassium silicate)가 벤젠에 대한 흡착성능이 가장 우수한 것으로 나타났다. 마이크로파 출력에 따른 탈착량은 출력에 비례하는 경향을 보였고, 연속되는 흡착과 탈착과정이 5회 반복되더라도 재현성이 충분히 나타났다. 결과적으로 VOCs로 오염된 폐활성탄의 재생방법으로서, PS를 바인더로 사용하여 활석이나 Ni-Zn ferrite를 활성탄에 코팅하여 마이크로파로 탈착시키면 효과적임을 알 수 있었다.

• 한국자동차공학회논문집
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• 제14권3호
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• pp.125-132
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• 2006

Transient kinetics of $NH_3$ adsorption/desorption and of SCR(selective catalytic reduction) of NO with $NH_3$ were studied over vanadium based catalysts, such as $V_2O_5/TiO_2$ and $V_2O_5-WO_3/TiO_2$. In the present catalytic reaction process, NO adsorption is neglected while $NH_3$ is strongly chemisorbed on the catalytic surface. Accordingly, it is ruled out the possibility of a reaction between strongly adsorbed $NH_3$ and NO species in line with the hypothesis of an Eley-Rideal mechanism. The present kinetic model assumes; (1) non-activated $NH_3$ adsorption, (2) Temkin-type $NH_3$ coverage dependence of the desorption energy, (3) non-linear dependence of the SCR reaction rate on the $NH_3$ surface coverage. Thus, the surface heterogeneity for adsorption/desorption of $NH_3$ is taken into account in this model. The present study extends the pure chemical kinetic model based on a powdered-phase catalytic system to the chemico-physical one applicable to a realistic monolith reactor.

• 한국지하수토양환경학회지:지하수토양환경
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• 제17권4호
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• pp.36-43
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• 2012

Various methods are used to remediate soil contaminated with heavy metals or petroleum. In recent years, harsh physical and chemical remediation methods are being used to increase remediation efficiency, however, such processes could affect soil properties and degrade the ecological functions of the soil. Effects of soil washing, thermal desorption, and land farming, which are the most frequently used remediation methods, on the physicochemical properties of remediated soil were investigated in this study. For soils smaller than 2 mm, the soil texture were changed from sandy clay loam to sandy loam because of the decrease in the clay content after soil washing, and from loamy sand to sandy loam because of the decrease in the sand content and increase in silt content during thermal desorption, however, the soil texture remained unchanged after land farming process. The water-holding capacity, organic matter content, and total nitrogen concentration of the tested soil decreased after soil washing. A change in soil color and an increase in the available phosphate concentration were observed after thermal desorption. Exchangeable cations, total nitrogen, and available phosphate concentration were found to decrease after land farming; these components were probably used by microorganisms during as well as after the land farming process because microbial processes remain active even after land farming. A study of these changes can provide information useful for the reuse of remediated soil. However, it is insufficient to assess only soil physicochemical properties from the viewpoint of the reuse of remediated soil. Potential risks and ecological functions of remediated soil should also be considered to realize sustainable soil use.

• 한국지하수토양환경학회지:지하수토양환경
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• 제20권5호
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• pp.41-46
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• 2015

Three types of experiments, based on the physical properties of oily sludge landfilled soil, were conducted to recover total petroleum hydrocarbons (TPH) from the soil. These experiments included gravity separation, solvent extraction using water, and air floatation. The oil portion was not easily separated from the wet (raw) soil because water molecules aggregate the soil particles, despite the fact that the soil was sandy. However, the drying and grinding processes destroyed the aggregates, causing the TPH recovery to increase to approximately 60% when air floatation was used. The drying process decreased the specific gravity of the soil sample, thereby enhancing the overall recovery of TPH from the soil. Although thermal desorption and/or incineration are common choices for heavily dumped sites, physical separation can recover the oil portion instead of simply removing it.

• 한국철도학회:학술대회논문집
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• 한국철도학회 2007년도 추계학술대회 논문집
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• pp.1386-1391
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• 2007

The ballast gravels are often contaminated by various pollutants, like diesel fuel, lubricants, and heavy metals. Especially, the gravels near the switching are apt to be polluted by the lubricant. Because this lubricant can pollute the soil of track, the contaminated ballast gravels should be cleaned immediately. In this study, a physical desorption method was used to remove the oil contaminants from the surface of the ballast gravels. Thermosetting resin was used as a media for physical remediation of ballast gravels. The total petroleum hydrocarbon of the gravels was monitored over time. In addition, scanning electron microscopic images were obtained to observe the removal of the oily pollutants from the surface of the gravels.

• Journal of Information Display
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• 제2권3호
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• pp.44-47
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• 2001

The extracted field emission current can be used to controllably heat microfabricated cold field emission cathode tips. The heating can be sufficient to smooth and recrystallize the tip surface by surface self-diffusion, and at least partially clean the surface of contaminants by thermal desorption. Self-heating not only allows for the achievement and maintenance of stable emission characteristics, but can be used to make the current-voltage characteristics of microfabricated field emitter tips nearly identical to one another. The resulting improvement in emission uniformity will allow for more reliable array operation at increased electron emission current densities.

• 폴리머
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• 제25권1호
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• pp.115-121
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• 2001

수평균 중합도 10000 및 신디오탁틱 다이애드기 함량 61.5%의 고분자량 신디오탁틱 폴리비닐알코올(high molecular weight syndiotactic poly(vinyl alcohol) (HMW s-PVA))/요오드계 편광필름을 제조하고 이의 흡착 거동 및 열수 하에서의 요오드의 내구성을 고찰하였다. 아탁틱 PVA 및 저분자량 s-PVA/요오드계 필름과 비교할 때 열수하에서의 HMW s-PVA 필름의 용해도 및 HMW s-PVA/요오드계 필름의 요오드 탈착은 현저히 억제되었다. 요오드 침지시간이 길어질수록 열수하에서의 요오드 탈착현상이 점차 심화되었다. 이는 처리 시간이 길어짐에 따라 PVA 분자와 요오드 분자간에 안정한 복합체가 형성되기보다는 물리적인 흡착에 의하여 흡착량이 증가하였기 때문이라고 설명된다.

• 공업화학
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• 제18권6호
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• pp.592-598
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• 2007

Temperature programmed desorption (TPD), XRD, SEM 및 FT-IR를 이용하여 코발트 프탈로시아닌 유도체의 황과 아민화합물에 대한 흡착효율을 조사하였다. 코발트 프탈로시아닌 유도체의 암모니아에 대한 TPD 측정결과, 산도가 낮은 온도($100{\sim}150^{\circ}C$)와 높은 온도($350{\sim}400^{\circ}C$)에서 두개의 탈착피크가 나타났다. 테트라카르복실 코발트프탈로시아닌(Co-TCPC)은 코발트 프탈로시아닌(Co-PC)보다 낮은 온도(물리적 흡착)에서 탈착피크가 약했지만 높은 온도(화학적 흡착)에서 강한 탈착피크가 나타났다. Co-TCPC와 Co-PC의 비표면적은 각각 37.5와 $18.4m^2/g$이었다. Co-TCPC와 Co-PC의 기공부피는 각각 0.17과 $0.10cm^3/g$이었다. 파과곡선으로부터 흡착용량을 계산하였더니 트리에틸 아민 가스 120 ppm의 평형농도에서 Co-TCPC의 흡착용량은 24.3 mmol/g, Co-PC의 흡착용량은 0.8 mmol/g로 나타났다. Co-TCPC와 Co-PC로 디메틸 술파이드 제거효율은 디메틸 술파이드 초기농도 225 ppm에서 각각 92와 18% 제거효율을 보였다. Co-TCPC와 Co-PC로 트리메틸아민 제거효율은 트리메틸아민 초기농도 118 ppm에서 각각 100.0%와 17.0% 제거효율을 보였다.

• Biotechnology and Bioprocess Engineering:BBE
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• 제2권2호
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• pp.126-131
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• 1997

The biosorption and desorption of Cr, Cu and Al were carried out using brown marine algae Sargassum fluitans biomass, known as the good biosorbent of heavy metals. The content of alginate bound to light metals could be changed by physical and chemical pretreatment. The maximum uptake of Cr, Cu and Al was independent of the alginate content. The maximum uptaker of Al was two times(mole basis) than those of Cu and Cr. The aluminum-alginate complex was found in the sorption solution of raw and protonated biomass. Most of Cu, Al and light metals sorbed in the biomass were eluted at pH 1.1. However, only 5 to 10% of Cr sorbed was eluted at pH 1.1. The stoiceometric ion exchange between Cu and Ca ion was observed on Cu biosorption with Ca-loaded biomass. A part of Cr ion was bound to biomass as Cr(OH)2+ or Cr(OH)2+. Al was also bound to biomass as multi-valence ion and interfered with the desorbed Ca ion. The behavior of raw S. fluitans in ten consecutive sorption-desorption cycles has been investigated in a packed bed flow-through-column during a continuous removal of copper from a 35 mg/L aqueous solution at pH 5. The eluant used was a 1%(w/v) CaCl2/HC solution at pH 3.