• 분석과학
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• 제26권4호
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• pp.287-297
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• 2013

본 연구는 고체 흡착관과 TD-GC/MS를 이용하여 7종의 휘발성 유기화합물에 대한 열탈착 분석조건을 최적화하였고, 기체상 및 액상 표준물질 첨가한 고체 흡착관을 사용하여 얻어진 검정곡선으로부터 휘발성 유기화합물을 비교 정량하였다. 대응표본 t-검정 결과, 스타일렌을 제외하고 벤젠, 톨루엔, 에틸벤젠, o-, m- 및 p-자일렌을 포함한 6종의 휘발성 유기화합물에 대해서는 액상 표준물질에 의한 표준 흡착관법이 기체상에 의해 제작된 표준 흡착관법이 유의수준 (${\alpha}=0.01$)에서 일치한 반면, 스타일렌에 대해서는 기체상 및 액체상으로 작성된 검정곡선에서 감응인자가 15.6% 차이가 발생하였는데 이것은 두방법 간에 유의한 차이가 있다는 것을 의미하였다. 따라서 BTEX를 포함한 스타일렌을 정량하는데 오차를 감소시키기 위해 액상 표준물질을 이용한 고체상 흡착관법을 사용하였다. 바로 그 점이 이 논문의 핵심내용임. 즉, 고가의 표준가스 대신에 저가의 액상 표준물질을 사용하여 정량하더라도 스타일렌 이외에 거의 동일한 값을 나타내기 때문임. 액체상 표준물법 조건에서 7종의 VOCs의 회수율은 $100{\pm}5%$, 재현성은 0.3~7.7%, 검출한계는 o-자일렌의 $0.01{\mu}g/m^3$에서부터 톨루엔의 $0.27{\mu}g/m^3$까지 범위를 나타내었다. 이러한 최적화된 분석방법을 신축 기숙사, 원룸 아파트 및 신차의 실내공기 중 휘발성 유기화합물을 정량하는데 적용하였다.

• Environmental Engineering Research
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• 제14권1호
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• pp.26-31
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• 2009

Sorption of $Ni^{2+}$ in aqueous solution was studied using montmorillonite. The experimental and equilibrium data fitted well to the Langmuir isotherm model. From the kinetics data for nickel sorption onto montmorillonite, the diffusion of $Ni^{2+}$ inside the clay particles was the dorminant step controlling the sorption rate and as such more important for $Ni^{2+}$ sorption than the external mass transfer. $Ni^{2+}$ was sorbed due to strong interactions with the active sites of the sorbent and the sorption process tends to follow the pseudo second-order kinetics. Thermodynamic parameters (${\Delta}G^{\circ},\;{\Delta}H^{\circ},\;{\Delta}S^{\circ}$) indicated a non spontaneous and endothermic adsorption process while the positive low value of the entropy change suggests low randomness of the solid/solution interface during the uptake of $Ni^{2+}$ by montmorilionite. Heavy metals such as $Ni^{2+}$ in aqueous bodies can effectively be sorbed by montmorillonite.

• 한국산학기술학회논문지
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• 제22권4호
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• pp.17-24
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• 2021

새로운 이산화탄소 분리용 흡착제 개발은 흡착속도, 소수성, 상용 흡착제보다 낮은 재생온도 등을 고려하여야 한다. 본 연구에서는 CO2를 분리하기 위하여 아미노실란이 그라프팅된 활성탄을 합성하였다. 아민 작용기 전구체로 methyltrimethoxysilane(MTMS) and 3-Aminopropyl-triethoxysilane(APTES)을 사용하여 그라프팅하였다. APTES를 그라프팅 활성탄이 MTMS을 사용한 것보다 우수한 흡착 특성을 나타내었다. 온도 및 이산화탄소 분압에 따른 흡착 특성으로 이산화탄소 분리 메커니즘을 규명하였다. 이산화탄소의 흡수/흡착능은 25 ℃에서 아민 그라프팅 활성탄과 활성탄과 비슷하지만 아민 그라프팅 활성탄이 75 ℃에서 더 높게 나타났다. 아민 작용기 그라프팅 활성탄은 이산화탄소 분압이 1 % 인 조건에서 활성탄보다 더 우수한 흡수능을 나타내었다. 아미노실란 그라프팅 활성탄은 물리적 흡착 특성을 지닌 화학적 흡수 메카니즘을 나타내었다. 아민 작용기가 부여되어 개질된 고체상 흡수/흡착제는 이산화탄소 흡착/흡수 공정만 아닌 재료 관련 산업에 큰 영향을 미칠 수 있는 고성능 복합 재료이며, 개발된 흡착제는 흡수/흡착 및 분리 관련 산업 공정에 적용될 수 있다.

• Advances in materials Research
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• 제9권4호
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• pp.251-263
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• 2020

α-mangostin imprinted polymers have been synthesized by a non-covalent imprinting approach with α-mangostin as a template molecule. The α-mangostin molecularly imprinted polymers (MIPs) prepared by radical polymerization using methacrylic acid, ethlylene glycol dimethacrylate, benzoyl peroxide, and acetonitrile, as a monomer, crosslinker, initiator, and porogen, respectively. The template was removed by using methanol:acetic acid 90:10 (v/v). The physical characteristics of the polymers were investigated by Fourier Transform Infrared spectroscopy (FTIR), scanning electron microscopy (SEM), and thermogravimetric analysis (TGA). The rebinding studies were carried out by batch methods. The results exhibited that the MIPs was able to adsorb the α-mangostin at pH 2 and the contact time of 180 min. The kinetic adsorption data of α-mangostin performed the pseudo-second order model and followed the Langmuir isotherm model with the adsorption capacity of 16.19 mg·g-1. MIPs applied as a sorbent material in solid-phase extraction, namely molecularly imprinted solid-phase extraction (MISPE) and it shows the ability for enrichment and clean-up of α-mangostin from the complex matrix in medicinal herbal product and crude extract of mangosteen (Garcinia mangostana L.) pericarp. Both samples, respectively, which were spiked with α-mangostin gives recovery more than 90% after through by MISPE in all concentration ranges.

• 원예과학기술지
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• 제31권2호
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• pp.239-245
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• 2013

Occupational exposure and risk assessment were conducted to evaluate the safety of operators when insecticide acetamiprid was applied to apple orchard using a speed sprayer. Dermal patches, cotton gloves, socks, and masks were used to monitor the dermal exposure, and personal air pump with solid sorbent was used to measure the potential inhalation exposure. In validation to analytical methods, the limit of detection and limit of quantitation were 0.25 ng and 1 ng, respectively. Good reproducibility (coefficient variation < 4%), linearity (coefficient determination > 0.999), and recovery (85.3-118.2%) were obtained. Trapping efficiency of solid sorbent was 96.4% while breakthrough did not occur. Only hand exposure was measured on the gloves during mixing/loading to give $33-1,132{\mu}g$. Exposure amount of operator 3 among 4 workers was noticeably high. The total volumes of spray liquid for operators were $535-1,235mL{\cdot}h^{-1}$, corresponding to 0.03-0.08% of the applied spray solution. Highest contaminated parts of body were thighs, chest, and lower legs. The inhalation exposure ratio to the total application amount was significantly low. However, wind seemed to affect the inhalation exposure of operator. For risk assessment, margin of safety was calculated by the application of cloth and dermal penetration rate to obtain values of much larger than 1 in all cases. Therefore, health risk of operators during treatment of acetamiprid in apple orchard could be of least possibility.

• 한국산업보건학회지
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• 제9권1호
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• pp.173-186
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• 1999

To utilize diffuse sampling of formaldehyde in air, a new sampler was designed. A glass fiber filter was impegnated with 2,4-dinitrophenylhydrazine(DNP) and phosphoric acid and mounted 37mm cassette. The formaldehyde vapor was sampled in the dynamic chamber and measured by high performance liquid chromatograph and compared with solid sorbent tube. The results were as follows ; 1. The desorption efficiencies of diffusive sampler between 97.0% and 100%. 2. the sampling rate is constant as in $58{\sim}61.8m{\ell}/min$ when sampling times are between 120 and 360 min. 3. There was a significant relationship between concentrations of diffusive samples and active samples with the coefficient of determination(R2) of 0.92. 4. Desorbed amount of formaldehyde diffusive sampler was increased by high relative humidity. 5. Wheth diffusive samplers were stored at room temperature or at refrigerator there was no statistically significant difference in the accuracy of result. 6. When the diffusive samplers, which collected formaldehyde vapor, were exposed to clean air for three hours, there was no significant loss of formaldehyde due to reverse diffusion. In conclusion, this study suggest that developed diffusive samplers will be a reasonable substitute for the solid sorbent tube for sampling formaldehyde and practical comparative study of developed diffusive sampler should be performed at workplaces of manufacturing industry.

• KEPCO Journal on Electric Power and Energy
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• 제1권1호
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• pp.115-120
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• 2015

$K_2CO_3$-based dry regenerable sorbents were prepared by spray-drying techniques to improve mass produced $K_2CO_3-Al_2O_3$ sorbents (KEP-CO2P, hereafter), and then tested for their $CO_2$ sorption capacity by a $2,000Nm^3/h$ (0.5 MWe) $CO_2$ capture pilot plant built for Unit 3 of the Hadong thermal power station in 2010. Each of the sample sorbents contained 35 wt.% $K_2CO_3$ as the active materials with various support materials such as $TiO_2$, MgO, Zeolite 13X, $Al_2O_3$, $SiO_2$ and hydrotalcite (HTC). Their physical properties and reactivity were tested to evaluate their applicability to a fluidized-bed or fast transport-bed $CO_2$ capture process. The $CO_2$ sorption capacity and percentage utilization of $K_2CO_3$-MgO based sorbent, Sorb-KM2, was $8.6g-CO_2/100g$-sorbents and 90%, respectively, along with good mechanical strength for fluidized-bed application. Sorbs-KM2 and KT were almost completely regenerated at $140^{\circ}C$. No degradation of Sorb-KM by $SO_2$ added as a pollutant in flue gas was observed during a cycle test.

• 약학회지
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• 제32권1호
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• pp.6-13
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• 1988

A gas chromatographic method is described for the determination of volatile free acids(VFAs) in body fluids. VFAs were trace enriched from body fluids by liquid-solid extraction using Chromosorb P as the solid sorbent and ether as the eluant. The enriched VFAs were injected in splitless injection mode onto a HP-20M fused silica capillary column. The flame ionization detector was used as the detector. The present method was applied to the profiling of VFAs in body fluids from patients suffering from the infectious disease, hepatitis. The VFAs concentrations were high in saliva of hepatitis patients and isobutyric acid detected in sera of hepatitis patients compared to healthy subjects.

• Bulletin of the Korean Chemical Society
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• 제31권12호
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• pp.3755-3759
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• 2010

A on-line SPE (solid phase extraction)-HPLC preconcentration method was developed for the determination of phenolic compounds at trace levels in environmental water sample. XAD-4 and Dowex 1-X8 were used as sorbent in the on-line SPE-HPLC method for the selective enrichment of nine phenolic compounds, which are included in the priority pollutants list of the US EPA. Also alumina prefiltering considerably reduced the amount of interfering peaks due to humic substances that could accumulated due to the preconcentration step and prevent quantification of polar phenolic compounds in environmental water samples. This method was used to determine the phenolic compounds in tap and river water and superiority to the US EPA 625 method in its enrichment factor, pretreatment time, recoveries, and detection limit. The limits of detection were in the range of $0.3-0.9\;{\mu}g/L$ in tap water sample.

• Korean Chemical Engineering Research
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• 제50권3호
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• pp.492-498
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• 2012

본 연구에서는 고온고압 건식탈황장치를 이용하여 고체순환량과 탈황반응기 내의 공극률에 대한 수력학적특성을 파악하고, 아연계 탈황제의 고온고압 조건에서 탈황반응온도에 대한 반응특성 및 연속운전을 통한 탈황 효율을 분석하였다. 실험에 사용된 고온고압건식탈황장치는 고속유동층 형태의 탈황반응기(내경: 0.015 m, 높이: 6.2 m), 기포유동층 형태의 재생반응기(내경: 0.053 m, 높이: 1.6 m), 가스의 역흐름을 방지하는 loop-seal, 두 반응기 후단에 압력컨트롤밸브로 구성되어있다. 수력학 특성으로는 고체순환밸브 개구비, 탈황반응기 가스 유속, 탈황반응기 온도 변화에 따른 고체순환량과 각 조건에서의 고속유동층 형태의 탈황반응기 높이에 따른 공극률 분포를 알아보았다. 고체순환량은 동일한 유속조건, 동일한 고체순환밸브 개구비에서 탈황반응기 온도가 상온일 때보다 $300^{\circ}C$와 $550^{\circ}C$일 때 감소하였으며 $300^{\circ}C$와 $550^{\circ}C$ 조건에서는 큰 차이가 없었다. 탈황반응기내의 공극률은 고체순환밸브 개구비가 10~20%로 고체순환량이 적은 경우 고속유동층 형태의 공극률 분포를 보이고, 30~40%로 고체순환량이 많아지는 경우 탈황반응기 하부에서 turbulent 형태의 공극률의 분포를 나타냈다. 아연계 탈황제의 탈황반응온도에 따른 반응특성은 시스템 압력 20 atm, 연속 반응 조건에서 탈황 온도를 변화시키면서 살펴보았다. 일정한 고체순환 조건에서 탈황온도 $450^{\circ}C$ 이하에서 탈황 효율 저하가 시작되는 것을 확인하였으며, 높은 탈황 효율을 유지시키기 위하여 10시간 연속운전에서는 탈황 반응 온도를 $500^{\circ}C$로 설정하여 실험하였다. 실험 결과, 10시간 연속운전을 통해, 유입 $H_2S$ 농도 5,000 ppmv 조건에서 탈황 반응기 후단 $H_2S$ 농도는 UV분석기(Radas2)와 검지관(GASTEC)의 검출한계인 1 ppmv 이하를 유지하여 $H_2S$ 제거 효율 99.99% 이상을 달성하였다.