해수에 유출된 유류는 대기와 해수와의 접촉을 통해 다양한 풍화 과정(증발, 확산, 분산, 유화, 용해, 산화, 침전 및 생물분 해 등)을 통해 물리·화학적 변화와 함께 생물학적 분해과정을 겪는다. 본 연구에서는 여러 가지 풍화작용 중 가장 즉각적이고 빠르며 오염물질의 질량에 가장 큰 영향을 미치는 인자라고 알려진 증발(evaporation)에 대한 영향을 확인해보고자 하였다. 휘발유, 등유, 경유 를 대상으로 25 ℃(해수 연평균 온도)와 35℃(적도 부근 온도) 조건에서 유류의 휘발특성을 비교하였다. 이를 위해, 일정 기간마다 채취 한 유류를 전처리하여 GC/MS 분석을 수행하고, 탄화수소의 변화량을 계산하여 비교하였다.

In order to prepare the information needed to construct a reduction system for volatile organic compounds (VOCs) exhausted from ship-block paint-booths in a giant shipyard, VOCs in paint-shop airs were analyzed and compared to the components in paint thinners. Aromatic hydrocarbons containing eight and nine carbon atoms are known to be major VOC compounds found in shipyard paint-shops. The total hydrocarbon (THC(C7)) concentrations calibrated using toluene gas, were measured in block paint-shops with two photo-ionization detector (PID) meters, and the resulting THC(C7) data were converted to THC(C1) concentrations according to the Standard Methods for the Measurements of Air Pollution in South Korea. THC(C1) concentrations near the spray site ranged from 10 to 2,000 ppm, but they were less than 400 ppm near the walls of the paint-booth. The measurements of THC concentrations, based on the height of the monitoring sites, were related to the height of the target to which the spray paints were applied. The maximum concentrations occurred at almost the same height as the spray targets. When painted blocks had been dried-by warming with no spraying, the THC concentrations were 80~100 ppm.

In this study, the thermo-catalytic hydrogenation using corn stark and wasted palm kernel shell was carried out for the production of hydrocarbon compounds in direct biomass liquefaction. The conversion of biomass in direct biomass liquefaction over Mo-based catalyst increased with increasing the reaction temperature and the content of the volatile matter contained in biomass and the corn starch was more available than the wasted palm kernel shell. And then, the conversion was about 97.9% using corn starch and was about 92.4% using wasted palm kernel shell at 400oC. It was confirmed that the liquefied products obtained after the thermo-catalytic reaction were C6, C7, C8-typed hydrocarbon compounds.