• 한국대기환경학회지
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• 제26권5호
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• pp.517-532
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• 2010

After establishment of Banwol industrial complex in 1987, Ansan city becomes the largest industrial sector development in Gyeonggi-do, Korea. As the population and industrial activity grow over this region, toxic air pollutants, particularly POPs (Persistent Organic Pollutants) from various emission sources have been major public concerns. Air samples for POPs monitoring were collected at the industrial sites ($A_2$), residential sites ($B_1$, $B_2$), commercial site (C), and rural/remote site (D) of the area of Ansan during 2008 with a prolonged industrial sampling site $A_1$ from 2001 to 2008. All samples were analysed for 2,3,7,8 substituted-polychlorinated dibenzo-p-dioxin and dibenzofurans (PCDD/Fs) and dioxin like polychlorinatd diphenyls (dl-PCBs). In site $A_1$, a steady decline of their concentrations from 2003 to 2008 was observed due to the reinforced emission guideline from waste incinerators. The average concentration of the PCDD/Fs and dl-PCBs ranged between 0.118 pg-TEQ/$m^3$ (rural/remote site D) and 0.532 pg-TEQ/$m^3$ (industrial area $A_2$). These level were generally consistent with previous studies in Gyeonggi-do, while higher than other places. Most of PCDD/Fs congener were partitioned into particle phase, whereas dl-PCBs were partitioned into gas phase. The logarithm of gas-particle partition coefficient $K_P$ of dl-PCBs and PCDD/Fs were well correlated with sub-cooled liquid vapor pressure $P_L$. The slope $m_T$ of log $K_P$ versus log $P_L$ for PCDD/Fs (-1.22) and dl-PCBs (-1.02) in industrial area ($A_2$) were high compared to other residential/commercial area. It suggests that this area was likely influenced by the direct emission source of PCDD/Fs and dl-PCBs. To simulate the partition of PCDD/Fs and dl-PCBs between gas and particle phase, Junge-Pankow model ($P_L$-base) and $K_{oa}$ model were applied. It was found that J-P model was more suitable than the $K_{oa}$ model in this study.

• 한국산학기술학회논문지
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• 제19권6호
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• pp.88-97
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• 2018

압력변환 증류공정(Pressure-Swing Distillation, PSD)을 통해서 1-프로판올과 벤젠 이성분계 혼합물의 분리공정에 대한 전산모사 및 공정 최적화를 수행하였다. Schneider Electric사의 PRO/II with PROVISION V10.0을 사용하였으며, 열역학 모델식으로는 NRTL 액체 활동도계수 모델식을 적용하였다. 고압에서 저압 증류탑 배열 공정과 저압에서 고압 증류탑 배열공정에 대한 재비기의 총 heat duty의 소모량의 합을 서로 비교하였다. 유틸리티 소모량을 최소화하기 위해서 각 공정의 저압 증류탑과 고압 증류탑 상부 벤젠의 조성, 이론단수와 원료 주입단의 위치를 최적화하였으며, 각각의 증류탑의 환류비를 조절하였다. 공정 최적화 수행결과, 총 재비기 heat duty 값은 각각 고압에서 저압 증류탑 배열 공정의 경우 $3.10{\times}10^6kcal/h$ 이었으며, 저압에서 고압 증류탑 배열 공정의 경우 $2.75{\times}10^6kcal/h$로 나타났다. 또한, 저압-고압 증류탑 배열 공정에 열통합 공정(heat integration)을 적용한 경우 재비기의 총 heat duty 값이 고압-저압 증류탑 배열 공정에 비해서 약 57.36%정도 적게 추산되었다.