http://chineseinput.net/에서 pinyin(병음)방식으로 중국어를 변환할 수 있습니다.
변환된 중국어를 복사하여 사용하시면 됩니다.
여수석유화학산단 산업폐수 재이용을 위한 블로우 다운 (Blow Down)수 발생현황 조사
권태옥 ( Tae Ouk Kwon ),문일식 ( Il Shik Moon ) 한국물환경학회 2005 한국물환경학회지 Vol.21 No.3
Purpose of this research is to quantitatively and qualitatively investigate the blow down wastewater produced from Yeosu Industrial Complex. Approximately, 38,325,000 tons/year of wastewater is produced, processed and finally discharged. Six representative companies, namely, A, B, C, D, E, F were chosen for this study. Each company produce over 5,000 tons/day of wastewater. In total, 6,844 tons/day of blow down water is produced from these six companies, put together. However, companies A and C produce about 24% and 37% of blow down water, respectively. It was found that the blow down water had favorable qualities, except for its high conductivity, ranging from 230 to 1,700 μs/㎝. It was evident that, this water can be suitable for reuse, for industrial purposes, if a suitable treatment, for example, RO membrane process is adopted to remove high conductivity.
UV, H<sub>2</sub>O<sub>2</sub>, 오존을 이용한 고급산화공정에서의 테레프탈산 제조공정 폐수 처리 : 유기물 및 색도제거 연구
권태옥,박보배,문일식,Kwon, Tae-Ouk,Park, Bo-Bae,Moon, Il-Shik 한국화학공학회 2007 Korean Chemical Engineering Research(HWAHAK KONGHA Vol. No.
UV/H_2O_2$, $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ 공정을 이용한 테레프탈산 제조공정 폐수의 COD 및 색도제거 연구를 수행하였다. UV/H_2O_2$, $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ 공정에서의 COD 제거율은 각각 10, 48, 56, 63%, 색도 제거율은 $UV/H_2O_2$ 공정이 80%, $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ 공정은 모두 99% 이상 효과적으로 제거되는 것으로 나타났다. COD 및 색도 제거율이 가장 우수한 $UV/H_2O_2/O_3$ 공정에서 테레프탈산 제조공정 폐수의 주요 유기물 성분인 테레프탈산, 이소프탈산 그리고 벤조산 성분은 120분 이내에 모두 99% 이상 제거되었다. 또한 $UV/H_2O_2$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ 공정에서의 최적 $H_2O_2$ 주입농도는 각각 0.5M, 25 mM 그리고 5 mM로 나타나, UV와 $H_2O_2$를 오존산화 공정에 조합함으로써 유기물 제거율 향상과 함께 사용된 $H_2O_2$의 저감효과를 동시에 얻을 수 있었다. UV/H_2O_2$, $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ processes were tested for the removal of COD and color from terephthalic acid wastewater. COD removal efficiencies were 10, 48, 56, 63% in the $UV/H_2O_2$, $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ process respectively. Color removal efficiency of $UV/H_2O_2$ process was 80% and $O_3$, $O_3/H_2O_2$, $UV/H_2O_2/O_3$ processes were almost more than 99%. Terephthalic acid, isophthalic acid and benzoic acid were completely destructed in terephthalic wastewater within 120 min by $UV/H_2O_2/O_3$ process and shows high COD and color removal efficiencies. The optimum concentration of $H_2O_2$ dosage was found to be 0.5 M, 25 mM and 5 mM for $UV/H_2O_2$, $O_3/H_2O_2$ and $UV/H_2O_2/O_3$ processes respectively, Organic destruction efficiency was enhanced and also reducing the consumption of $H_2O_2$ dosage by combining UV, $H_2O_2$ and $O_3$ process.