• 한국환경과학회지
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• 제16권1호
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• pp.1-8
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• 2007

Atmospheric photochemistry of $O_3-NOx-RH$ were considered theoretically, to clarify the reasons for the different trends of between the formation of photochemical oxidants (Ox) and its primary pollutants for the Low-and High-NOx regimes. Equations of OH, $HO_2$, and production of ozone ($O_3$) as a function of nitrogen oxides (NOx) and reactive hydrocarbons (RH) were represented in this study. For the Low-NOx regime, $HO_2$ radical is proportional to RH but independent of NOx. OH radical is proportional to NOx but inversely-proportional to RH. $O_3$ production is proportional to NOx but has a weak dependence on RH. For the High-NOx regime, OH and $HO_2$ radicals concentrations and $O_3$ production are proportional to RH but inversely-proportional to NOx. In addition, the Osaka Bay and surrounding areas of Japan were evaluated with the mass balance of odd-hydrogen radicals (Odd-H) using CBM-IV photochemical mechanism, in order to distinguish the Low- and High-NOx regimes. The Harima area (emission ratio, RH/NOx = 6.1) was classified to the Low-NOx regime. The Hanshin area (RH/NOx = 3.5) and Osaka area (RH/NOx = 4.3) were classified to the High-NOx regime.

• 한국환경보건학회지
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• 제31권4호
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• pp.260-265
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• 2005

Indoor air quality might be affected by source strength of indoor pollutants, ventilation rate, decay rate, outdoor level, and so on. Although technologies measuring these factors exist directly, direct measurements of all factors are not always practical in most field studies. The purpose of this study was to develop an alternative method to estimate the source strength and deposition constant by application of multiple measurements. For the total duration of 60 days, indoor and outdoor $NO_2$ concentrations every 3 days were measured in 30 houses in Seoul, Asan and Daegu. Using a compartment model by mass balance and linear regression analysis, penetration factor (ventilation divided by sum of air exchange rate and deposition constant) and source strength factor (emission rate divided by sum of air exchange rate and deposition constant) were calculated. Subsequently, the source strength and deposition constant were estimated. Natural ventilation was $1.80{\pm}0.42\;ACH,\;1.11{\pm}0.50\;ACH,\;0.92{\pm}0.26\;ACH$ in Seoul, Asan and Daegu, respectively. Calculated deposition constant(K) and source strength of $NO_2,$ in this study were $0.98{\pm}0.28\;hr^{1}\;and\;16.28{\pm}7.47\;ppb/h,$ respectively.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1993년도 Proceedings of International Conference for Agricultural Machinery and Process Engineering
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• pp.443-452
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• 1993

Direct freezing tests of soybean seed by liquid nitrogen were carried out at various moisture contents and the following important conclusions were drawn from the results of temperature measurements of soybean seed and photographs of bubbles generated on its surface : 1) Assuming that the temperature gradient in a soybean seed is negligible because of its small seed size and the freezing ratio is followed the Heiss's formula, and a differential equation based on the heat energy balance was introduced . The equation was easily solved by the Runge-Kutta-Gill method and the predicted values of the temperature were in good agreement with the observed data. 2) The photographs of bubble generation during freezing showed the boiling mode was nucleate, and then the most suitable formula on the nucleate boiling heat transfer was introduced from many formulate proposed up to now by fitting the calculated values based on the formula to the observed data. The formula used for the predict on of the seed temperature was as follows: $\frac{{\partial}T_s}{\partial\theta}\;=\;-\frac{{\alpha}(T_s\;-\;T_L)^{3.3}}{W(C_s\;-\;\frac{{\delta}m(CT_s\;+\;{\sigma})}{T_s^2})}$ where C = difference of the specific heat between pure ice and water m=moisture content of soybean seed $T_s$ = seed temperature $T_L$ = Temperature of liquid nitrogen W = mass of soybean seed $\alpha$ = proportional constant $\delta$ = constant depends on variety or the type of seed $\theta$ = time $\sigma$ = latent heat of melting of pure ice This study will give important information in the hydro-freezing technique by liquid nitrogen, available as a new technique of processing agricultural products in the near future.

• 대한환경공학회지
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• 제33권2호
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• pp.103-112
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• 2011

본 연구에서는 기존의 질소 수지에 관한 연구를 바탕으로, 우리나라의 2008년 질소의 총 유입과 유출을 수지분석 방법을 이용하여 추정하였다. 질소의 유 출입은 도시지역, 농 축산지역, 임야지역의 세부분으로 나누어 산출하였다. 질소의 주요 유입으로는 화학적, 생물학적 질소고정, 건식 및 습식 침착량, 해외로부터 수입된 양 등이 있으며, 유출된 양은 작물흡수, 휘발, 탈질, 침식, 표면유출, 산림소비 등으로 결정하고 그 양을 추정하였다. 연간 질소의 총 유입량은 1,294,155 ton/yr이며, 총 유출량은 632,228 ton/yr이었다. 질소수지를 기존의 2005년 질소 수지와 상호 비교 및 분석한 결과, 2008년도에 총 유입된 질소는 2005년 질소유입 보다 1.9% 저감된 것으로 조사되었다. 총 유입 질소의 감소는 질소비료 사용량 감소, 국토 개발, 경작지 감소 등으로 인한 결과이며 총 유출 질소는 6.3% 감소하였다. 질소 수지 분석에 의한 연간 발생한 비점오염의 양을 추정해본 결과, 2005년도에 연구되었던 질소 수지량에 비해서 22% 증가한 것으로 조사되었다. 탈질로부터 아산화질소 배출량을 산정하였는데, 농업지역과 하수처리장에서 약 8,289 ton/yr이 배출되었다.

• 상하수도학회지
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• 제24권6호
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• pp.775-788
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• 2010

The decomposition of 2,4,6-trinitrotoluene (TNT) and the mass balance of nitrogen (N) species as products were investigated in a UV/H2O2system by varying pH, concentrations of $H_2O_2$, and $O_2$. All experiments were conducted in a semi-batch system employing a 50 mL reaction vessel and a coil-type quartz-tube reactor. In contrast with previous studies employing batch mode, TNT decomposition in the semi-batch mode was proportionally enhanced by increasing $H_2O_2$ concentration to 10 mM (0.034%), indicatingthat an inhibitory effect of excess $H_2O_2$on hydroxyl radical (${\cdot}OH$) can be negligible. N compounds are released as $NO_2^-$ in the early stages of the reaction, but $NO_2^-$ is rapidly oxidized to $NO_3^-$ by means of ${\cdot}OH$. $NH_4^+$ was also detected in this study and showed gradually the increase with increasing reaction time. In this study, $NH_4^+$ production can involve the reduction of nitro group of TNT concurrent with the production of $NO_3^-$. Of the N species originating from TNT decomposition, 12 ~ 72% were inorganic forms (i.e. [$NO_3^-$] + [$NO_2^-$] + [$NH_4^+$]). This result suggests that the large remaining N portions indicate that unidentified N compounds can exist.

• 한국대기환경학회지
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• 제25권6호
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• pp.503-511
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• 2009

VOC mixture was fed to a trickle bed air biofilter (TBAB) with step-change in influent mixture concentrations from 50 ppmv to 1,000 ppmv, corresponding to loadings of $5.7\;g/m^3/hr$ to $114.1\;g/m^3/hr$. VOC mixture was an equimolar ratio of two aromatic VOCs, i.e., toluene and styrene, and two oxygenated VOCs, i.e., methyl ethyl ketone (MEK) and methyl isobutyl ketone (MIBK). The TBAB system employed backwashing as biomass control. The experimental results showed that a critical loading rate for VOC mixture removal was determined to be about $60\;g/m^3/hr$, and critical loading rates for individual VOCs in the mixture were different. Specifically, toluene content in the mixture played a major role in the biofilter overall performance. As VOC mixture was fed beyond the critical loading rate, reacclimation of the biofilter to reach the 99% removal efficiency following backwashing was delayed, which was a critical factor in the biofilter performance. In the mass balance analysis, 63.8% of the carbon equivalent in VOCs removal was used for $CO_2$ production during the experimental runs. The 82.6% nitrogen utilized in the biofilter was contributed to microbial cell synthesis. The obtained results were compared against consistently high efficient performance of TBAB for VOC mixture by employing backwashing as biomass control.

• 한국수산과학회지
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• 제24권1호
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• pp.21-30
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• 1991

충무시 북서쪽에 위치한 폐쇄성 내만으로 만 외측에는 굴 양식을 하고 있는 북만의 부영양화현상을 구명하고 수질이 최악에 달하는 하계에 일정수준 이상의 용존산소를 유지하기 위한 적정오염부하량 산정을 위해 1988년 1월부터 동년 12월까지 평균 월 4회 조사한 결과를 요약하면 다음과 같다. 전 조사 지점에서 총무기질소는 $0.10{\~}127.41$(평균: 10.71)$\{mu}g-at/l$, 인산 인은 ND-4.29(평균: 0.40) ${\mu}g-at/l$, Chlorophyll-a는 $0.35{\~}132.75$(평균; 11.90) $mg/m^3$이었고, 여름철 동안 평균농도는 각각 $11.06{\mu}g-at/l,\;0.80\mu g/l,\;11.11mg/m^3$로 이미 부영양상태에 있었다. 용존산소는 전 조사지점에서 $0.00{\~}13.42$(평균:6.45)ml/l 였고, 장마가 끝나고 일정한 기간이 경과한 시점인 7월에 전 지점의 저층에서 평균 2.08ml/l의 저산소수괴가 형성되었으며, 8월이후 증감을 되풀이하면서 점차 회복되는 경향을 보였다. 하계에 북만의 시간에 따른 용존산소 변화곡선은 $DO(ml/l)=15.57-1.40{\times}(day)+0.03{\times}(day)^2+0.0001{\times}(day)^3+......$와 같이 나타낼 수 있었고, 이와 같은 산소변화 특성으로부터 구한 산소소비계수 및 공급계수의 고유치는 각각 0.222/day, 0.018ml/l/day로 북만의 용존산소 수지 특성으로 볼 때 하계에 무산소 또는 저산소 상태를 막고 4ml/l이상의 용존산소를 유지하기 위해서는 이 일대의 해역에 수로의 변경이나 산소 공급장치를 이용 0.856ml/l/day 만큼의 산소를 공급하든지 또는 이 량에 해당되는 유입 BOD 부하를 폐수처리장 건설 등을 통하여 감소시켜야 할 것으로 생각된다.

• 한국식품영양과학회지
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• 제22권4호
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• pp.367-373
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• 1993

본 연구는 15~16세의 여자 고등학생 7명을 대상으로 4주간 평상시와 같은 생활양식과 식생활 환경하에서 에너지 섭취량(GE)과 체내 에너지 보류량(BE)의 변동을 측정하므로써 (에너지 평형법) 에너지 소비량을 산출하였다. 에너지 섭취량과 대변으로의 에너지 손실량(FE)은 열량계로 측정하였고 소변으로의 에너지 손실량 (UE)은 질소 배설량으로부터 환산하였다. 체내 지방조직량 (FM)은 피부두께를 측정하여 산출한 신체 밀도법에 의하였다. 총 에너지 섭취량에 대한 당질, 단백질 및 지방질의 구성비는 각각 70.1$\pm$1.8%, 12.2$\pm$0.7% 및 17.7$\pm$2.0% 이었다. 총 에너지 섭취량에 대한 대변으로의 에너지 손실율은 2.8%이었다. 대변과 소변으로의 에너지 손실량을 감하여 산출한 1일 1인당 평균 대사에너지량(ME)은 2022 $\pm$50㎉ 이었다. 28일동안의 체성분 변동량으로부터 산출한 체내 총 에너지변동량(BE)은 평균 2400$\pm$950㎉ 가 증가하였다. 1일 1인당 평균 에너지 소비량은 1958$\pm$87㎉로서 체중 kg당 39$\pm$2㎉ 이었다.

• 대한토목학회논문집
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• 제14권3호
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• pp.655-668
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• 1994

기존의 토양상 및 퇴비상을 이용한 악취제거가 주로 흡착에 의존한 나머지 탈취상이 쉽게 탈취능의 한계에 이른다. 따라서, 본 연구에서는 미생물 활성 탈취상의 조건인 높은 유기물함량, 보수성, 통기성 및 낮은 정압 등을 고르게 갖추고 있는 토탄에 활성슬러지를 식종하여 분뇨처리장, 하수처리장 등에서 발생빈도 및 취기강도가 큰 무기성악취 중 암모니아의 제거실험을 수행하였다. 실험결과, 자연 토탄상에서는 암모니아의 토탄수분에 의한 이온화에 따라서 pH가 상승하여 암모니아의 자연 유출 현상이 관찰되었다. 암모니아 제거 기작은 주로 음이론 콜로이드에 의한 흡착에 의존하였다. 미생물 활성 토탄상에서는 미생물 활동에 따른 pH의 완만한 상승으로 이론적 암모늄 이온의 비율이 자연토탄상보다 높았으나, 실제로 토탄상에 축적된 암모니아성 질소의 값은 질산균의 질산화에 의해 자연 토탄상보다 적었다. 암모니아의 제거기작은 반응조 운영 초기에는 흡착이 우세하였으며, 중반이후에는 질산화가 두드러졌다. 실험으로 얻은 암모니아 유입부하량, 암모니아 유출부하량, $NH_4{^+}$-N, $NO_x$-N, Org-N을 이용하여 질소에 대한 물질수지(Mass Balance)를 산정하고, 실험결과로 얻은 미생물 활성 탈취상의 최대 활성 시점인 비정상상태의 임계시간과 회귀분석에 의해 구한 암모니아의 흡착곡선을 이용하여 미생물 활성 토탄상에서 흡착능 포화의 연장시간을 산정하였다.

• 환경위생공학
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• 제12권3호
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• pp.9-17
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• 1997

This research aims to remove nitrogen in the piggery wastewater by combined process with upflow anaerobic sludge blanket (UASB) and biofilm process. For the effective denitrification. anaerobic and anoxic reactors were connected to a reactor. The effluent of aerobix reactor was recycled equally with influent in the upper filter of anaerobic reactor for denitrification and outlet of UBF reactor was connected to the settling tank with $1.5{\;}{\ell}$ capacity and the settling sludge was repeatedly recycled to UASB zone. The organic loading rate of total reactor was operated from 0.4 to $3.1kgCOD/m^{3}/d$ and it was observed that the removal rate of TCOD was 80 to 95 percentage. Ammonia nitrogen was removed over 90 percentage in the less volumetric loading rate than $0.1{\;}kgN/m^{3}/d$. But because of non-limitation of organic materials, it was reduced to 70 percentage in the more volumetric loading rate than $0.6{\;}kgN/m^{3}/d$. But denitrification rate was observed 100 percentage in the all of loading rate. This is caused by the maintenance of optimum temperature, sufficient carbon source, and competition of electron acceptors. The results of COD mass balance at the $1.21{\;}kgCOD/m^{3}/d$ was observed with the 71.7% percentage of influent COD. It was revealed that the most part of organic materials was removed in the aerobic and the anaerobic reactor because 38.4 percentage was conversed into $CH_{4}$ gas and 11 percentage was removed in the aerobic reactor with cell synthesis and metabolism. Besides, 5.7% organics was used to denitrification reaction and 3.7% organics related to sulfate reduction.