본 연구는 국내 개발 이탈리안 라이그라스(IRG)의 봄철1회 및 2회 이용 시 수확적기를 구명하고자 국립축산과학원(수원)에서 조생종 ‘Kowinearly’ 품종을 공시, 2009년 9월 30일에 파종하여 2010년 6월까지 수행하였다. 처리내용은 1차 수확시기로 출수시(T1), 출수기(T2), 출수후기∼개화초기(T3), 개화기∼개화후기(T4), 등숙기(T5) 및 등숙후기(T6) 등 6처리였으며, 2차 수량조사는 6월 11일 동일하게 실시하였다. ‘Kowinearly’의 출수시는 5월 4∼5일, 출수기는 5월 14일, 도복은 개화 이후 많이 관찰되었다. 건물률은 T1 14.8%에서 T6 35.0%로 생육진행에 따라 높아졌으며, 조단백질, RFV, 건물 소화율 등 사료가치는 생육 지연에 따라 낮아졌다. 건물수량과 가소화 건물수량은 T4에서ha당 각각 8,984 kg과 5,728 kg으로, 조단백질 수량은 T3에서 795 kg으로 유의적으로 높았으며(p<0.05), 재생초의 건물수량, 조단백질 수량, 가소화 건물수량은 T1과 T2에서차이 없이 각각 5,425 kg, 596 kg, 3,204 kg (T1)과 4,811 kg,589 kg, 3,143 kg (T2)으로 유의적으로 높았다(p<0.05). 총건물수량, 조단백질 수량, 가소화 건물수량은 T2와 T3에서차이 없이 각각 11,089 kg, 1,254 kg, 7,669 kg (T2)과 10,354kg, 1,225 kg, 6,915 kg (T3)으로 유의적으로 높았다(p<0.05).일당 건물생산량과 일당 가소화건물생산량은 1차 생육은T2, T3, T4에서, 재생초는 T2, T1에서 높았으며, 전 기간일당생산량에서는 출수기인 T2에서 가장 높았고 다음이T3, T4, T1 순이었다. 이상의 결과를 종합하여 볼 때, IRG‘Kowinearly’를 봄철에 1회 수확하여 이용할 경우 단위면적당 생산량과 사료가치를 고려한 수확적기는 출수후기∼개화기이며, 봄철 2회 수확하여 이용할 경우 재생과 단위면적당 총 생산량을 고려한 1차 수확적기는 출수기가 유리하다고 판단된다.

현재 분리막 여과 공정은 정수처리에서 많은 관심을 받고 있다. 하지만, 분리막의 효율적인 운영을 위하여 '혼화/응집(/침전)' 등의 전처리 시설 설치로 인한 부지면적 및 비용증가와 5~10%의 배출수 문제가 추가적으로 발생한다. 그래서 본 연구에서는 전처리 공정 없이 지표수(한강)에 대하여 가압식 PVDF 분리막[(주)에코니티]으로 운전하여 성능을 검토하였으며 그 결과 1년 동안 화학적 세정 없이 여과 flux가 1~2.4 m/d (at 25℃)로 운전되었고, 유입원수의 탁도와 상관없이 분리막 처리수의 탁도는 0.05 NTU 이하로 안정되게 유지되었다. 또한, 회수율 제고를 위하여 1개월 동안 가압식 배출수(역세수 + 배수)를 침지식 PE 분리막[(주)에코니티]으로 연계하여 2단 막여과 운영을 한 결과 전체 공정 회수율을 99.5%까지 증가시킬 수 있었다.

Particle collection efficiency and air cleaning capacity were tested for the two-stage electrostatic precipitator for use in indoor air cleaning systems. A wire-plate type ionizer was used as a particle charger and a dielectric film consisted of polypropylene (or polyethylene) coated metals and zigzagged metal electrodes was used as a particle collector in the electrostatic precipitator. Both particle collection efficiency and air cleaning capacity increased as increasing the applied voltage on the charger and the collector, and furthermore, as increasing the collector film width (i.e. collection area). Air cleaning capacities estimated by the product of particle collection efficiency and air flow rate were quite well consistent with the experimental ones with a proportional constant of 0.964. Ozone concentrations emitted from the charger at the applied voltages of 5.0 and 5.2 kV were less than 0.05 ppm, indoor ozone standards of UL 867-2002, KS C 9314 and SPS-KACA002-132. For the air flow rate of 11.7 m³/min, the applied floor area of 48.2 m² could be obtained when 5.2 kV and 6.0 kV were applied on the ionizer and the collector, respectively and the collector of two 15 mm polyethylene dielectric films was used.

본 연구는 공급자(supplier), 소매상(retailer) 그리고 고객(customer)으로 구성된 2 단계 공급사슬에서 소매상의 관점에서 소매상의 최적 재고정책 결정에 관한 문제를 다루었다. 공급자는 수요 증대를 목적으로 소매상의 주문량에 따라 다단계로 일정기간동안 제품 판매대금에 대한 지불 연기(외상)를 허용하고, 고객의 수요는 소매상의 제품 재고량에 영향을 받는다는 가정 하에 재고 모형을 설계하였다. 모형 분석을 통하여 소매상의 이익을 최대화하

In this paper, cycle performance analysis of two-stage compression and one-stage expansion refrigeration system using alternative Freon refrigerants is presented to offer the basic design data for the operating parameters of the system. Pure alternative Freon refrigerant R32, R134a and near NARM(Non-Azeotropic Refrigerants Mixtures) R404A, R407C, R410A and ARM(Azeotropic Refrigerant Mixtures) R507A were used working fluids in this study. The operating parameters considered in this study included evaporation temperature, condensation temperature, subcooling degree, superheating degree, mass flow rate ratio of inter-cooler. The main results were summarized as follows : The COP of two-stage compression and one-stage expansion refrigeration system increases with the increasing subcooling degree and mass flow rate ration of inter-cooler, but decreases with the increasing evaporating temperature, condensing temperature and superheating degree. Therefore, subcooling degree, mass flow rate ratio of inter- cooler of two-stage compression and one-stage expansion refrigeration system using alternative Freon refrigerants have an effect on COP of this system.

본 연구는 SDI (Silt Density Index)를 통해 RO막 전처리 장치로서의 섬유여과기 적용 가능성을 평가한 것이다. 실험 대상 원수는 탁도가 0.76∼1.6 NTU인 하수처리장 방류수와 탁도가 2.2∼3.3 NTU인 해수 및 탁도가 100 NTU인 지표수이었다. 2단 섬유여과기 공정의 최종여과수인 2차 여과수의 탁도는 17% PAC 10∼30 ppm주입 시 0.07∼0.25 NTU였으며 SDI는 1.4∼2.8이었다. 하수처리장 방류수에 대해 2단 섬유여과기 pilot 여과수와 실험실 규모의 MF, UF평막 여과수의 탁도 및 SDI15를 측정하여 비교한 결과, 여과수 수질은 2단 섬유여과기 > MF > UF순으로 약간 향상하였으며, SDI15 차이는 0.7∼1.0 수준으로 크지 않았다. 따라서 2단 섬유여과 공정을 RO막 전처리 공정으로 사용할 경우 통상의 RO막 제조사가 요구하는 SDI15 5 이하를 충분히 만족시킬 수 있을 것으로 판단된다.

  기간차량경로 문제는 차량용량제약을 고려한 차량경로문제를 다 기간으로 확장한 형태의 문제로 역방향 로지스틱스의 폐기물 혹은 재활용품 수거에 관련된 주요한 운영 문제들 중의 하나로 각 고객에 대해서는 계획기간 중에 방문해야 하는 횟수가 정해져 있어 방문날짜 조합을 결정해야 하며 주어진 방문날짜 조합 하에 각 기간의 차량경로도 결정해야 한다. 주요한 제약조건으로는 차량의 용량제약과 각 기간의 가용 시간제약이 있으며 소요차량의 대수를 최소화하는 것을 목적으

Numerical analysis was conducted to characterize the particle charging quantities in the charging cell of a 2-stage parallel-plate electrostatic precipitator with respect to particle size. The numerical method took into consideration of particle charging rate equations and particle equations of motion, allowing the locally varying non-uniform electric field and ion number concentration along the particle trajectory. The charging rate model developed by Lawless (1996) was used in the present study. According to the present study, the numerical results showed good agreement with the available experimental data.

This paper considers a scheduling problem concerned with an assembly system where two components are first treated in their own parallel machines and then pulled to be assembled into a final product at a single assembly machine. The objective measure is t

2단계 접속 논리(two-stage cascaded logic)는 관측 지역 내에 새로이 출현한 표적에 대한 트랙을 만드는 대표적인 방법중의 하나이다. 2단계 접속 논리의 트랙 생성 (track formation)에 관한 성능 평가 방법 및 결과는 Bar-Schalom에 의해 발표된 바가 있으나, 그 연구 결과는 트랙 생성 성능을 도출할 때 클러터로 인한 오경보율(false alarm probability)을 무시한다는 가정에 기초한 것이기 때문에, 오경보율이 높은 경우에는 적용 할 수 없다는 단점을 지닌다. 이에 본 논문에서는 오경보율을 고려하여 2단계 접속 논리의 트랙 생성 성능을 평가 할 수 있는 개선된 방법을 제시하고자 한다. 그리고 2단계 접속 논리에서 사용하는 데이터 연관(data association)기법으로 트랙 분리(track splitting)기법과 최 근접 데이터 선택 기법(nearest neighbor rule)을 사용하는 경우에 대하여 각각의 성능 평가 결과를 몇 가지 예시하고자 한다.

In this study, the two-stage electroflotation-rising process was investigated with the aim of improving the performance of the conventional one-stage electroflotation process. A total of 32 min (the electroflotation and rising times were 30 min and 2 min, respectively,) was required when a current of 0.35 A was applied in the one-stage electroflotation-rising experiment. The amount of electric power required to treat 1 m3 of water was 1.75 kWh/m3. For the two- stage system, the time required to achieve a turbidity removal rate of over 95% was 16 min (50% of the one-stage system). The amount of electric power required to treat 1 m3 of water was 0.59 kWh/m3, which was only 33.7% of that required for the one-stage process. The total treatment time and electric power were excellent in case of the two-stage system in comparison with those of the one-stage process. The rate of turbidity removal for the horizontal electrode arrangement is 9.3% higher than that of vertical electrode arrangement. When Na2SO4 was used as the electrolyte, the optimum electrolyte concentration was 1.0 g/L.

This study aims to investigate the interplay between education and local roads on Foreign Direct Investment (FDI) in the Philippines, using economic growth as an instrument. The study used the quantitative research design applying both descriptive and inferential statistics. A combination of Two Stage Least Square Regression Model and three approaches in Panel Regression Model such as Pooled Least Square, Fixed Effect Model, and Random Effect Model were utilized in order to study the effects of education and local roads on foreign direct investment of the Philippines. Based on Fixed Effect regression results, higher education graduates and local road investments, as conditioned by economic growth, were significant factors in order to increase the foreign direct investment in the Philippines. Accordingly, a unit increase in higher education graduates, as conditioned by economic growth, leads to 8.758 unit increases in the foreign direct investment. While, a unit increased in local road investments, as conditioned by economic growth, leads to a 0.002 decrease in foreign direct investment. The regression results of the study suggest that the Foreign Direct Investment in the regions such as CAR, I, II, IV-B, V, VIII, IX, X, XI, XII, XIII, and ARMM are higher compared to Region IV-A.

본 논문은 콘크리트 배합 방식(NMA, TSMA1, TSMA2)에 따른 순환 굵은골재 치환량에 따른 콘크리트의 기계적 성능을 비교 평가 하였다. 실험은 순환 굵은골재를 0%, 50%, 100%로 3수준으로 콘크리트의 배합 방식에 따라 실험을 진행하였다. 굳지 않은 콘크리트에서는 공기량, 슬럼프, 단위용적질량 실험을 진행하였으며, 경화 콘크리트에서는 압축강도 및 휨강도 시험을 진행하였다. 본 연구의 실험결과 NMA 방식과 비교하여 TSMA 방식에서 강도 저하가 나타나고 있음을 확인할 수 있었다. 하지만, 이는 순환 굵은골재가 다량 치환됨에 따른 것으로 사료된다. 순환 굵은골재가 다량 치환됨에 따라 슬럼프 증진, 공기량 증진, 강도 저하가 나타남을 확인하였다.

Understanding the response of a crop to water deficiency is the first step towards breeding drought-tolerant varieties. In this study, inbred maize (Zea mays L.) lines KS140 and KS141 were subjected to drought stress by withholding water for 10 days at the V5 or V6 leaf stage. Water-deficient plants experienced a decrease in relative leaf water content, stomatal conductance, net CO2 assimilation rate, and water use efficiency compared to well-watered plants. This was accompanied by a decrease in the relative leaf water content that resulted in severe growth retardation in KS140 and KS141. However, leaf chlorophyll content in KS140 was unchanged. To understand the proteome dynamics during the 10-day drought stress in maize leaves, comparative proteome analysis was carried out between the well-watered and water-withheld leaves. Differential expression was observed for 29 protein spots from KS140 and 14 protein spots from KS141, and these were identified using MALDI-TOF mass spectrometry. Among identified proteins, metabolism and stress related proteins were highly were increased by drought stress. This study provides a protein profile of a Korean maize inbred line during drought stress, which will be valuable for future studies of the molecular mechanisms underlying drought resistance and for development of selective breeding markers for drought tolerance in maize.

This study has cross checked the change of internal sludge-recycle in Anaerobic-Digestion, and researched about not only the improvement of Bio-gas production from the digested sludge but also the efficient method of sludge minimization. Ultimate object of the study is to reduce the amount of sludge by the improved efficiency of contact with the organic-matter and the microbes in Anaerobic-Digestion. The sludge-recycle fluidized sludge layer and raised the activity of the sludge, the optimal sludge-recycle ratio, VS and COD removal ratio were 1,000%, 28.2% and 27.7%, respectively. Through these results of this study, it may be of use to treat waste sludge by the sludge-recycle ratio in terms of minimization and circulation of resources.

This study aimed for evaluating the applicability of the two stage dual media filtration system in field water treatment plant. The field plant of two stage and dual media filtration system was operated for 2 months. Average iron concentrations of the settled water, existing filtered water and second stage filtered water was 0.041 mg/L, 0.007 mg/L and 0.005 mg/L, respectively. Removal efficiency of iron concentration in the second stage is appropriately 35% more than in existing filtered water. Also removal efficiency of residual chlorine in the dual media filtration system is relatively 42.3% more than in existing filtered water due to adsorption of activated carbon, but the removal of ammonia nitrogen by adsorption is insufficient. Average concentrations of THM and chloroform in the settled water are 0.033 mg/L, 0.026 mg/L, respectively and in existing filtered water are 0.023 mg/L and 0.023 mg/L. Average concentrations of THM and chloroform in the dual media filtration system are 0.008 mg/L and 0.013 mg/L. Therefore removal efficiency of THM concentration in second stage is more than 66.4% in existing filtrated water. Also removal efficiency of chloroform in the dual media filtration system is more than 50.0% in existing filtered water because of the adsorption of activated carbon. In this case backwashing period in dual stage system is 4～5 days, but in existing filtration system is 1～2 days.