Cuticular hydrocarbons (CHCs) were analyzed using GC and GC-MS, and compared with developmental stages of the bean bug, Riptortus pedestris. Carbon numbers on each developmental stages differed from 14-19 in eggs to 4th nymph, 25 in 5th nymph, and over 30 in last nymph that until adult emergence. Carbon numbers are increased to 16-17 carbons over time in newly emerged adults, 18-22 in 1 and 3 days after emergence, respectively; 23-27 in 6 days after emergence; approximately 30 in over 10 days after emergence. Carbon numbers increased as passed days after emergence. Riptortus pedestris consisted of n-nonacosane on almost all developmental stages, and followed by n-hentriacontane and 13,17-;15,19-demethyltritriacontane. Eggs, however, consisted of unknown compounds with high proportion and followed by n-heptacosane, and newly emerged adults also has a high proportion of n-heptacosane. From the above results, CHCs on developmental stages of the bean bug consist of n-alkane with saturated hydrocarbons (36-65 %), followed mono- or di- methylalkanes. However, newly emerged female and male adults mostly consisted of methyl-alkane. The major constituents of CHCs on the developmental stages of Riptortus pedestris is differently proportioned, but hardly showed the difference in their composition.

This study was performed to compare the host preference, survivorship and feeding behavior using EPG against ggot-mae-mi, Lycorma delicatula against seven plants such as Ailanthus altissima, Vitis vinifera, Malus pumila, Pyrus calleryana, Hibiscus syriacus, and Pinus densiflora. In host preference. L. delicatula was most preferred the Ailanthus altissima, Vitis vinifera and was not preferred the other plants. Survival rate of 3rd Nymph was recorded from Ailanthus altissima, Vitis vinifera as 15.0, and 15.4 days, respectively, it showed longest period. However, Malus pumila, Pyrus calleryana, Hibiscus syriacus, were survived within 6 days and Pinus densiflora was within 5 days. Moreover, L. delicatula was survived within 2 days to the three kinds of fruits. Ecdysis rate from 3rd to 4th nymph also high from Ailanthus altissima, Vitis vinifera as 63.3, 63.0 % and the order was followed as Malus pumila(17.7%) > Pyrus calleryana(9.3%) > Hibiscus syriacus(7.8%) > Pinus densiflora(5.9%). Especially, ecdysis rate was recorded 0% to the three kinds of fruits. Feeding behavior was analyzed using EPG and compared the differences their waveform from seven kinds of plants and three kinds of fruits. Non-probing time was short in host plants, reversely, Phloem-feeding time was recorded longer in Ailanthus altissima, Vitis vinifera as 45.7 and 13.7 min, respectively. And other plants and fruits were not showed feeding behavior.

본 논문에서는 효과적인 레이싱 드론 조종 훈련을 위한 VR 콘텐츠의 기획 및 제작에 대해 다루고자 한다. 실제 환경에서의 직접적인 레이싱 드론 조종 훈련은 공간적, 경제적 한계점이 분명한데, 이러한 한계점에 대한 해결책으로 VR 기반 드론 잠입액션 게임 <Drone S>의 제작을 통해 제시하고, 효과적인 드론 조종 능력 증진을 강구하고자 한다. 특히 FPV 고글과 HMD 기반 VR의 유사성을 활용하여 실제와 유사한 환경에서의 가상현실 콘텐츠를 기획하였으며, 레이싱 드론과 드론 레이싱에서 사용되는 구조물의 특징을 고려하여 가상 드론과 맵 및 장애물을 디자인하였다. 또한 점진적으로 증가하는 장애물의 난이도를 통해 사용자의 몰입도와 현존감을 높이고자 하였다.

This study is to compose the optimized membrane module process system to selectively separate and treat toxic gas emitted from the semiconductor process. To optimize the operation of membrane module process system to treat toxic gas, the inlet toxic gas toward the membrane module shall have equal flux and equal pressure. Therefore, if the inlet flux on the membrane may be equalized only with the adjustment of pipe diameter and arrangement without installation of devices such as flowmeter at the junction between distributing pipe and separation membrane, the pipe composition of membrane module process system may be optimized to reduce the cost as well. Here, the inlet gas pressure toward the membrane module shall be above 3 bar, and thus in this study, the system was established for gas to be compressed with the compressor to stably maintain the pressure at the inlet of membrane module. Accordingly, the flow and pressure of gas within the pipe from the compressor to the membrane module were evaluated through the numerical analysis to optimize the diameter and arrangement of pipe - eventually to be reflected on the on-site design. Based on the result of flow analysis, the 5,000 LPM fluoride gas separation system to be applied to the actual semiconductor process was established, and to confirm the separation and return efficiency of NF3, CF4, and SF6, in this study 1,000 ppm of highly concentrated NF3, CF4, and SF6 were injected into the system to check the rate of separation and return. The system was continuously operated for 300 hours, and in case of SF6 and CF4, on average of 93% or higher return rate and concentration ratio of 1 were maintained, while in case of NF3, on average of 90% or higher return rate and concentration ratio of 1 were maintained. Therefore, it was confirmed that the fluoride gas separation system may be applied as a low-energy consumption high-efficiency system for the electronic industry.

In this research, chemical vapor deposition equipment built in the semiconductor·CVD (Chemical Vapor Deposition)process was introduced. Through polysulfone hollow fiber membranes under similar conditions to those of the actualprocess, conditions such as flow and pressure were used to observe the influence in order to separate and collect the SF6and CF4 substances. Results showed that as the retentate flow rate of the discharge unit increased and the residence timeto penetrate the membrane decreased, the emission concentration increased. As the pressure of the discharge unit increasedand the exhaust flow decreased, when the retentate flow rate was 10L/min, CF4 was shown to have a density of 4,963ppm, and it was 4,028ppm for SF6 the gas mixture had a concentration effect of three to four ratio. In addition, throughthe separation factor of fluorinated gases that arise in the actual process, the collection and concentration of SF6 and CF4were possible each gas’s recovery rate was higher than 99%.

This research was conducted to configure an optimal membrane module system that would selectively separatehazardous gases which are emitted during the processes in the semiconductor industry. In order to identify the most integralcharacteristic results, a numerical analysis formula which incorporates the dimensions of pipe diameter and gas flow ratewas utilized. Based on the results of the numerical analysis formula, a prototype designed with the main pipe being 100Awith gas outlets made with identical diameter thickness to the main pipe, set at equal intervals, was built. When the gasflow rate is set at 100L/min, although the processing outlets 1, 2, and 3 showed 0.03m/sec deviations in the rate ofspeed, when considering the variables of the average flow rate, the same emission rates are noted. However, in the instanceof when the overall prototype pipe dimensions was enlarged to 200A and the gas flow rate was increased to 500L/min,there was better stabilization. Therefore concluding that as the pressure rates flowing in the main pipe increases, morestable characteristics at the gas outlets can be found.

Of the 6 most abundantly recognized Greenhouse Gases, SF6 (Sulfur Hexafluoride) is one of the most potentially consequential gases to Global Warming. The permeation characteristics of fluorinated gases N2 and SF6 used in the semiconductor processes were examined by study through the processes that occur during the Hollow Fiber Membrane Separation Technology. The developed module had a permeance of 8.83 ~ 17.40 GPU for N2 with N2/SF6 selectivity of 8.64 ~ 40.80 at various pressure and temperature. The SF6 isolation results showed the variables increased SF6 concentration levels of 13% ~ 63%, with a yield increase of 50% ~ 96%. These results are proven to be well utilized in the semiconductor manufacturing processes in the recovery of SF6 through the Hollow Fiber Membrane Separation Technology.