• 한국수산과학회지
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• 제21권4호
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• pp.206-216
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• 1988

키조개, Atrina(Servatrina)pectinata의 효율적인 종묘생산기술개발을 목적으로 1986년 6월 8일부터 10월 16일까지 진해만내의 칠천도 연구리 앞바다에서 부유유생의 출현시기와 각 유생단계별 생존율을 조사하고, 1987년 7월 6일부터 11월 23일까지는 연구리 앞바다에서, 1987년 7월 9일부터 1988년 2월 15일까지는 여자만에서 각각 수직식 및 수평식 채묘실험을 하였다. 부유유생 조사기간중 크기가 약 $135\times144um$인 D형유생은 8월 1일, 8월 12일, 8월 25일에 각각 출현 peak가 있었으며, $300\times317um$인 umbo형유생은 8월 9일, 8월 22일, 9월 4일에, $468\~450um$의 성숙 유생은 8월 22일, 9월 3일, 9월 16일에 각각 peak가 있었다. D형유생에서 umbo형유생으로 되는데는 약 $9\~10$일 걸렸으며, 순간생존율(survival rate/day)은 0.94, 전생존율은 $54\%$였다. umbo형유생에서 성숙유생으로 되는데는 약 $12\~14$ 일 걸렸으며 순간생존율은 0.08, 전생존율은 약 $19\%$였다. D형유생은 발생에서 채묘의 대상이 되는 성숙유생으로 되는데는 약 $22\~23$일 걸렸으며 이 기간 중 전생존율은 약 $10\%$였다. 치패의 부착밀도는 연구리 앞바다의 수직식 채묘기에서 0.16개체/$m^2$이었으며, 여자만 수역의 수평식 채묘기에서 0.48개체/$m^2$이었다. 부착치패의 평균갑장은 1987년 9월 27일 $0.51({\pm}0.15)\;mm$, 11월 21일, $38.52({\pm}6.98)\;mm$, 1988년 2월 15일에는 $49.00({\pm}10.77)\;mm$였다. 각장(SL)에 대한 각고(SH)의 관계식은, SH=0.4749 SL-0.5893 (r=0.9651) 각장(SL)에 대한 전중(TW)의 관계식은, $$TW=0.0700\;SL^{2.6772}\times10^{-3}(r=0.9780)$$. 전중(TW)에 대한 육중(MW)의 관계식은, MW=0.4913 TW-0.1228 (r=0.9809)이었다.

• Journal of Biosystems Engineering
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• 제33권6호
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• pp.384-389
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• 2008

Three prototype chestnut harvesters were constructed and evaluated their chestnut collection ability and field efficiency. Air-lock paddle system successfully picked up all loose material, and pick up efficiency was about 56 kg/h. Power required to operate this system was evaluated to be 8.7 kW with an air flow rate of $32.6\;m^3/min$. A radial blade type blower with 0.41 m impeller diameter was considered to be a minimum size for this system. For the auger system, air was sucked into the cylinder as the hinged flat cover began to be opened by the material pushed by the auger, and the empty burrs flew back to the container through the space between auger flights and collected in the bottom of the container. It was considered to add a device to prevent air from flowing back or to use the back flowing air for separation of burrs and nuts inside the container. The venturi system could not pick up chestnuts, as they only carried part way up to the suction hose. Consideration was given to an idea that the venturi could be used as a cleaning and separation mechanism for containers filled with both empty burrs and good nuts. A minimum vacuum of 129 mm wg was required to pick up chestnuts, and the corresponding inlet air velocity was 19.3 m/s. 104 mm of vacuum, which was about 81 % of that required for nuts, was enough to pick up burrs with nuts inside. Also, empty burrs with higher moisture content recorded the same pressure as for the burrs with nuts.

• 한국물환경학회지
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• 제35권6호
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• pp.567-573
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• 2019

DABF(Dissolve Air Flotation with Ball Filter) is developed as the DAF with the addition of a fiber ball at the lower part of the DAF. The DABF with a capacity of 4,500 ㎥/h was constructed at Gijang SWRO plant in Busan. Since the ball filter has high filtration rate, the loading rate of DABF was designed from 20 to 42 ㎥/h/㎡. When one DABF basin is in the back washing mode, the loading rate of other two DABF basins is increased to 42 ㎥/h/㎡. Turbidity at the BF outlet in DABF is <2 NTU at turbidity of 5-10 NTU at the BF inlet. If there is no algae bloom and turbidity is low in raw seawater, only BF in DABF is operated and meets <2 NTU at the BF outlet. Even if BF is operated at high hydraulic loading rates, no significant differential pressure increases and reduction in the turbidity removal rate is minimal in a day. Thus, DABF is the pre-treatment technology that provides stable water quality even with BF onlyoperation without DAF operation. Compared with the DAF, DABF requires additional facilities such as valves, piping, and drainage systems for backwashing the BF. But in terms of footprint and operating costs, DABF has more advantages than DAF. With DABF application, the load of the downstream filtration equipment is decreased so that the capacity of the filtration equipment can be reduced. Also, if the downstream filtration equipment is to be maintained the same regardless of DABF, the operating cost of DABF is less than DAF.

• 한국유체기계학회 논문집
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• 제19권6호
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• pp.50-54
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• 2016

The performance of a scroll expander is the most important factor for the efficiency of small scale Organic Rankine cycle waste heat power generation systems. In this research, a scroll compressor was purchased and operated in reverse to function as a scroll expander. With air as a working fluid, a series of performance test were conducted on this expander by varying the inlet and outlet pressure. Secondly, We have tested through 2000 to 3500 rpm rotational speed to find the maximum power and efficiency of the expander. And last, It was observed in the initial experiments that the design of the expander's orbiting scroll wrap partially blocked the fluid intake which may have caused unnecessary flow resistance. To verify this theory, a small part of the scroll wrap was removed and the performance test was redone. It was observed that the lower back pressure assure the higher efficiency and power of expander and the rotational speed that shows maximum adiabetic efficiency of scroll expander is 69% at 2500 rpm. And by modified wrap of the scroll, we could get volume flow rate for 13% to 19% and power for 5% to 18% increased. But the maximum efficiency of the modified scroll was decreased 8%.

• 대한기계학회논문집B
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• 제38권8호
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• pp.671-676
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• 2014

볼텍스 컵은 실린콘 웨이프 제조공정과 같이 민갑한 물체을 이송시키는 방법으로 제안되었다. 볼테스 컵의 상부에 위치한 노즐을 통해 공기를 공급하면 내부 실린더에서 큰 선회유동이 생성된다. 공기는 볼텍스 컵과 바닥면 사이의 틈새로 빠져나가면서 흡입압력을 생성시키고 물체를 들어 올릴 수 있게 된다. 본 논문에서는 볼텍스 컵에 관한 3차원 유동 해석을 통해 실험 결과와 해석 결과를 비교하여 해석의 신뢰성을 확인하였다. 그리고 볼텍스 컵의 길이 변화와 형상 변화를 주어 해석을 통해 흡입 압력 생성에 영향을 미치는 정도를 분석하였고, 볼텍스 컵 형상의 최적 조건을 제시하였다.

• 한국전자통신학회논문지
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• 제15권5호
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• pp.857-864
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• 2020

본 논문에서는 전술정보통신체계(TICN)의 구성 부체계 중 하나인 교환접속체계에서 이더넷 프로토콜을 지원하고 VoIP 교환기와 연동하여 보안된 음성통화/영상통화를 제공하고 다자간 통화, 지령기능 등의 차등 서비스를 지원하는 다기능형 VoIP 전화기의 야전에서의 전원부 불량을 저감하기 위해 개선한 방법들을 제안하였다. 다기능형 VoIP 전화기의 전용 어댑터 출력전압 인입부의 TVS 적용, PoE 모듈 입력단 TVS 적용, Blocking Diode 추가 및 폴리스위치 뒷단의 DC/DC 컨버터 추가 적용을 통하여 전원부를 개선하고 성능 및 환경 시험등을 수행하여 제안방법 타당성을 입증하였다.

• 한국환경과학회지
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• 제25권7호
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• pp.1017-1028
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• 2016

Wind information is one of the major inputs for the prediction of urban air flow using computational fluid dynamic (CFD) models. Therefore, the numerical characteristics of the wind data formed at their mother domains should be clarified to predict the urban air flow more precisely. In this study, the formation characteristics of the wind data in the Seoul region were used as the inlet wind information for a CFD based simulation and were analyzed using numerical weather prediction models for weather research and forecasting (WRF). Because air flow over the central part of the Korean peninsula is often controlled not only by synoptic scale westerly winds but also by the westerly sea breeze induced from the Yellow Sea, the westerly wind often dominates the entire Seoul region. Although simulations of wind speed and air temperature gave results that were slightly high and low, respectively, their temporal variation patterns agreed well with the observations. In the analysis of the vertical cross section, the variation of wind speed along the western boundary of Seoul is simpler in a large domain with the highest horizontal resolution as compared to a small domain with the same resolution. A strong convergence of the sea breeze due to precise topography leads to the simplification of the wind pattern. The same tendency was shown in the average vertical profiles of the wind speed. The difference in the simulated wind pattern of two different domains is greater during the night than in the daytime because of atmospheric stability and topographically induced mesoscale forcing.

• 한국가스학회지
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• 제21권5호
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• pp.9-15
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• 2017

천연가스 연료는 매장량과 경제성 측면에서 미래 가치가 매우 높기 때문에 여러 가지 이용 기술 개발이 활발하게 이루어지고 있으며 내연기관을 이용한 발전 분야에서도 그 중요성이 점점 증가하고 있는 실정이다. 천연가스 연료를 이용하는 MW급 발전용 대형 왕복엔진의 경우 연료공급시스템의 고도화 개발이 필요한데 그 중에서도 천연가스 분사기의 개발은 실질적인 천연가스 연료 이용을 위한 핵심이다. 본 연구에서는 천연가스 분사기를 상부에 위치한 솔레노이드의 전자기력에 의해 구동되고 하부의 밸브 바디부 전기자와 이동판이 상하로 움직이는 구조의 분사밸브 형태로 고안 및 설계하였으며 이 시작품의 동특성을 엔진 흡기 모사 조건에서 실험하였다. 지난 연구에서는 전기자의 변위와 지름 및 솔레노이드 코어 지름을 변경해 가면서 실험을 수행하였으며, 그 후속으로 솔레노이드 코어의 금속 재질 변경과 메인 하우징의 입구 크기 및 공급 압력에 따른 분사밸브의 동특성을 살펴보았다.

• 한국농공학회지
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• 제6권2호
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• pp.816-825
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• 1964

1. Outline: The flow of the siphon spillway is very intricate and affected by vacuous condition. It is an intresting problem to make vacuum rapidly in_siphon, i.e, to provoke the perfect siphonaoge with the lowest water-level of overflow. The hydraulic experiments of siphon spillway have practiced at the Masan Lake, Haenam, the province of Junnam and gained rational and economical results which cannot be odtained by calculation. 2. Experiment: The model scale was a half of that of the prototype. 3. Results and discussion: In the experiments of 14 runs, washing, overflow water level, outlet, water level of cushion, phenomenon of water flying and water pressure of every part, etc. were studied. a) The relation of overflow water-level at siphon inlet and deflector When the elevation of the deflector is 10. 65m and the form of deflector O.4m long is the hypotenuse of an $45^{\circ}$ isosceles triangle, the over flow water-level is the minimum, i. e. the siphonage was excellent. There is no effect by the rising of overflow water-Ievel between 11.95m to 1O.65m of deflector elevation (in the first plan, it is 11.05m). But the overflow water-level rises remarkably in the outside region of the above limits. b) The relation of overflow water-level, the length of cushion and standard height of the base. The reduction of the length of cushion brings the rising of overflow waterlevel, and the rising of the standard height of the base brings the rising of overflow water level. For the long cushion length and low standard height of the base, it cannot be expeted to have the falling of overflow water-level. The most satisfactory data were obtained at 5.20m of the base standard height and 6.1m of the length of cushion. The first vah,le planned was 5.70 m and 4.30m.

• 한국대기환경학회지
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• 제24권4호
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• pp.415-422
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• 2008

This study was carried out to investigate the effect of operating and design conditions of gas dispersion type of absorber on $SO_2$ removal efficiency. pH difference between upper and lower part of gas dispersing plate of absorber was 0.2, which was relatively low. This was supposed that recirculation capacity of absorbing liquid between froth zone and reaction zone of absorber be increased by oxidation air injection through liquid riser which acted as liquid pump. Test results showed that $SO_2$ removal efficiency was more sensitive than absorber ${\Delta}P$. High $SO_2$ removal even at lower pH resulted from very low concentration of $HSO_3^-$ ion in absorbing liquid because of direct supply of dissolved oxygen into froth zone. 96% of $SO_2$ removal efficiency was obtained under the condition of absorber pH 5.2, flue gas flow rate of $1,530\;Nm^3/hr$, inlet $SO_2$ concentration of 800 ppm, absorber ${\Delta}P$ of 250mmAq. The following equation by a multiple linear regression was obtained to describe the relationship between $SO_2$ removal and operating variables. $$f=1-{\exp}(-1.3939+1.060pH+0.0139{\Delta}P-0.00267G-0.000064SO_2Conc.),\;R^2=0.9719$$