• Agricultural and Biosystems Engineering
• /
• 제3권2호
• /
• pp.59-64
• /
• 2002

Odor generated during composting of livestock manure is mainly due to ammonia emission. Biofiltration is a desirable method to control composting odor. This study was conducted to analyze the efficiency of using fresh compost as a biofilter. A mixture of cattle manure and recycled compost was composted in a bin equipped with a suction-type blower. The exhaust gas was filtered through the fresh compost. Residence time was controlled by the flow rate of exhaust gas and the depth of filtering materials. At the aeration rate of 30 L/min(experiment I), ammonia reduction rate varied from 100% to -15% for biofilter A(residence time 56.5 s) and almost 100% for biofilter B(residence time 113 s). At the aeration rate of 30 L/min, the cumulative ammonia reduction rate was 80.5% for biofilter A and 99.9% for biofilter B. At the aeration rate of 50 L/min(experiment II), the lowest reduction rate showed a negative value of -350% on the 8th and 9th day for biofilter A(residence time 33.9 5), and 50% on the loth day for biofilter B(residence time 67.8s). At the aeration rate of 50 L/min, the cumulative ammonia reduction rate was 82.5% fur biofilter A and 97.4% for biofilter B. Filtering efficiency was influenced by residence time. The moisture content(MC) and total nitrogen(T-N) of the filtering material were increased by absorbing moisture and ammonia included in the exhaust gas, while pH was decreased and total carbon(T-C) remained unchanged during the filtering operation.

• 한국안전학회지
• /
• 제20권1호
• /
• pp.36-41
• /
• 2005

PCV(Positive Crankcase Ventilation) valve acts as a flow control valve to get a re-combustion of blow-by gas by having it flow from a crankcase to an inlet manifold suction tube. The blow-by gas of the crankcase should be eliminated or taken properly because it cause corrosion to critical parts, and contributes to increase crankcase pressure that can cause a drop in efficiency. The excessive stress and strain on the PCV valve that remove these harmful gas would be bring the difficult on the flow rate control and failure of the valve. Those condition inevitably induce the accident. Therefore, this study purpose is FEM evaluation of the stresses and deformation in the X3 PCV model according to the change of the differential pressure between inlet and outlet. From results, the maximum equivalent stresses increased linearly according to the increase of the differential pressure at the about 50mm from the inlet position and were under the yield strength of the valve. And the deformations were relatively small regardless of the in-outlet differential pressure variation.

• 한국추진공학회지
• /
• 제2권3호
• /
• pp.20-35
• /
• 1998

벽면을 통한 유체의 유동이 있는 난류운동장의 특성을 분석하였다. 벽면을 통한 유체의 유동은 유출과 유입의 경우를 포함하여 Re$_{w}$ 의 절대크기가 0~160으로 다양하며 입구에서의 $Re_{in}$도 3${\times}$$10^3$에서 8${\times}$$10^4$까지 넓은 범위를 대상으로 하였다. 벽면을 통한 유체의 유동은 벽면 경계층의 변화를 초래하고 이에 따라 난류 유동장의 급격한 변화를 일으켜 벽면을 포함한 전 유동장의 특성을 변화시킨다. 이러한 복잡한 유동장을 올바로 예측하기 위하여 난류운동에너지 소산율 방정식의 자 항에 대한 모델을 개선한 수정 $\kappa$-$\varepsilon$ 모델을 도입하였으며 기존의 난류모델과의 비교를 통하여 성능 검증을 시도하였다. 해석을 통한 분석결과로부터 수정 $\kappa$-$\varepsilon$ 모델은 벽면을 통한 유체유동이 있는 복잡한 유동장을 올바로 예측할 수 있음을 알 수 있었다. 따라서 수정 $\kappa$-$\varepsilon$ 모델을 이용하여 다양한 경우의 벽면 및 입구 조건을 갖는 난류유동장을 해석할 수 있을 것으로 판단된다.단된다.

• 대한기계학회논문집B
• /
• 제39권9호
• /
• pp.713-718
• /
• 2015

본 연구의 목적은 자동차용 에어컨 시스템의 연비 개선을 위하여 압축기의 성능 향상을 도모하고자 하는데 있다. 압축기 성능은 자동차용 에어컨 압축기 전용 열량계를 이용하여 평가를 수행하였다. 압축기의 성능을 향상시키기 위하여 흡입 유량의 증대와 토출 사체적 축소를 검토하였으며, 각 개선 항목에 대한 평가를 진행하여 성능과 COP 의 개선을 확인하였다. 흡입 유량을 증대했을 경우 저속 구간보다 고속구간에서의 성능 효과가 컸으며, 토출 사체적을 축소했을 경우 상대적으로 저속 구간의 성능 개선효과가 컸다. 조합품의 경우 저속과 고속에서 전반적으로 균형 있게 개선되었으며, 토출측 온도가 가장 크게 개선되었다. 성능의 경우 저속에서 약 3.2%, 고속에서 약 8.3% 개선되었으며, COP 는 저속에서 약 5.8%, 고속에서 약 6.2% 개선되었고, 토출 온도는 저속에서 $3^{\circ}C$, 고속에서 $5^{\circ}C$ 개선되었다.

• 한국초전도ㆍ저온공학회논문지
• /
• 제3권1호
• /
• pp.64-68
• /
• 2001

An experimental study on the Joule-Thomson cryocooler with the mixed refrigerant (MR) is described in this paper, J-T refrigeration experiment was performed with a single stage regular air-conditioning compressor The mixed refrigerant in the experiment was composed of 75% mol fraction of $N_2$. 30% moi fraction of CH$_4$. 30% moi fraction of $C_2$H$_{6}$. 10% mot fraction of $C_3$H$_{8}$ and 15% mot fraction of iso-C$_4$H$_{10}$. Oil mist in the MR stream could be eliminated completely by the glass microfiber filter. Since a single stage compressor that had been designed thor R22 is not appropriate for high Pressure ratio of the mixed refrigerant especially during the transient period. two modifications were incorporated to regular J-T refrigeration cycle. First. a Portion of the MR was by-passed at the inlet of the heat exchanger and transferred directly to 7he suction of the compressor in the modified system. Second, a buffer volume was Prepared to change the mass flow rate of refrigerant. The pressure ratio in J-T expansion device was relieved at the beginning of the operation due to the by-Pass scheme. but it gradually decreased during the transient Process as some of the MR component condensed at low temperature. The buffer volume at the suction side was used to increase the MR gas density in the system after the transient cool-down period. Form the experiment with the modified system, the refrigerator could reach the lowest temperature of -152$^{\circ}C$ without cooling load. and about -15$0^{\circ}C$ with 5 W of cooling load . . . .

• 유기물자원화
• /
• 제21권3호
• /
• pp.74-81
• /
• 2013

본 연구는 생활폐기물 처리에서 매립되는 폐기물량을 줄이고 재활용비율을 늘리기 위하여 고안된 풍력선별기 (공기의 흐르는 방향을 이용하여 공기 중에서 비중분리를 수행하는 방법)에 대하여 ANSYS사의 CFX Program을 이용한 수치 해석적 방법을 통해 풍력선별기의 모형을 설계 및 제작하고 시뮬레이션을 통해 풍력에 따른 폐기물의 분리 효율을 고찰하였다. 흡입장치에서 비닐봉지 1000mL를 흡입하도록 설계할 때 입구 풍속은 0.9 m/sec 이상에서 100%효율을 얻을 수 있었고 1.6 m/sec 이상에서 의 플라스틱병 500mL 와 플라스틱병 1500mL의 혼합 폐기물 효율의 100 % 알루미늄 250mL 선별 효율은 2.3 m/sec 이상에서 100% 마지막으로 알루미늄 250mL를 5mm 두께 압축 선별 효율은 2.4 m/sec 이상에서 90% 임을 알 수 있었다.

• 설비공학논문집
• /
• 제19권12호
• /
• pp.842-849
• /
• 2007

For a $CO_2$ two-stage twin rotary compressor used for heat pump water heater system, changes of $CO_2$ solubility in PAG oil were investigated along the gas passages from the first stage suction to final discharge. Only slight changes in solubility took place in suction chambers for both of the first and second stages, but for compression chambers, solubility variation ranged from 0.115 to 0.136, and from 0.133 to 0.182, respectively for the first and second stages. Calculation of gas flashing in parts of leakage oil flows and of oil contained in control volumes due to solubility changes was conducted and included in gas pressure calculation. For the second stage, gas flashing amounts to around $5%\sim6%$ for most leakage flows. Cooling capacity, compressor input, and COP obtained by calculation were well compared to the experimental results. Effects of operation speed on the compressor performance was also studied: as the shaft speed increased, adiabatic efficiency decreased rapidly due to increased over-compression loss.

• Journal of Biosystems Engineering
• /
• 제26권5호
• /
• pp.441-448
• /
• 2001

Hot air heater with light oil combustion is used as the most common heater for greenhouse heating in the winter season. However, exhaust gas heat discharged to atmosphere through chimney reaches up to 10~20% of total heat capacity of the oil burred. In order to recover the heat of this exhaust gas and to use for greenhouse heating, the heat pipe type exhaust heat recovery system was manufactured and tested in this experiment. The system consisted of a heat exchanger made of heat pipes, ø15.88${\times}$600mm located in the rectangular box of 675(L)${\times}$425(W)${\times}$370(H)mm, an air suction fan and air ducts. The number of heat pipe was 60, calculated considering the heat exchange amount between exhaust gas and air and heat transfer capacity of a heat pipe. The working fluid of heat pipe was acetone because acetone is known for its excellent heat transfer capacity. The system was attached to the exhaust gas path. According to the performance test it could recover 53,809 to 74,613kJ/h depending on the inlet air temperature of 12 to -12˚at air flow rate of 1.100㎥/h. The temperature of the exhaust gas left the heat exchanger dropped to 100$^{\circ}C$ from 270$^{\circ}C$ after the heat exchange between the suction air and the exhaust gas.

• 한국재료학회지
• /
• 제34권1호
• /
• pp.12-20
• /
• 2024

This study successfully prepared high-porosity aluminosilicate fibrous porous ceramics through vacuum suction filtration using aluminosilicate fiber as the primary raw material and glass powder as binder, with the appropriate incorporation of glass fiber. The effects of the composition of raw materials and sintering process on the structure and properties of the material were studied. The results show that when the content of glass powder reached 20 wt% and the samples were sintered at the temperature of 1,000 ℃, strong bonds were formed between the binder phase and fibers, resulting in a compressive strength of 0.63 MPa. When the sintering temperatures were increased from 1,000 ℃ to 1,200, the open porosity of the samples decreased from 89.08 % to 82.38 %, while the linear shrinkage increased from 1.13 % to 10.17 %. Meanwhile, during the sintering process, a large amount of cristobalite and mullite were precipitated from the aluminosilicate fibers, which reduced the performance of the aluminosilicate fibers and hindered the comprehensive improvement in sample performance. Based on these conditions, after adding 30 wt% glass fiber and being sintered at 1,000 ℃, the sample exhibited higher compressive strength (1.34 MPa), higher open porosity (89.13 %), and lower linear shrinkage (5.26 %). The aluminosilicate fibrous porous ceramic samples exhibited excellent permeability performance due to their high porosity and interconnected three-dimensional pore structures. When the samples were filtered at a flow rate of 150 mL/min, the measured pressure drop and permeability were 0.56 KPa and 0.77 × 10^-6 m² respectively.

• 대한기계학회논문집B
• /
• 제39권8호
• /
• pp.645-651
• /
• 2015

본 논문은 중앙구동 이젝터의 유량비에 미치는 설계변수의 영향에 대한 연구를 목적으로 한다. 중앙구동 이젝터의 설계변수는 구동노즐 출구 단면적 및 거리비, 디퓨저 출구 단면적비로 설정하였다. 실험장치는 가변노즐 이젝터, 전동 모터-펌프, 구동유체 저장수조, 제어판넬 그리고 고속 카메라 시스템으로 구성하였다. 유량비는 실험변수에 따라 측정되는 유입 공기량과 구동유체인 물의 유량을 이용하여 도출하였다. 유량비는 구동노즐 거리비와 혼합관 길이비가 커지면 증가하는 반면에, 구동노즐 면적비와 디퓨저 출구 면적비가 커지면 감소하였다.