• 대한기계학회논문집B
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• 제24권3호
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• pp.402-410
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• 2000

As the combustion process of CWM consists of the water evaporation, the release and combustion of volatile matter, and the combustion of char for every particle, it is more complex than that of existent liquid fuel. Though the many studies on CWM combustion have been carried out by the single droplet using hanging methods or the multiple droplet using atomization methods, any report don't presents definite solution about the effects by the initial water evaporation and combustion of volatile. When CWM is suddenly exposed in the high temperature surroundings, the internal water evaporates and then each droplet builds up pores. Besides, porosity rate changes along the temperature of surroundings, the composition ratio of CWM, and the initial diameter of droplet. In result, because it affects the whole combustion rate, the combustion of CWM has complex mechanism as compared with the combustion of liquid or gas fuel. Therefore, concentrating on porous structure of CWM, this study has proceeded to acquire the basic data on the CWM injection combustion and closely examines the effects of the first stage combustion on the whole combustion by measuring the diameter variations, pore rate, mass fraction burned, and the internal temperature changes of CWM droplet. The results demonstrate that $60{\sim}70%$ of initial mass is reduced during water evaporation and volatile combustion period, and swelling rate, mass faction burned, and density variation are greatly concerned with atomization of CWM etc.

• 대한조선학회지
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• 제17권2호
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• pp.11-16
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• 1980

For vibration analysis of stiffened plates the orthotropic plate analogy is commonly accepted. As to stiffened plates in contact with water, however, there is still much uncertainty in estimation of the added mass because of the lack of direct methods. The authors, considering that for added mass of plates there are many reliable data derived theoretically or experimentally available, suggest a method to estimate the added mass of a stiffened plate by combining the mass increase factor, $\beta$, of an equivalent orthotropic plate and the correction factor, $\kappa$, for the effects of stiffeners. The latter is to be derived from systematic experimental investigations. Then, the natural frequency in water, f', can be calculated from that in air, f, by the equation $f'=f/\sqrt{1+\kappa\beta}$. To investigate practical applicability of this method, a systematic experiment was carried out with five uniaxially stiffened plates. Each of them had a plate of same size, $600mm{\times}600mm{\times}3.2mm$, but stiffeners of different size in the web-depth, 41.6mm, 51.2mm or 66.8mm and of different spacing 75mm, 100mm, or 150mm. Natural frequencies were measured under simply supported-edge conditions in both air and water, and corresponding $\kappa$ values derived. In spite of wide variations of web-depth and spcae of stiffeners, the experimental results show that the diversity of $\kappa$ values is not remarkable; mean values of $\kappa$ are 1.31 with standard deviation of 0.025 for the first modes and 1.27 with that 0.077 for the second modes. Hence, the authors concluded that the above $\kappa$ values can be used generally for the cases of uniaxially stiffened plates both sides of which contact with water, and that $\kappa$ values of general use for the cases of cross-stiffened plates may also be obtainable from similar experiments.

• 설비공학논문집
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• 제12권4호
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• pp.345-353
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• 2000

In this study, the performance of five ejectors has been investigated with working fluids of water and water vapor. The diameters of nozzle and mixing tube of five ejectors were 1 and 1.5(ejector A), 1 and 2(ejector B), 1 and 2.5(ejector C), 1 and 3(ejector D), 2 and 4(ejector E) in millimeters. The length of the mixing tube was 8-10 times of its diameter. For each ejector, the ratio of mass flow rate of ejected water to that of entrained water vapor, $\mu$, was evaluated in terms of evaporator pressure, mass flow rate of ejected water, and water temperature. It was found that the performance of an ejector was not stable when the ratio of diameters was too small or too large(ejector A and D) and $\mu$ was almost the same for two ejectors with the same diameter ratio(ejector B and E). It was also found that $\mu$ increased almost linearly with an increase of evaporator pressure and the ratio $\mu$ increased as water temperature decreased. As expected, $\mu$ converged to zero as the water temperature approached the evaporator temperature. Finally, a non-dimensional correlation has been developed to predict$\mu$ terms of evaporator pressure and saturation pressure of ejected water.

• 한국물환경학회지
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• 제22권6호
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• pp.1137-1143
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• 2006

In this study we investigated the removal characteristics of NOM and bromate formation characteristics in SOMT reactor. The system was recently developed as a novel ozone reactor and installed in SJ pilot plant. DOC values were decreased within 3% after treatment of 0.5~2.0 mg/L ozone dosage in SOMT reactor while the $UV_{254}$ value was 69% decreased at 2.0 mg/L ozone dosage. The composition of NOM was analysed by LC-OCD (Organic Cabon Detector) after ozone treatment in SOMT reactor to elucidate the variation of NOM character. Polysaccharide (more than 20,000 g/mol) fraction of NOM was decomposed while building blocks (350~500 g/mol) and neutral (less than 350 g/mol) fraction increased. Spiked bromide reacted with 0.5~2.0 mg/L ozone dosage in the SOMT reactor. The bromate formation was proportional to the ozone dosage ($R^2=0.978$) but not proportional to reaction time. The maximum concentration of formated bromate was not exceeded to 10% of spiked bromide concentration.

• 설비공학논문집
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• 제23권4호
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• pp.273-280
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• 2011

In this study, the steady state performance of a $CO_2$ heat pump water heater was measured with a variation of operating conditions such as refrigerant charge amount, compressor frequency, EEV opening, and water mass flow rate. Transient state performance tests were also conducted to investigate major system effects associated with the interaction between the $CO_2$ heat pump water heater and the water tank. Optimum refrigerant charge amount for the system was 1600 g. At compressor frequencies of 50 Hz and 60 Hz, water mass flow rates of 95 kg/h and 105 kg/h, and EEV opening of 8% and 16%, the water heating temperatures were $65^{\circ}C$ and $68^{\circ}C$ and COPs were 3.0 and 2.8, respectively. In the transient condition, the instantaneous COP decreased with an increase in the inlet water temperature.

• Membrane and Water Treatment
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• 제13권6호
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• pp.313-320
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• 2022

Theoretical calculation results are presented for the enhancement of the water mass flow rate through the hydrophobic micro/nano pores in the membrane respectively on the micrometer and nanometer scales. The water-pore wall interfacial slippage is considered. When the pore diameter is critically low (less than 1.82nm), the water flow in the nanopore is non-continuum and described by the nanoscale flow equation; Otherwise, the water flow is essentially multiscale consisting of both the adsorbed boundary layer flow and the intermediate continuum water flow, and it is described by the multiscale flow equation. For no wall slippage, the calculated water flow rate through the pore is very close to the classical hydrodynamic theory calculation if the pore diameter (d) is larger than 1.0nm, however it is considerably smaller than the conventional calculation if d is less than 1.0nm because of the non-continuum effect of the water film. When the driving power loss on the pore is larger than the critical value, the wall slippage occurs, and it results in the different scales of the enhancement of the water flow rate through the pore which are strongly dependent on both the pore diameter and the driving power loss on the pore. Both the pressure drop and the critical power loss on the pore for starting the wall slippage are also strongly dependent on the pore diameter.

• 대한지하수환경학회지
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• 제1권1호
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• pp.6-9
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• 1994

지하수의 Ar/$N_2$가스의 비율은 탈질화(denitrification)의 정도를 측정하는 하나의 방법으로 사용된다. (Barnes et al., 1975; Vogel et al., 1981; Mariotti et al., 1988) 그 비율 측정은 일반적으로 질량분석기 (Mass Spectrometer)를 사용한다. 본 실험에서 사용한 Mass Spectrometer는 일반적인 Static Mass Spectrometer가 아닌 Ar과 $N_2$을 시간적으로 동시에 측정하여 오차를 줄일 수 있는 VG Optima isotope ratio Mass Spectrometer를 사용하였다. 두 지역 지하수의 Ar/$N_2$가스의 비율을 측정한 결과 Site 1(Grand Island, NE)의 경우 대기가스가 포화된 증류수의 Ar/$N_2$가스 비율인 0.026보다 낮은 0.015-0.018로서 탈질이 일어났음을 알 수 있으며, Site 2(Shelton, NE)의 경우 0.023-0.02로서 탈질이 일어나지 않음을 알 수 있다. 본 실험의 목적은 지하수에 응해되어 있는 Ar/Nitrogen의 비율을 정확히 측정하는 방법을 개발하므로서 탈질의 정도를 정확히 측정하며 탈질의 전개 과정을 관찰하기 위한 것이다.

• 환경생물
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• 제17권2호
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• pp.175-182
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• 1999

1996년 여름 제주도 서쪽 해안에서 전에 볼 수 없을 정도로 유용 대형저서동물이 대량으로 죽어, 전복, 오분자기, 소라, 해삼, 말똥성게에 큰 피해를 주었다. 제주도 해안에서 식물플랑크톤 대발생은 없었고, 대량폐사가 일어나기 전에 해안에서 표층 저염수가 나타났기 때문에 저염분 스트레스가 대량폐사에 결정적인 영향을 미쳤을 것으로 여겨진다. 같은 기간 관측된 강수량이 적어, 강수량으로 저염화를 설명하지 못한다. 국립수산진흥원(1997)이 관측한 자료는 1996년 8월 제주도와 중국 사이 해역에 표충 저염수가 나타난 것을 확실히 보여준다. 제주도 서쪽 해안에 나타난 표층 저염수는 다량으로 유출된 강물이 그 기원일 가능성이 가장 높다. 해류와 양자강에서 제주도까지 거리등도 표층 저염수가 양자강에서 방류된 강물에서 기원한 것이라는 가설을 지지한다.

• 대한토목학회논문집
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• 제26권5C호
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• pp.359-368
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• 2006

시공후 터널의 거동에 영향을 주는 대표적인 인자들로 시간에 따른 투수상태와 지반의 장기거동을 들 수 있다. 본 연구에서는 이러한 인자들과 관련된 터널거동을 분석하기 위한 수치해석모델을 개발하고 터널이 겪을 수 있는 다양한 시공 후 하중 조건에 대하여 수치해석을 수행하였다. 터널 변상에 대한 영향인자와 터널거동의 메카니즘을 파악하기 위해 가능한 모든 변상 발생 시나리오를 구성하였으며, 부직포의 투수계수, 수위상승, 장기적인 이완하중과 과발파로 인한 손상 등 터널의 시공 후 장기 변상에 관련된 인자들이 조사되었다. 시공 후 터널 변상 발생 시나리오는 터널형식과 그에 따른 하중 메카니즘에 따라 크게 두 가지로 구분할 수 있음을 알 수 있었다. 토사터널에 대해서는 투수상태와 관련된 거동이 주요 변상의 원인으로 분석되었으며 배수재의 투수계수 저하와 수위상승에 의한 영향에 대해 분석하였다. 암반 터널에서는 암반의 점소성 거동을 분석하였고 암반의 이완과 크립에 의한 장기적인 이완하중의 영향에 대해 연구하였다.

• 한국소음진동공학회:학술대회논문집
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• 한국소음진동공학회 2003년도 추계학술대회논문집
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• pp.270-275
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• 2003

The nonlinear dynamic characteristic of a straight tube conveying fluid with constraints and an attached mass on the tube is examined in this study. An experimental apparatus composed of an elastomer tube conveying water which has an attached mass and constraints is made and comparisons are done between the theoretical results from non-linear equation of motion of piping system and experimental results. And the results show that the tube is destabilized as the mass of the attached mass increases, and stabilized as the position of the attached mass close to the fixed end. In case of a small end-mass, the system shows rich and different types of periodic solutions. For a constant end-mass, the system undergoes a series of bifurcations after the first Hopf bifurcation, as the flow velocity increases, which causes chaotic motion of the tube eventually.