• Journal of Biomedical Engineering Research
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• v.25 no.6
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• pp.599-604
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• 2004

Implantable flexible sensor using polymer/metal multilayer processing technique for telemetrical real-time blood pressure monitoring is presented. The realized sensor is mechanically flexible, which can be less invasively implanted and attached on the outside of blood vessel to monitor the variation of blood pressure. Therefore, unlike conventional detecting methods which install sensor on the inside of vessel, the suggested monitoring method can monitor the relative blood pressure without injuring blood vessel. The major factor of sudden death of adults is a disease of artery like angina pectoris and myocardial infarction. A disease of circulatory system resulted from vessel occlusion by plaque can be preventable and treatable early through continuous blood pressure monitoring. The procedure of suggested new method for monitoring variation of blood pressure is as follows. First, integrated sensor is attached to the outer wall of blood vessel. Second, it detects mechanical contraction and expansion of blood vessel. And then, reader antenna recognizes it using telemetrical method as the relative variation of blood pressure. There are not any active devices in the sensor system; therefore, the transmission of energy and signal depends on the principle of mutual inductance between internal antenna of LC resonator and external antenna of reader. To confirm the feasibility of the sensing mechanism, in vitro experiment using silicone rubber tubing and blood is practiced. First of all, pressure is applied to the silicone tubing which is filled by blood. Then the shift of resonant frequency with the change of applied pressure is measured. The frequency of 2.4 MHz is varied while the applied pressure is changed from 0 to 213.3 kPa. Therefore, the sensitivity of implantable blood pressure is 11.25 kHz/kPa.

• Korean Chemical Engineering Research
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• v.56 no.6
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• pp.871-877
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• 2018

Storing the surplus energy from renewable energy resource is one of the challenges related to intermittent and fluctuating nature of renewable energy electricity production. $CO_2$ methanation is well known reaction that as a renewable energy storage system. $CO_2$ methanation requires a catalyst to be active at relatively low temperatures ($250-500^{\circ}C$) and selectivity towards methane. In this study, the catalytic performance test was conducted using a pressurized bubbling fluidized bed reactor (Diameter: 0.025 m and Height: 0.35 m) with $Ni/{\gamma}-Al_2O_3$ (Ni70%, and ${\gamma}-Al_2O_3$30%) catalyst. The range of the reaction conditions were $H_2/CO_2$ mole ratio range of 4.0-6.0, temperature of $300-420^{\circ}C$, pressure of 1-9 bar, and gas velocity ($U_0/U_{mf}$) of 1-5. As the $H_2/CO_2$ mole ratio, temperature and pressure increased, $CO_2$ conversion increases at the experimental temperature range. However, $CO_2$ conversion decreases with increasing gas velocity due to poor mixing characteristics in the fluidized bed. The maximum $CO_2$ conversion of 99.6% was obtained with the operating condition as follows; $H_2/CO_2$ ratio of 5, temperature of $400^{\circ}C$, pressure of 9 bar, and $U_0/U_{mf}$ of 1.4-3.

• Korean Chemical Engineering Research
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• v.60 no.4
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• pp.535-543
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• 2022

A CPFD (Computational particle fluid dynamics) model of solar fluidized bed receiver of silicon carbide (SiC: average d_p=123 ㎛) particles was established, and the model was verified by comparing the simulation and experimental results to analyze the effect of particle behavior on the performance of the receiver. The relationship between the heat-absorbing performance and the particles behavior in the receiver was analyzed by simulating their behavior near bed surface, which is difficult to access experimentally. The CPFD simulation results showed good agreement with the experimental values on the solids holdup and its standard deviation under experimental condition in bed and freeboard regions. The local solid holdups near the bed surface, where particles primarily absorb solar heat energy and transfer it to the inside of the bed, showed a non-uniform distribution with a relatively low value at the center related with the bubble behavior in the bed. The local solid holdup increased the axial and radial non-uniformity in the freeboard region with the gas velocity, which explains well that the increase in the RSD (Relative standard deviation) of pressure drop across the freeboard region is responsible for the loss of solar energy reflected by the entrained particles in the particle receiver. The simulation results of local gas and particle velocities with gas velocity confirmed that the local particle behavior in the fluidized bed are closely related to the bubble behavior characterized by the properties of the Geldart B particles. The temperature difference of the fluidizing gas passing through the receiver per irradiance (∆T/I_DNI) was highly correlated with the RSD of the pressure drop across the bed surface and the freeboard regions. The CPFD simulation results can be used to improve the performance of the particle receiver through local particle behavior analysis.

• Journal of the Korean Society of Clothing and Textiles
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• v.28 no.12 s.138
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• pp.1596-1604
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• 2004

Quality Function Deployment(QFD) is a product development tool which ensures that the voice of the customer needs is heard and translated into products. To develop a sensible brassiere for middle-aged women QFD was adopted. In this study the applicability and usefulness of QFD was examined through the engineering design process for a sensible brassiere for middle-aged women. The customer needs for the wear comfort of brassiere was made by one-on-one survey of 100 women who aged 30-40. The customer competitive assessment was generated by wearing tests of 10 commercial brassieres. The subjective assessment was conducted in the enviornmental chamber that was controlled at $28{\pm}1^{\circ}C,\;65{\pm}3\%RH.$ As a results, we developed twenty-one customer needs and corresponding HOWs for the wear comfort of brassiere. The Customer Competitive Assessment was generated by wearing tests of commercial brassiere. The subjective measurement scale and dimension for the evaluation of sensible brassiere were extracted from factor analysis. Four factors were fitting, aesthetic property, pressure sensation, displacement of brassiere due to movement. The most critical design parameter was wire-related property and second one was stretchability of main material of brassiere. Also, wearing comfort of brassiere was affected by the interaction of initial stretchability of wing and support of strap. Engineering design process, QFD was applicable to the development of technical and aesthetic brassieres.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.40 no.11
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• pp.745-753
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• 2016

Micro methanol-steam reformer for fuel cell can effectively produce hydrogen as reforming response to steam takes place in low temperature (less than $250^{\circ}C$). This study conducted numerical research on this reformer. First, study set wall temperature of the reformer at 100, 140, 180 and $220^{\circ}C$ while methanol conversion efficiency was set in 0, 0.072, 3.83 and 46.51% respectively. Then, porosity of catalyst was set in 0.1, 0.35, 0.6 and 0.85 and although there was no significant difference in methanol conversion efficiency, values of pressure drop were 4645.97, 59.50, 5.12 and 0.45 kPa respectively. This study verified that methanol-steam reformer rarely responds under the temperature of $180^{\circ}C$ and porosity does not have much effect on methanol conversion efficiency if the fluid flowing through reformer lowers activation energy by sufficiently contacting reformer.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.38 no.7
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• pp.607-618
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• 2014

An experimental investigation of turbulent heat transfer during the vertical upward flow of supercritical $CO_2$ was conducted in a circular tube with inner diameter of 4.5 mm. The experiments were conducted at bulk fluid temperatures ranging from 29 to $115^{\circ}C$, pressures from 74.6 to 102.6 bar, local wall heat fluxes from 38 to $234kW/m^2$, and mass fluxes from 208 to $874kg/m^2s$. At moderate wall heat and low mass fluxes, the wall temperature had a noticeable peak value. For observing the buoyancy and flow acceleration effects on heat transfer, the ratios of Nusselt numbers from the experimental data and a reference correlation were compared with the $Bo^*$ and $q^+$ distributions. The flow acceleration parameter $q^+$ appropriately represented the heat transfer phenomena in the experiments. A new heat transfer correlation for the vertical upward flow of the supercritical pressure fluid was developed, and was found to agree with the experimental data with an error margin of ${\pm}30%$.

• Fire Science and Engineering
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• v.29 no.5
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• pp.104-109
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• 2015

The purpose of this study was to compare the ventilatory volume and airway pressure of a facial mask, endotracheal intubation, King tube, and I-gel devices with an Oxylator EM-100 using a RespiTrainer. The data were obtained from July 20 to 21, 2015. Data were analyzed using SPSS WIN 18.0 software. The ventilatory volume for endotracheal intubation was 537 ml (95% CI 530~545 ml), that for the King tube was 502 ml (95% CI 499~506 ml), that for the I-gel was 88 ml (95% CI 485~491 ml), and that for the facial mask was 499 ml (95% CI 496~503 ml). The airway pressure for endotracheal intubation was $11.34cmH_2O$ (95% CI $11.21{\sim}11.41cmH_2O$), that for the King tube was $10.67cmH_2O$ (95% CI $10.60{\sim}10.75cmH_2O$), that for the I-gel was $10.42cmH_2O$ (95% CI $10.35{\sim}10.67cmH_2O$), and that for the facial mask was $10.61cmH_2O$ (95% CI $10.55{\sim}10.68cmH_2O$). As a result, we were able to identify the appropriate ventilatory volume using the Oxylator EM-100.

• Food Industry
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• s.94
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• pp.37-40
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• 1988

1) 본 연구에서 시료로 선정한 충남 서산산 건강(dry ginger)은 수분이 $9.4\%$, 회분이 $8.7\%$ 그리고 alcohol에 의한 추출량이 약 $9\%$이다. 이는 선진국에 채택사용하고 있는 건강의 규격기준에 의하면 양호하다. 2) Non- flavor물질의 추출을 최소화하고 특히 증류과정에서 유효성분 손실을 최소화 할 수 있고, 엑기스내의 용매 잔류량이 인체에 유해하지 않고 추출효율을 높일 수 있는 용매는 ethyl alcohol이다. 3) 널리 사용하고 있는 관류추출(percolation)의 성능을 분석하고 이의 개선방안을제시하였다. - 추출효율을 높이기 위하여 건강(dry ginger)의 입자를 작게하면 압력강하가 증대되어순환되는 용액의 유속을 제어하기가 힘들다. - 입자가 작을 시에는 유체의 흐름이chan-nelling현상을 나타낸다. - 위와 같은 조건에서는 물질 전달속도가 느리므로 추출효율을 증대시킬 수가 없다. - 따라서 percolation추출에 사용되는 건강의 입자크기는 30mesh크기 이상이어야 운전조작이 용이하나 추출효율이 낮으므로, 추출시간 6시간에 회수된 생강엑기스양은 약 $2.5\%$이다. 4) percolation추출의 단점을 보완하기 위하여 기계적교반 추출을 선택하여 다음과 같은 개선점을 찾았다. - 교반형 추출에서는 고 - 액분리시 cake 저항에서 문제가 야기되지 않는 범위까지 건강의 입자를 작게할 수 있으므로 추출효율을 크게 향상시킬 수 있었다. 즉, 작게 분쇄된 건강(30mesh통과$90\%$)을 대상으로 추출시간 3시간에 $7\%$의 회수율로 증대시켰다. 최적 운전조건은 다음과 같다. 건강시료:1kg 시료크기:-30mesh$90\%$ 용매:ethyl alcohol 3$\iota$ 교반속도:900r.p.m 추출온도:상온($15\~25^{\circ}C$) 추출시간:3시간 일차 추출조건과 동일하게 하여 얻어진 엑기스의 수율이 $2\~2.5\%$이므로 총엑기스의 수율은 건강(dry ginger)무게기준으로 $8.5\~9.5\%$이었다. 5) 교반추출의 효율이 개선되었다 하더라도 추출물의 분리가 용이하여야만 공정의 이용이 가능하다. 그러므로 교반추출후 고 - 액분리를 위하여 정압여과 장치를 이용하여 여과시 cake의 평균 비저항을 얻었으며, 이의 값은 $4.31\times10^8cm\;/\;gr$으로서 여과에는 어려움이 없다는 것을 의미한다. 따라서 추출속도와 효율이 상대적으로 우수한 교반형 추출기의 가능성을 예시할 수 있음을 알 수 있었다. 6) 추출물을 농축과정에서 휘발성 oil의 손실을 최대로 줄이기 위해서는 단순증류를 하지 말고 분별증류를 수행하여야 하며, gingerol과 같은 중요성분의 열분해 반응을 억제하기 위해서는 열전달 효율을 증대시켜 증류조작을 원활히 수행하여야 하므로, still내의 농축물을 계속 교반시켜야 하며 감압상태에서 증류온도는 $40\~50^{\circ}C$로 유지시키는 것이 가장 바람직하다. 7) Ethyl alcohol로 추출된 엑기스내의 수분이나 회분함량은 외국산 제품에 비하여 약간 낮고, 반면에 조지방 및 조단백 성분의 함량은 약간 높게 나타나고 있어 대체적으로 본 연구에서 얻어진 엑기스내의 비풍미성분(non- fla-vour component) 함량은 외국산에 비하여 많은 차이가 없다. 8) 수입 외국산에 비하여 국산엑기스(본 연구에서 ethyl alcohol로 추출)내의 무기성분등의 함량은 비교적 낮은 편이다. 9) 건강에서부터 oleoresin을 얻어 paradol을 제거시킨 후 순수한 gingerol을 분리하여 IR과 NMR로 확인한 결과, 국산건강의 엑기스에는 주로 6-gingerol이고 약간의 10-gingerol이 함유된 것으로 나타났다. 10) 순수하게 분리된 gingerol을 열분석(TGA와 DTG)한 결과 약 $75^{\circ}C$에서 gingerol의 열분해 반응이 일어남을 알수 있었다. 11) 건강 분말시료와 엑기스내의 미생물 검사 결과 건강분말에서는 세균수가 많이 존재하는 것으로 나타났으나, 이는 ethyl alcohol로 추출하는 공정 중 대부분의 균들이 사멸된 것으로 나타났다. 12) 관능적 측면에선, 본 연구에서 제조한 엑기스와 수입엑기스를 비교한 결과 생강 특유의 맛은 비슷했으나, 수입엑기스에서는 쓴맛과 톱밥냄새를 느낀다는 결과를 나타내었으며 전체적인 종합적 풍미는 국산 건강엑기스가 좋은 것으로 나타났다.

• Journal of the Korean Society of Marine Environment & Safety
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• v.24 no.1
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• pp.92-100
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• 2018

Vortical systems are considered a main feature to sustain turbulence in a boundary layer through interaction. Such turbulent structures result in frictional drag and erosion or vibration in engineering applications. Research for controlling turbulent flow has been actively carried out, but in order to show the effect of vortices in a turbulent boundary layer, it is necessary to clarify the mechanism by which turbulent energy is transferred. For this purpose, it is convenient to demonstrate and capture phenomena in a laminar boundary layer. Therefore, in this study, the interactions of disturbed flow around a hemisphere on a flat plate in laminar flow were analyzed. In other words, a street of hairpin vortices was generated following a wake region formed after flow separation occurred over a hemisphere. Necklace vortices surrounding the hemisphere also appeared due to a strong adverse pressure gradient that brought high momentum fluid into the wake region thereby leading to an increase in the frequency of hairpin vortices. To mitigate the effect of these necklace vortices, local suction control was applied through a hole in front of the hemisphere. Flow visualization was recorded to qualitatively determine flow modifications, and hot-film measurements quantitatively supported conclusions on how much the power of the hairpin vortices was reduced by local wall suction.

• Journal of the Korean Ceramic Society
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• v.34 no.2
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• pp.131-138
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• 1997

Silicon carbide films were chemically vapor deposited onto graphite substrates using MTS(Ch3SiCl3) as a source and Ar or H2 as a diluent gas. The experiments were performed at a fixed condition such as a de-position temperature of 130$0^{\circ}C$, a total pressure of 10 torr, and a flow rate of 100 sccm for each MTS and carrier gas. The purpose of this study is to consider the variation of the growth behavior with the addition of each diluent gas. It is shown that the deposition rate leads to maximum value at 200 sccm addition ir-respective of diluent gases and the deposition rate of Ar addition is faster than that of H2 one. It seems that these characteristics of deposition rate are due to varying interrelationship between boundary layer thick-ness and the concentration of a source with each diluent gas addition, when overall deposition rate is con-trolled by mass transport kinetics. The preferred orientation of (220) plane was maintained for the whole range of Ar addition. However, above 200 sccm addition, especially that of (111) plane was more increased in proportion to H2 addition. Surface morphologies of SiC films were the facet structures under Ar addition, but those were gradually changed from facet to smooth structures with H2 addition. Surface roughness be-came higher in Ar, but it became lower in H2 with increasing the amount of diluent gas.