• 한국추진공학회지
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• 제22권1호
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• pp.1-6
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• 2018

아임계 및 초임계에서 액체질소 분류의 온도가 분사기 내부와 세 개의 축방향 하류 위치(0.9, 10.6, 28.1d)에서 열전대를 이용하여 측정되었다. 액체질소는 공급라인과 분사기를 냉각하며 분사되므로, 분류의 온도는 시간에 따라 감소한다. 이때 챔버와 분사기 사이에 분사 차압이 존재하므로, 아임계에서 분류는 감압비등에서 비등 그리고 비등이 일어나지 않는 상태로 변화한다. 초임계에서 가짜끓음이 존재함에 착안하여, 가짜 감압비등의 존재에 대해 가정하였으며, 실제로 초임계에서도 아임계와 유사하게 일정 온도 영역에서 하류에서 온도의 변화가 없는 구간이 확인되었으며, 이를 바탕으로 가짜 감압비등이 존재할 수 있음을 보였다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2017년도 제48회 춘계학술대회논문집
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• pp.803-810
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• 2017

초임계 조건에서의 연소반응에서는 액체산소가 초임계 상태로 천이되며 스도보일링과 급격한 물성치변화를 발생시킨다. 이때 초임계 상태에서 작동하는 분사기의 연소반응은 급격한 밀도차로 인한 난류확산에 의해 지배되며, 따라서 스도보일링과 함께 발생하는 확산유동에 대한 연구가 필요하다. 많은 연구자들에 의해 초임계 연소해석에서 발생하는 이 현상들에 대한 연구가 진행되었지만 다양한 변수들에 의한 사례연구가 부족한 상태이다. 본 연구에서는 초임계 압력조건에서 산화제-연료비(O/F)와 연소기 직경, 리세스비를 통해 재순환유동 및 액체산소코어 길이에 변화를 주어 이로 인한 유동구조 및 화염구조의 변화를 수치적으로 연구하였다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2017년도 제48회 춘계학술대회논문집
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• pp.709-712
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• 2017

극저온 액체 질소가 초임계 상태에서 분사될 때 역광기법(backlight method)을 이용하여 사진을 얻었다. 이 때, 유체의 온도를 함께 측정하였고, 이를 바탕으로 가짜 감압비등이라는 새로운 분열기구를 제안하고자 하였으나, 역광기법은 정성적인 분무의 외관은 보여주지만 분사되는 유체의 큰 밀도로 인하여 밀도 변화를 보여줄 수 없었다.

• 대한화학회지
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• 제13권2호
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• pp.149-156
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• 1969

$NaAl(OH)_2CO_3$was synthesized using colloidal earth (Allophane) as the starting material and some of its were studied in detail. It was found that Dawsonite was formed in the pH range (pH 12.5~12.0) that the concentration of $HCO_3^-$ was just begun to increase and the presence of $HCO_3^-$ in the product was clarified from the infrared absorption spectrum. The chemical formular of Dawsonite was therefore presumed as $NaAlO (OH) HCO_3$. From toahhe results of X-ray powder diffraction, both peaks at 5.7 $\AA$ and 2.8 $\AA$ were observed, and fibrous crystalline structure was observed from electron micrograph and also found from the microscopic electron diffraction at 5.7 $\AA.$ Therefore the fibrous axis was considered as =Al=O2=Al=O2=Al=(*image) direction. True specific gravity of Dawsonite was 2.44 and its porosity was 91.4%. It was practically insoluble in water, but decomposed in the boiling water to form Pseudo Boehmite. Stable pH range of Dawsonite was about 4.5~11.5. From the results of D.T.A. and T.G.A., it was observed that $CO_2$was liberated at $350^{\circ}C$, and $H_2O$ at $650^{\circ}C$, and converted into strongly hygroscopic $NaAlO_2$, which was easily decomposed in water into $\beta-Al(OH)_3(Bayerite)$ and NaOH.

• Journal of Mechanical Science and Technology
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• 제17권10호
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• pp.1507-1519
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• 2003

The two-phase flow patterns for both non-loop and loop type oscillating capillary tube heat pipes (OCHPs) were presented in this study. The detailed flow patterns were recorded by a high-speed digital camera for each experimental condition to understand exactly the operation mechanism of the OCHP. The design and operation conditions of the OCHP such as turn number, working fluid, and heat flux were varied. The experimental results showed that the representative flow pattern in the evaporating section of the OCHP was the oscillation of liquid slugs and vapor plugs based on the generation and growth of bubbles by nucleate boiling. As the oscillation of liquid slugs and vapor plugs was very speedy, the flow pattern changed from the capillary slug flow to a pseudo slug flow near the annular flow. The flow of short vapor-liquid slug-train units was the flow pattern in the adiabatic section. In the condensing section, it was the oscillation of liquid slugs and vapor plugs and the circulation of working fluid. The oscillation flow in the loop type OCHP was more active than that in the non-loop type OCHP due to the circulation of working fluid in the OCHP. When the turn number of the OCHP was increased, the oscillation and circulation of working fluid was more active as well as forming the oscillation wave of long liquid slugs and vapor plugs in the OCHP. The oscillation flow of R-142b as the working fluid was more active than that of ethanol and the high efficiency of the heat transfer performance of R -142b was achieved.

• Nuclear Engineering and Technology
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• 제36권6호
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• pp.528-539
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• 2004

It is essential in commercial reactors that the safety limits imposed on the fuel pellets and fuel clad barriers, such as the linear power density (LPD) and the departure from nucleate boiling ratio (DNBR), are not violated during reactor operations. In order to accurately monitor the safety limits of current reactor states, a detailed three-dimensional (3D) core power distribution should be estimated from the in-core detector signals. In this paper, we propose a calculation methodology for detailed 3D core power distribution, using in-core detector signals and core monitoring constants such as the 3D Coupling Coefficients (3DCC), node power fraction, and pin-to-node factors. Also, the calculation method for several core safety parameters is introduced. The core monitoring constants for the real core state are promptly provided by the core design code and on-line MASTER (Multi-purpose Analyzer for Static and Transient Effects of Reactors), coupled with the core monitoring program. through the plant computer, core state variables, which include reactor thermal power, control rod bank position, boron concentration, inlet moderator temperature, and flow rate, are supplied as input data for MASTER. MASTER performs the core calculation based on the neutron balance equation and generates several core monitoring constants corresponding to the real core state in addition to the expected core power distribution. The accuracy of the developed method is verified through a comparison with the current CECOR method. Because in all the verification calculation cases the proposed method shows a more conservative value than the best estimated value and a less conservative one than the current CECOR and COLSS methods, it is also confirmed that this method secures a greater operating margin through the simulation of the YGN-3 Cycle-1 core from the viewpoint of the power peaking factor for the LPD and the pseudo hot pin axial power distribution for the DNBR calculation.