• Journal of Hydrogen and New Energy
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• v.18 no.3
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• pp.275-283
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• 2007

본 논문은 세관(ID<7 mm) 내 R-22와 R-134a의 증발 열전달과 유동양식에 대한 실험적 연구이다. R-22와 R-134a의 유동양식을 관찰하기 위해 내경 2와 8 mm의 파이렉스 튜브를 사용하였고, 열전달 계수는 내경 1.77, 3.35, 5.35 mm의 수평 평활동관에 대해서 측정하였다. 증발 유동양식에서 내경 2 mm의 환상류 영역이 내경 8 mm에 비해 저건도 영역에서 발생하는 것을 확인할 수 있었고, 내경 2 mm의 유동양식은 Mandhane의 선도와 많은 오차를 보였다. 세관(ID<7 mm) 내 증발 열전달 계수는 종래의 대구경관(ID>7 mm)에 비해 관직경에 대한 영향이 많이 나타나는 것을 알 수 있었다. 내경 1.77 mm의 열전달 계수는 내경 3.36 mm와 5.35 mm에 비해서 20내지 30% 정도 높은 것을 나타났다. 또한 종래의 열전달 상관식(Shah's, Jung's, Kandlikar's and Oh-Katsuda's correlation)과 비교한 결과, 실험 데이터는 상관식과 많은 이탈 정도를 보였다. 따라서 실험데이타를 기초로 세관내 R-22와 R-134a에 적용할 수 있는 증발 열전달 상관식을 새로이 제안하였다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.20 no.5
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• pp.1725-1734
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• 1996

Experimental condensation and evaporation heat transfer coefficients were measured in a horizontal smooth tube and a horizontal micro-finned tube with HFC-134a. The test sections are straight, horizontal tubes with have a 9.52mm outside diameter and about 5000mm long. The micro-finned tube had 60 fins with a height of 0.12mm and a spiral angle of 25.deg.. The condensation test section was a double-pipe type with counter flow configuration. The evaporation test section employed an electic heating method. Enhancement factors which is defined as a ratio of the heat transfer coefficient for micro-finned tube to that for smooth tube, varied from 1.3 to 1.6(mass flux:110~190kg/m$^{2}$s) for condensation and 1.2 to 1.5 (mass flux:70~160kg/m$^{2}$s) for evaporation. The experimental data of condensation and evaporation heat transfer coefficients were compared to several empirical correlations. Based on these comparisons, modified correlations of the condensation and evaporation heat transfer coefficient for both smooth and micro-finned tubes were proposed.

• Journal of Welding and Joining
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• v.29 no.3
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• pp.64-69
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• 2011

Since welding process for most pipelines with large diameter has been carried out by the manual process, automation of the welding process is necessary for the sake of consistent weld quality and improvement in productivity. Therefore the development of the optimized algorithm to decide the welding condition is an effective technique to prove the feasibility of interface standards and intelligent control technology to increase productivity and reduce the cost of system integration. In this study, the pipe welding experiment has been carried out using plused GMA welding process to select optimal welding condition. And necessary information in root-pass welding has been obtained by applying in the pipeline using the selected welding conditions through the welding experiment.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.26 no.1
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• pp.179-187
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• 2002

Finite element analysis was performed to evaluate the integrity of the tubes in the fixed tubesheet of horizontal type heat exchanger under operating condition. For the finite element analysis of the heat exchanger, tubes and tubesheets were equivalently modeled with concentroidal hexagonal columns and solid plates having equivalent properties for the convenience of finite element modeling, respectively. Load combination of tube pressure and thermal expansion most likely to precipitate possible failure of the tubes was selected and applied to the finite element analysis. The compressive stresses of the tubes were calculated based on displacements of each tube, which were obtained from anile element analysis. Finally, the maximum tube stress was compared with the design criterion of ASME Boiler and Pressure Vessel Code Section VIII.

• Journal of Power System Engineering
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• v.11 no.4
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• pp.44-49
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• 2007

Generally, the economic concept of optimized design and operating conditions in fluidized bed heat exchangers can hardly be realized. Because the lack of fundamental knowledge about the particle flows, the optimum design of the fluidized bed heat exchanger is rather limited. In the present work, measurements are made on pressure drops and friction factors in the horizontal circular tube with solid particles in the circulating water. Two different solid particles of diameters of 3mm and 4mm are covered. The Reynolds numbers are ranged from 10,000 to 45,000. It is concluded that the friction factors for the particles of 4mm diameter are much higher than those for the particles of 3mm diameter. And at the lower particle concentration, the friction factors are strongly influenced by the fluid velocity rather than the particle concentration; However, the effect of the particle concentration on friction factors is also significantly higher at a higher particle concentration operating condition.

• Korean Journal of Veterinary Research
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• v.15 no.2
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• pp.271-277
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• 1975

한국재내산양(韓國在來山羊) 11두(頭)의 흉벽근(胸壁筋)을 절개하여 관찰하였던 바 다음과 같은 결과(結果)를 얻었다. 1. 산양(山羊)의 흉벽(胸壁)에는 횡격막을 포함하여 11개의 筋들을 확인할 수 있었다 : 전배거근(前背鋸筋) M. serratusdorsalis cranialis, 후배거근(後背鋸筋) M. serratus dorsalis caudalis, 사각근(斜角筋) M. scalenus, 늑횡근(肋橫筋) M. transversus costarum, 늑골거근(肋骨擧筋) Mm. levatores costarum, 외늑간근(外肋間筋) Mm. intercostales externi, 내늑간근(內肋間筋) Mm. intercostales interni, 늑연골간근(肋軟骨間筋) Mm. intercartilaginei, 늑골후인근(肋骨後引筋) M. retractor costae, 흉횡근(胸橫筋) M. transversus thoracis, 횡격막(橫隔膜) Diaphragma. 2. 전배거근(前背鋸筋)의 발달이 아주 미약하여 단지 1예(例)에서만 볼 수 있었다. 3. 사각근(斜角筋)은 천부(淺部)(M. scalenus supracostalis)와 심부(深部)(M. scalenus primal costae)로 구분되었으며 이들은 각각 배(背), 복(腹)으로 나누어졌고, 천부(淺部)는 제 1늑골 및 제 3~4늑골에서 기시(起始)하고 있었다. 4. 늑연골간근(肋軟骨間筋)은 제 7늑간에서는 양쪽 늑골이 서로 밀접하게 붙어있어 나타나지 않았으며, 제 1늑간 부터 제 6늑간 사이에서는 섬유방향이 거의 수평으로 향하고 있어 내늑간근(內肋間筋)의 연장으로 보이고 제 8늑간 부터 마지막 늑간사이에서는 거의 수직으로 향하고 있어 외늑간근(外肋間筋)의 연장으로 보인다.

• Proceedings of the KIEE Conference
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• 2002.07d
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• pp.2031-2033
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• 2002

고 배속 광디스크 드라이브(ODD) 시스템에서 위치제어 성능을 향상시키기 위해서는 디스크의 면 진동과 수평 진동과 같은 외란에 의한 오차를 감소 시켜야만 한다. 따라서 하드디스크를 포함한 여러 분야에서 뛰어난 외란 제거 성능을 보이고 있는 외란 관측기는 좋은 대안이 될 수 있다. 그러나 ODD 같은 양산용 전자제품에 외란 관측기를 구현하기 위해서는 별도의 계산 장치가 필요하고, 출력신호를 직접 Feedback 신호로 활용해야 하는 경우가 발생한다. 본 논문에서는 ODD 시스템의 외란을 제거하기 위한 수정된 구조를 가지는 오차를 기초로 한 외란관측기(Error Based Modified Disturbance Observer, EM-DOB)를 제안한다. EM-ROB 시스템은 DOB 시스템에 비해 그 구조가 더욱 간편하고 쉽게 구현 할 수 있다는 장점을 가진다. 그리고 제안한 EM-DOB 시스템의 특성을 연구하고 실험을 통해서 EM-DOB의 효용성을 입증하였다.

• Proceedings of the SAREK Conference
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• 2008.06a
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• pp.154-159
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• 2008

Two-phase flow boiling heat transfer of R-410A in horizontal small tubes was reported in the present experimental study. The local heat transfer coefficients were obtained over a heat flux range of 5 to 40 kW/$m^2$, a mass flux range of 170 to 600 kg/$m^2s$, a saturation temperature range of 3 to $10^{\circ}C$, and quality up to 1.0. The test section was made of stainless steel tubes with inner diameters of 0.5 and 3.0 mm, and lengths of 330 and 3000 mm, respectively. The section was heated uniformly by applying a direct electric current to the tubes. The effects on heat transfer of mass flux, heat flux, inner tube diameter, and saturation temperature were presented. The experimental heat transfer coefficient is compared with six existing heat transfer coefficient correlations. A new boiling heat transfer coefficient correlation based on the superposition model for R-410A in small tubes was developed with mean deviation of 10.13%.

• Transactions of the Korean Society of Mechanical Engineers
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• v.18 no.5
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• pp.1275-1287
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• 1994

Heat transfer performance improvement by fin and grooves is studied for condensation of R-11 on integral-fin tubes. Eight tubes with trapezoidal shaped integral-fins having fin densities from 748 to 1654 fpm and 10, 30 grooves are tested. A plain tube having the same diameter as the finned tubes is also tested for comparison. R-11 condenses at saturation state of $32^{\circ}C$ on the outside tube surface cooled by inside water flow. All of test data ate taken at steady state. Beatty and Katz's, Rudy's and Webb's theoretical models are used to predict the R-11 condensation coefficient of tubes having 748, 1024 and 1299 fpm. The predicted value by Betty and Katz's model is within 10% of experimental values in this study at fpm<1024 and Rudy's model predicted the experimental data at fpm>1024 within 15%. The tube having fin density of 1299 fpm and 30 grooves has the best overall heat transfer performance. This tube shows the overall heat transfer coefficient of 11500 $W/m^{2}K$,/TEX> at coolant velocity of 3.0m/s.

• Journal of Korean Society of Forest Science
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• v.85 no.2
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• pp.325-328
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• 1996

The cultured stain fungus isolated firstly from discolored wood of Pinus rigida was inoculated on wood blocks to investigate the invading pathway of the fungus. The inoculated fungus rapidly colonized in the ray parenchyma and moved radially along them. In process of time the fungus penetrated tracheids where it started to move into vertical direction. After 90 days the fungus colonized all over the wood tissue, therefore some cell lumens were filled with full of hyphae. In addition methanol extracts did not affect the invading pathway of the stain fungus.