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이재성,고광국,Lee, Chai-Sung,Koh, Kwang-Gook 대한화학회 1961 대한화학회지 Vol.5 No.1
A small size Fischer-Tropsch Catalyst testing apparatus, designed for an operating pressure of 150 psig, was test fabricated from ordinary schedule 40 iron pipes. The operability of the apparatus was tested by charging the reactor tube with the Lurgi Fischer-Tropsch iron Catalyst and passing through it the water gas obtained by gasifying the Korean anthracite using steam and oxygen. With the kind of catalyst charged, the apparatus was proven to daily produce about 50c.c. of synthetic greasy product, water and water soluble compounds, by running at a temperature of $250^{\circ}C$ and at a space velocity of 180 volume of gas per volume of catalyst/hr. About 20 consecutive days of operation is claimed to be sufficient for gathering an enough amount of synthetic products for such ordinary tests as distillation analysis, density measurement, iodine value determination etc. This trial fabrication of apparatus may be the first case of its kind in Korea in that the work has been conducted out in much a pilot plant scheme rather than a routine laboratory way which depends on small glass ware apparatus.
이재성,김영우,Lee, Chai-Sung,Kim, Yeong U. 대한화학회 1962 대한화학회지 Vol.6 No.1
The water gas shift conversion catalyst prepared by the American Cyanamide Co. was subjected to fluidization in a 2-in. Pyrex glass tube to obtain the basic fluidization characteristic data. The size of the catalyst charged ranged from 70 to 120 meshes and it was supported on a single layer 300-mesh wire gauze through which the fluidizing medium, the air, was passed. Following are some data and facts found by the authors: (1) The catalyst particles were porous, and their surfaces were trough and irregular. (2) The average effective particle density and the average shape factor of these particles were 152.2 lb/$ft^3$ and 0.865 respectively. (3) As the particle diameter of the catalyst increased, the minimum fluid voidage of the bed decreased slightly. (4) Just before the incipient fluidization, pressure drop suddenly fell and the bed expanded simultaneously. (5) After fluidization set in, the expansion characteristics of the catalyst bed were similar to those of sand and glass beads except intense bubbling in the catalyst bed.
無煙炭의 反應成에 關한 硏究 (第1報) 反應成 試驗藏置의 試作
한태희,이재성,신성식,Hahn, Tae-Hee,Lee, Chai-Sung,Shin, Sung-Sik 대한화학회 1962 대한화학회지 Vol.6 No.1
The "reactivity" of coal is one of the important characteristics of a coal used as a process raw material as well as a fuel. In this study, the reactivity was measured in terms of the magnitude of the reaction rate constant in the reduction of carbon dioxide with coal. A reactivity-testing apparatus was designed and constructed, and its performance characteristics were investigated by using Korean anthracite and hard-wood charcoal. Experiments were carried out at temperatures ranging from 750 to 1100$^{\circ}C$ with pulverized Korean anthracite whose sizes range from 1 to 10mm in diameter. Results showed that the reaction rate constant was not appreciably affected by the particle size investigated, and the reactivities of the anthracite and the charcoal were found to be a function of reaction temperature alone. It was also found that a straight line was produced when the logarithm of the rate constant is plotted against the reciprocal of the absolute temperature. The reactivities of the charcoal were found to be 2 to 10 times higher than those of the anthracite at a temperature ranging from 750 to 1100$^{\circ}C$, and 90% of carbon dioxide was reduced to carbon monoxide by the anthracite at a temperature above 1050$^{\circ}C$.
상변화물질을 충전한 수평원통관 내에서 응고시 열전달특성
염성배(Sung Bae Yum),홍창식(Chang Shik Hong),이재성(Chai-sung Lee) 한국태양에너지학회 1991 한국태양에너지학회 논문집 Vol.11 No.2
본 연구에서는 용융된 파라핀을 채운 수평 원관의 관벽을 냉각할 때에 관 내에서 일어나는 열전달현상을 다루었다. 관내의 파라핀을 고상과 액상으로 구분하여 고상층에 대해서는 열전도 모델을, 그리고 액상층에 대해서는 자연대류를 고려한 열전달모델을 세워 수치해석하였고 이 과정에 대한 실험을 행하여 얻은 응고형태로부터 방열량을 계산하였다. 아울러 초기의 용융파라핀의 온도와 관벽의 냉각온도가 응고에 미치는 영향을 고찰하였다.<br/> 방열과정에서 액상파라핀의 응고속도를 결정하는 요인은 관벽의 냉각온도와 초기 액상온도이나 대부분의 액상현열이 응고 초기에 급속히 방출되기 때문에 관벽의 냉각 온도가 지배적인 요인으로 작용하였다. 따라서 방열과정에서의 열전달은 고상층 내의 열전도에 의해서 이루어지게 된다. 실험에서 관찰한 응고형태에서는 상부에 빈 공간이 발견되었다. 이는 초기 액상온도가 응고초기에 급속히 떨어짐으로써 온도에 따른 액상의 밀도차로 인해 생긴 것이다. 고ㆍ액간의 밀도차로 인한 수축현상은 응고과정의 전반에 걸쳐서 고르게 일어나므로 그 영향을 응고형태에서 구별하여 파악하기는 어려웠다.<br/> Fourier수와 고상의 Stefan수를 종속변수로 사용하면 관벽의 냉각온도와 초기액상온도에 무관하게 응고량은 단일곡선으로 표현할 수 있었다. Heat transfer characteristics for heat retrieving processes in a paraffin-filled horizontal circular cylinder was studied. Theoretical and experimental analyses were carried out. In the theoretical analysis, solid and liquid phases were treated separately. Namely, convection for liquid and conduction for solid phase were investigated respectively. The retrieved heat was calculated from the experimentally determined solidified mass. Furthermore, the effects of initial temperature of the liquid and cooling temperature on the heat discharge rate were also studied.<br/> In the heat retrieving process, the governing factor for the solidifying rate is the cooling temperature, because most of the liquid sensible heat is rapidly discharged in the initial stage of solidification. Hence heat transfer mechanism during heat retrieving process can be safely considered as conduction. In the cut of frozen paraffin, there showed an empty space in the upper region. It is caused by the temperature drop in the liquid paraffin. While volume shrinkage caused by phase transition was indiscernible.<br/> Irrespective of cooling temperature and initial liquid temperature, solidified mass was well-correlated with the product of Fourier number and Stefan number in the solid phase.