• 한국정밀공학회지
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• 제25권7호
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• pp.116-123
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• 2008

In the fossil power plant, the reliability of the components which consist of the many welded parts depends on the quality of welding. The residual stress is occurred by the heat flux of high temperature during weld process. This decreases the mechanical properties as the strength of fatigue and fracture or causes the stress corrosion cracking and fatigue fracture. Especially, the accidents due to the residual stress occurred at the weld parts of high-temperature and high-pressure pipes and steam headers. Also, the residual stress of the welded part in the recently constructed power plants has been brought into relief as the cause of various accidents. The aim of this study is the measurement of the residual stress using the x-ray diffraction method. The merits of this are more accurate and applicable than other methods. The materials used for the study is P92 steel for the use of high temperature pipe on super critical condition. The variables of tests are the post-weld heat treatment, the surface roughness and the depth from the original surface. The test results were analyzed by the distributed characteristics of the full width at half maximum intensity (FWHM) in x-ray diffraction intensity curve and by the relation of hardness with FWHM.

• 한국태양에너지학회 논문집
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• 제33권6호
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• pp.39-46
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• 2013

This work introduces a simple one-reactor adsorption desalination system that harnesses low temperature heat sources (solar energy, waste heat), which has been experimentally studied to elicit the most suitable design parameters and operating conditions. The design process of the system was divided into three parts to reflect the operating principle of desalination technology with application of adsorption processes. First, the evaporator for the vaporization of saline water was designed, then the reactor for the adsorption and release of the steam, followed by the condenser for condensation of the fresh water. The specific water yield is measured experimentally with respect to the time while controlling parameters such as heat source temperatures, coolant temperatures, system switching and half-cycle operational times. The present system well demonstrates the applicability of silica gel in relation to adsorption technologies that utilize low temperature heat sources ranging from 60 to $80^{\circ}C$, such as solar energy and waste heat.

• Corrosion Science and Technology
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• 제22권5호
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• pp.351-358
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• 2023

Although many thermal power plants use heat recovery systems, high exhaust gas temperatures are maintained due to corrosion at dew points and ash deposits caused by condensate formation. The dew point of exhaust gas is primarily determined by the concentration of SO₃ and steam, and various experiments and calculation equations have been employed to estimate it. However, these methods are known to be less suitable for exhaust gases with low SO₃ concentrations. Therefore, in this study, since the temperature of the exhaust gas is expected to decrease due to the low-load operation of the coal-fired power plant, sulfuric acid condensation and low-temperature corrosion are anticipated. We aimed to conduct a quantitative evaluation to propose ways to prevent damage by limiting operating conditions and improving facilities. The experimental results showed that the corrosion rate increased linearly with rising temperatures at a certain sulfuric acid concentration. Furthermore, variations in sulfuric acid concentrations generated during the current power plant operation process did not significantly affect the dew point, and the dew point of sulfuric acid under these conditions was observed to be between 120 - 130 ℃.

• 한국염색가공학회지
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• 제29권3호
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• pp.115-121
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• 2017

Demands for nylon suede as an artificial leather are increasing due to its functionality and aesthetics. To achieve high value added nylon suede based on green technology, this study was carried out in order to obtain useful data for the nylon suede fabrics with eco-friendly dyeing process by a pad-steam method instead of a dip dyeing process using sulphur black dye to reduce the industrial waste of water. The dyeability of the nylon suede was investigated according to reducing temperatures, dye concentrations, and reducing agent's concentrations. Throughout the results of the CIE $L^*a^*b^*$ and Munsell values, the optimized dyeing conditions of the nylon suede using sulphur black dye are $70^{\circ}C$ of dyeing temperature, 30% o.w.f. of dye concentration, and $9g/{\ell}$ of reduction agent concentration, respectively. Furthermore washing colorfastness, light colorfastness and perspiration colorfastness were achieved in the range of 4-5 grades.

• 한국수소및신에너지학회논문집
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• 제23권4호
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• pp.337-345
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• 2012

To check effects of operating variables on reaction characteristics of WGS catalyst for SEWGS process, water gas shift reaction tests were carried out in a pressurized fluidized bed reactor using commercial WGS catalyst and sand(as a substitute for $CO_2$ absorbent) as bed materials. Simulated syngas(mixed with $N_2$) was used as a reactant gas. Operating temperature was $210^{\circ}C$ and operating pressure was 20 bar. WGS catalyst content, steam/CO ratio, gas velocity, and syngas concentration were considered as experimental variables. CO conversion increased as the catalyst content and steam/CO ratio increased. CO conversion at fluidized bed condition was higher than that of fixed bed condition. However, CO conversion were maintained almost same value within the fluidized bed condition. CO conversion decreased as the syngas concentration increased. The optimum operation condition was confirmed and long time water gas shift reaction test up to 24 hours at the optimum operating conditions was carried out.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.417-423
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• 2007

Oxy-gasification or oxygen-blown gasification, enables a clean and efficient use of coal and opens a promising way to CO2 capture. The coal gasification process of a slurry feed type, entrained-flow coal gasifier was numerically predicted in this paper. The purposes of this study are to develop an evaluation technique for design and performance optimization of coal gasifiers using a numerical simulation technique, and to confirm the validity of the model. By dividing the complicated coal gasification process into several simplified stages such as slurry evaporation, coal devolatilization, mixture fraction model and two-phase reactions coupled with turbulent flow and two-phase heat transfer, a comprehensive numerical model was constructed to simulate the coal gasification process. The influence of turbulence on the gas properties was taken into account by the PDF (Probability Density Function) model. A numerical simulation with the coal gasification model is performed on the Conoco-Philips type gasifier for IGCC plant. Gas temperature distribution and product gas composition are also presented. Numerical computations were performed to assess the effect of variation in oxygen to coal ratio and steam to coal ratio on reactive flow field. The concentration of major products, CO and H2 were calculated with varying oxygen to coal ratio (0.2-1.5) and steam to coal ratio(0.3-0.7). To verify the validity of predictions, predicted values of CO and H2 concentrations at the exit of the gasifier were compared with previous work of the same geometry and operating points. Predictions showed that the CO and H2 concentration increased gradually to its maximum value with increasing oxygen-coal and hydrogen-coal ratio and decreased. When the oxygen-coal ratio was between 0.8 and 1.2, and the steam-coal ratio was between 0.4 and 0.5, high values of CO and H2 were obtained. This study also deals with the comparison of CFD (Computational Flow Dynamics) and STATNJAN results which consider the objective gasifier as chemical equilibrium to know the effect of flow on objective gasifier compared to equilibrium. This study makes objective gasifier divided into a few ranges to study the evolution of the gasification locally. By this method, we can find that there are characteristics in the each scope divided.

• 공업화학
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• 제19권2호
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• pp.157-160
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• 2008

탄화수소 계열의 연료로부터 고순도의 수소를 생산하는 것은 연료전지의 효율적인 운전과 밀접하다. 일반적으로 대부분의 탄화수소 연료에서 수소를 생산하는 과정은 수소, 일산화탄소, 이산화탄소와 수증기 혼합물이 생성되는 개질 과정 및 일산화탄소를 저감하는 전이반응과 선택적 산화반응 과정으로 구성되어 있다. 전이반응은 일산화탄소를 이산화탄소로 전환하는 동시에 수소가 생성되는 고온 전이와 저온전이로 구성된 두 단계의 촉매전환 공정이다. 일반적으로 개질기에서 생성된 개질 가스는 고온전이 반응기를 거쳐 일산화탄소 농도를 3~5%까지 저감한다. 본 연구에서는 고온전이 반응기를 설계 및 제작하여 일산화탄소 농도를 2~4%까지 저감하였다. 고온전이 반응에서 철이 첨가한 촉매(G-3C)를 사용하여 부분산화 개질에서 생성된 일산화탄소를 이산화탄소로 전환하였다. 그리고 고온전이 영향인자인 수증기 주입량, 개질 가스 조성, 반응온도, 개질 가스 주입량변화에 대한 연구를 진행하였다.

• 한국응용과학기술학회지
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• 제21권3호
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• pp.225-230
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• 2004

Synthesis gas is a high valued compound as a basic chemicals at various chemical processes. Synthesis gas is mainly produced commercially by a steam reforming process. However, the process is highly endothermic so that the process is very energy-consuming process. Thus, this study was carried out to produce synthesis gas by the partial oxidation of methane to decrease the energy cost. The effects of reaction temperature and flow rate of reactants on the methane conversion, product selectivity, product ratio, and carbon deposition were investigated with 13wt% Ni/MgO catalyst in a fluidized bed reactor. With the fluidized bed reactor, $CH_4$ conversion was 91%, and Hz and CO selectivities were both 98% at 850$^{\circ}C$ and total flow rate of 100 mL/min. These values were higher than those of fixed bed reactor. From this result, we found that with the use of the fluidized bed reactor it was possible to avoid the disadvantage of fixed bed reactor (explosion) and increase the productivity of synthesis gas.

• Korean Chemical Engineering Research
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• 제45권1호
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• pp.17-24
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• 2007

본 연구의 목적은 제지공정에서 건조 실린더의 모델을 규명하고 입력변수들에 대한 공정의 응답 특성을 분석하는 것이다. 모델의 규명은 실제 공장의 운전 데이터에 근거하였는데 건조공정에서는 실린더로 공급되는 수증기의 압력이 주요 변수가 된다. 수증기 응축액으로부터 캔버스로의 열전달 계수는 실린더 및 웹과 펄프의 열 전도도와 운전 데이터에 근거하는 실험식으로 나타낼 수 있음이 밝혀졌다. 실린더 모델은 측정되는 수분함량과 웹 온도를 이용하여 검증하였으며 건조 공정의 안정성은 실린더 모델로부터 얻은 전달함수로부터 확인하였다.

• 한국식품과학회지
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• 제23권1호
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• pp.76-80
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• 1991

미강유 정제 부산물로부터 오리자놀을 분리하기위해, dark oil과 dark oil의 증류잔류물인 pitch로부터 용매분리법 이용하여 오리자놀을 분리하였다. 분리과정 중 방해물질인 왁스분은 dark oil과 acetone을 1 : 1(w/v)로 혼합하여, $0^{\circ}C$에서 침전시켜 제거하였고, 여기에서 얻어진 dewaxed dark oil에 8 part의 hexane을 섞어 저온분리하여 오리자놀함량이 51.3%인 농축물을 얻었다. 이 농축물에 methanol 20 part를 가하고 재결성하여 98.3%의 오리자놀결정물을 얻었다. Dark oil로부터 pitch를 제조하는 적정조건은$180^{\circ}C$와 $0.2{\sim}0.4torr$의 진공상태에서 2%(w/w)의 steam을 가하는 증류조건이 오리자놀의 파괴를 최소화 하였다. 이로부터 얻어진 pitch의 오리자놀순도와 회수율은 27.3%와 82.3%였다. Pitch에 hexane을 가하고 저온분리하여 오리자놀순도가 75.4%인 오리자놀결정물을 얻었으며 이 농축물에 methanol을 가한 후 재결정하여 순도가 99%인 결정물을 얻었다. 이상과 같은 저온윤리법을 이용하였을 때 오리자놀의 회수율은 dark oil 9.5%, pitch 28.5%로 나타났다.