• 한국태양에너지학회 논문집
• /
• 제22권1호
• /
• pp.9-21
• /
• 2002

To develope chemical heat pump using available energy sources, solar heat and other kinds of waste thermal energy, we have studied the heat transfer rate in cylindrical bed reactor packed with calcined Dolomite. Two dimensional (radial and circumferential) Partial differential equations, concerning heat and mass transfer in packed bed of calcined Dolomite, are solved numerically to describe the characteristics of the reaction of calcined Dolomite and heat transfer. The results obtained by numerical analysis about two dimensional profiles of temperature and conversion of reactant in the packed bed reactor and the amount of exothermic heat released from the reactor are follows. It was found that all of calcined Dolomite packed bed kept the reaction temperature of about 750K throughout the entire part of the bed, immediately after the steam was introduced exothermic reaction of hydration was proceeded from the packed bed inpu to output and from wall side to center. The rate of thermochemical reaction depends on the temperature and concentration and it is also governed by the boundary conditions and heat transfer rate in the particle packed bed.

• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2008년도 추계학술대회B
• /
• pp.2221-2226
• /
• 2008

The objective of this paper is to describe the experimental and numerical investigation of the analysis of the heat transfer in a solar chemical reactor. These are compared about methane steam reforming process in the solar chemical reactor which was a volumetric absorber consisting of honeycomb and a multilayered catalyst supports. With this high operating temperature, convective heat loss, thermal fracture are important features for designing SCR. In order to estimate the system performance and to design the actual solar reactor with various conditions, CFD analysis was used in this study. The nickel oxide porous metal is inserted inside the solar chemical reactor to increase the conversion rate of the reforming reaction. Simulation has been carried out based on the experimental data. According to the simulation results, the optimum methane-steam mole ratio and thickness and numbers of catalyst supports were obtained.

• 공업화학
• /
• 제21권1호
• /
• pp.24-28
• /
• 2010

이산화탄소의 광물고정화는 자연계의 풍화 작용을 모사한 것으로 매우 안정한 반응이지만 반응 속도가 매우 느리다. 이러한 반응 속도 증가를 위하여 광물의 전처리가 필요하다. 본 연구에서는 이산화탄소 광물고정화 속도 증가를 위한 두 가지의 전처리 방법을 소개하고 고정화 효율 증가를 확인하였다. 열적전처리는 $630^{\circ}C$에서 행해지는데, 이는 이산화탄소가 고정화되는 것을 방해하는 사문석 분자 내의 -OH기의 제거한다. FT-IR 피크를 통해 -OH기가 제거되는 것을 확인할 수 있다. 화학적전처리는 사문석 내의 주요 광물고정화 성분인 마그네슘 성분을 $75^{\circ}C$의 추출 온도에서 황산을 이용하여 추출해내는 것이다. 황산의 수소이온이 사문석 내의 결합을 약화시켜 마그네슘이 추출되도록 한다. 이는 ICP-AES와 XRF를 통하여 추출량을 확인하였다. 전처리가 끝난 사문석을 이용하여 이산화탄소 광물고정화 반응을 진행시 열적전처리의 경우 43%의 이산화탄소 고정화 효율을 나타내는데, 전처리를 하지 않았을 때 27%의 효율에 비하여 증가하였음을 확인하였다. 하지만 이 경우 많은 에너지가 소비된다는 단점이 있다. 화학적 전처리의 경우 열적전처리에 비해 45 atm, $25^{\circ}C$라는 비교적 온화한 조건에서 진행되는데, 이산화탄소 고정화 효율도 전처리 전인 24%에서 42%까지 상승하는 것을 확인할 수 있다.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2007년도 추계학술대회 논문집
• /
• pp.424-428
• /
• 2007

In the current most tool using heat and mass balance in a coal gasifier is dependent on commercial code such as STANJAN, CHEMKIN. However, in order to keep the self-reliance technology, it is necessary to develop the original design tool available for comprehension and analysis on the spot. So in this study, its own heat and mass balance program is developed on the assumption that the process in a coal gasifier is adiabatic and quasi-equilibrium. The mass balance is calculated by using the chemical equilibrium principle. Also the heat and mass balance according to main operating factors such as temperature, pressure and O2/Coal ratio, was carried in this tool. This heat and mass balance was verified on the basis of the results simulated in STANJAN, commercial codes using similar logic.

• Nuclear Engineering and Technology
• /
• 제41권8호
• /
• pp.1025-1044
• /
• 2009

Systematic research has been conducted by KAERI to develop a supercritical carbon dioxide Brayton cycle energy conversion system coupled with a sodium cooled fast reactor. For the development of the supercritical $CO_2$ Brayton cycle ECS, KAERI researched four major fields, separately. For the system development, computer codes were developed to design and analyze the supercritical $CO_2$ Brayton cycle ECS coupled with the KALIMER-600. Computer codes were developed to design and analyze the performance of the major components such as the turbomachinery and the high compactness PCHE heat exchanger. Three dimensional flow analysis was conducted to evaluate their performance. A new configuration for a PCHE heat exchanger was developed by using flow analysis, which showed a very small pressure loss compared with a previous PCHE while maintaining its heat transfer rate. Transient characteristics for the supercritical $CO_2$ Brayton cycle coupled with KALIMER-600 were also analyzed using the developed computer codes. A Na-$CO_2$ pressure boundary failure accident was analyzed with a computer code that included a developed model for the Na-$CO_2$ chemical reaction phenomena. The MMS-LMR code was developed to analyze the system transient and control logic. On the basis of the code, the system behavior was analyzed when a turbine load was changed. This paper contains the current research overview of the supercritical $CO_2$ Brayton cycle coupled to the KALIMER-600 as an alternative energy conversion system.

• 수산해양기술연구
• /
• 제55권4호
• /
• pp.411-418
• /
• 2019

In this study, to investigate the effect of physical and chemical properties of butanol on the engine performance and combustion characteristics, the coefficient of variations of IMEP (indicated mean effective pressure) and fuel conversion efficiency were obtained by measuring the combustion pressure and the fuel consumption quantity according to the engine load and the mixing ratio of diesel oil and butanol. In addition, the combustion pressure was analyzed to obtain the pressure increasing rate and heat release rate, and then the combustion temperature was calculated using a single zone combustion model. The experimental and analysis results of butanol blending oil were compared with the those of diesel oil under the similar operation conditions to determine the performance of the engine and combustion characteristics. As a result, the combustion stabilities of D.O. and butanol blending oil were good in this experimental range, and the indicated fuel conversion efficiency of butanol blending oil was slightly higher at low load but that of D.O. was higher above medium load. The premixed combustion period of D.O. was almost constant regardless of the load. As the load was lower and the butanol blending ratio was higher, the premixed combustion period of butanol blending oil was longer and the premixed combustion period was almost constant at high load regardless of butanol blending ratio. The average heat release rate was higher with increasing loads; especially as butanol blending ratio was increased at high load, the average heat release rate of butanol blending oil was higher than that of D.O. In addition, the calculated maximum. combustion temperature of butanol blending oil was higher than that of D.O. at all loads.

• Fibers and Polymers
• /
• 제5권1호
• /
• pp.75-81
• /
• 2004

To obtain high molecular weight (HMW) poly(methyl methacrylate) (PMMA) with high conversion, methyl methacrylate (MMA) was polymerized in suspension using a room temperature initiator, 2,2'-azobis(2,4-dimethylvaleronitrile) (ADMVN), and the effects of polymerization conditions on the polymerization behavior of MMA and the molecular parameters of PMMA were investigated. On the whole, the experimental results well corresponded to the theoretically predicted tendencies. These effects could be explained by a kinetic order of ADMVN concentration calculated by an initial rate method and an activation energy difference of polymerization obtained from the Arrhenius plot. Suspension polymerization at 25℃ by adopting ADMVN proved to be successful in obtaining PMMA of HMW (number-average degree of polymerization (P/sub n/): 30,900-36,100) and of high yield (ultimate conversion of MMA into PMMA: 83-93 %) with diminishing heat generated during polymerization. The P/sub n/ and lightness were higher and polydispersity index was lower with PMMA polymerized at lower temperatures.

• 한국자동차공학회논문집
• /
• 제5권3호
• /
• pp.15-26
• /
• 1997

In this study, the theoretical investigation of the electrically heated catalyst(EHC) for vehicle application has been carried out using the thermal equivalence of EHC system and the data of vehicle tests to meet ultra low emission vehicle(ULEV) standard. To improve the efficiency of EHC system, it is necessary to understand relation between the power, the operating time and the conversion efficiency of EHC system. The relation was found with thermal equivalence of EHC system which considers the power supply to EHC, heat loss, chemical exothermic energy generated by oxidation reaction and net energy coming in via the exhaust gas. From this relation, the limits of needful power and operating time to meet the ULEV standard can be suggested, when the conversion efficiency of catalyst was known.

• 에너지공학
• /
• 제19권3호
• /
• pp.195-202
• /
• 2010

최근 국내 연간 1차 에너지 사용량의 약 30% 이상이 폐열로 손실되어지고 있다. 이러한 현실을 타개하기 위하여, 본 논문에서는 장거리 열수송시 에너지 손실을 최소화할 수 있는 신기술로 화학 열변환을 이용한 장거리 열수송 기술을 채택하여, 화학 열변환에 있어서의 최적조건 도출을 목적으로 하였다. 화학 열변환을 위한 반응에 대해서는 많은 연구와 기술개발이 이루어지고 있으며, 그 중 물질이 안정하고, 값이 저렴하며, 생성물이 가스인 메탄올 분해 합성 반응이 가장 타당한 것으로 판단되었다. 본 연구에서는 장거리 열수송 기술 개발에 필요한 메탄올 분해 합성 반응 촉매를 각각 선정하여, 열수송 시스템 구축을 위한 메탄올 분해 합성 반응의 최적화 조건 도출을 위한 실험 연구를 수행하였다. 메탄올 합성 반응에서는 온도, 압력, $H_2$/CO ratio, 공간 속도, 촉매 형태에 따른 영향을 보았고, 메탄올의 분해 반응에서는 온도, 공간속도, 촉매 형태를 변수로 하여 상압에서 영향을 분석하여 메탄올 분해 합성 반응의 최적화 조건을 제시하였다.

• 제어로봇시스템학회:학술대회논문집
• /
• 제어로봇시스템학회 1989년도 한국자동제어학술회의논문집; Seoul, Korea; 27-28 Oct. 1989
• /
• pp.813-818
• /
• 1989

A two compartmented autoclave reactor for the polymerization of low density polyethylene is analyzed with respect to the effects of heat transfer and operation variables. Each compartment being considered as a completely mixed cell, two CSTRs model is proposed. The system shows various multiplicity features of steady state and periodic oscillatory motions. Heat removal efficiency and initiator supplement appear to have significant effect on the conversion of monomer with the temperature properly maintained, which should be taken into account in the reactor design.