• Proceedings of the Korean Radioactive Waste Society Conference
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• 2012.10a
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• pp.343-344
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• 2012

• Cement
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• s.65
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• pp.42-58
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• 1976

• Korean Chemical Engineering Research
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• v.47 no.4
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• pp.481-487
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• 2009

In this of study, effects of input air velocity(0.05~0.22 m/sec) and molten carbonate salt temperature ($870{\sim}970^{\circ}C$) on flow regime transition have been studied by adopting a drift-flux model of air holdup and a stochastic analysis of differential pressure fluctuations in an air-molten sodium carbonate salt two-phase system(molten salt oxidation process). Air holdup where the flow regime transition begins was determined by air holdup-drift flux plot. The air holdup value which the flow regime transition begins was increased with increasing molten carbonate salt temperature due to the decrease of viscosity and surface tension of molten carbonate salt. To characterize the flow regime transition more quantitatively, differential pressure fluctuation signals have been analyzed by adopting the stochastic method such as phase space portraits and Kolmogorov entropy, The Kolmogorov entropy decreased with an increasing of molten carbonate salt temperature but increased gradually with an increase in an air velocity, however, it exhibited different tendency with the flow regime and the air velocity value which flow regime transition begins was same to the results of drift-flux analysis.

• Journal of Energy Engineering
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• v.8 no.4
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• pp.592-604
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• 1999

The steady state and dynamic characteristics of large cell area MCFC stacks were analyzed to solve the problems such as temperature difference generated in stacks and pressure difference between anode and cathode. Manipulated variables (current density, duel utilization rate, oxidant utilization rate) and controlled variables (temperature difference, anode and cathode pressure difference) which had an important effect on the MCFC stack performance were determined using operation results of two types of MCFC stacks (5kW (3,000 $\textrm{cm}^2$, 20 ea). 3kW (6,000 $\textrm{cm}^2$, 5ea)). The stability and transfer function representing system dynamics were obtained by steady state gain rate which showed the relative change between MVs and CVs. The transfer function was a 3$\times$3 matrix and a typical first order system without time delay. The optimal operating condition of large cell area MCFC stacks could be determined by analyzing dynamic characteristics. In case of a 5 kW MCFC stack, pressurized operation with recycle flow should be used to control the outlet temperature less than 68$0^{\circ}C$ and to control the MCFC system effectively. MIMO control or decoupler should be used to remove the interaction between MVs and CVs. This result will be used as important data in determining the control structure design and operation mode of large cell area MCFC systems in the future.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.10 no.2
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• pp.77-85
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• 2012

This study was carried out to remove (/recover) the uranium from the Uranium-bearing Lime Precipitate (ULP). An oxidative dissolution of ULP with carbonate-acidified precipitation and a dissolution of ULP with nitric acid-hydrogen peroxide precipitation were discussed, respectively. In point of view the dissolution of uranium in ULP, nitric acid dissolution which could dissolved more than 98% of uranium was more effective than carbonate dissolution. However, in this case, uranium was dissolved together with a large amount of impurities such as Al, Ca, Fe, Mg, Si, etc. and some impurities were also co-precipitated with uranium during a hydrogen peroxide precipitation. On the other hand, in the case of carbonate dissolution-acidified precipitation, U was dissolved less than 90%. Therefore, it was less effective than nitric acid dissolution for the volume reduction of radioactive solid waste. However, it was very effective to recover the pure uranium, because impurities were hardly dissolved and hardly co-precipitated with uranium.

• Journal of Korean Society of Environmental Engineers
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• v.36 no.5
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• pp.342-351
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• 2014

The present paper investigates the performance of direct wet mineral carbonation technology to fix carbon dioxide ($CO_2$) from relatively high $CO_2$ concentration feeding gas using wollastonite ($CaSiO_3$)-water (and 0.46 M acetic acid) suspension solution. To minimize the energy consumed on the process, the carbonation in this work is carried out at atmospheric pressure and slightly higher room temperature. As a result, carbon fixation is confirmed on the surface of $CaSiO_3$ after carbonation with wollastonite-water suspension solution and its amount is increased according to the $CO_2$ composition in the feeding gas. The leaching and carbonation ratio of wollastonite-water suspension system obtained from the carbonation with 50% of $CO_2$ composition feeding gas is 13.2% and 10.4%, respectively. On the other hand, the performance of wollastonite-acetic acid in the same condition is 63% for leaching and 1.39% for carbonation.

• Economic and Environmental Geology
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• v.35 no.2
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• pp.121-136
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• 2002

The $CO_2$-rich springs in the Kyungpook Province has been found at 16 locations. Most of the $CO_2$-rich springs outflow along either fault zones or the geologic boundary between Mesozoic granites and their adjacent rocks. The $CO_2$-rich water samples show a high $CO_2$ concentration ( $P_{CO2}0.46 to 5.21 atm), weak acidic pHs, wide electrical conductivity values ranging from 422 to 2,280 $\mu\textrm{S}$/cm, and high re content. They are classified into the ca-HC $O_3$ type in chemical composition.$\delta$$^{18}$ O and $\delta$$^2$H data indicate that $CO_2$-rich water is meteoric origin. The $\delta$$^{13}$ C values (-1.5$\textperthousand$ to -6.1$\textperthousand$ PDB) suggest that dissolved $H_2$C $O_3$$^{0}$ C $O_3$- are mainly derived from a deep-seated $CO_2$ and carbonate minerals. The thermodynamic equilibrium state between $CO_2$-rich water and major minerals, and hydrochemical characteristics indicate that major source minerals determining the chemical composition of $CO_2$-rich water are carbonate minerals, plagioclase, K-feldspar and Fe-oxides. Under high $CO_2$ pressure and the weak acidic condition, most of the $CO_2$-rich water samples are thermodynamically in the dissolution state with respect to albite and carbonate minerals.

• Journal of Energy Engineering
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• v.8 no.1
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• pp.7-13
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• 1999

원형 용융탄산염 단위 연료전지의 성능 및 온도분포가 수치모사를 통해 얻어졌다. 원형 단위전지내에서는 사각형 단위전지에 비해 비교적 균일한 온도분포가 얻어졌다. 전지의 바깥쪽으로 갈수록 가스전환율이 커졌고 전류밀도도 크게 증가하였다. 운전전압이 감소할수록 각 가스들의 전환율은 커지고 전류밀도도 커졌다. 원형 전지에서의 평균전류밀도나 출력은 전압이 높을 때는 사각형 전지보다 작았고, 전압이 낮을 때는 더 컸다. 음극 및 양극 가스의 전환율도 마찬가지였다. 전압이 낮을 때 가스의 전환율이 커서 원형 전지의 효용성이 크게 나타났다.

• 한국전기화학회:학술대회논문집
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• 2001.06a
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• pp.237-242
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• 2001

용융탄산염 연료전지에서 분리판으로 사용되는 316L 스테인리스 스틸의 내식성을 향상시키기 위해 Ni과 Al을 전기도금법에 의해 코팅하였으며 열처리를 통해 스테인리스 스틸표면에 $Ni_2Al_3$, NiAl 등의 금속간화합물을 형성시켰다. $62mol\%Li_2CO_3-38mol\%K_2CO_3$ 전해질 내에서 100시간 동안 침지실험을 수행한 결과 Al의 도금두께가 $10{\mu}m$ 이상인 경우에는 내식성이 상당히 향상되었음을 확인하였다.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 1993.05a
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• pp.87-89
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• 1993

용융탄산염 연료전지 양극 재료인 tape casting된 다공성 Ni-Cr 합금과 Ni-Al 합금의 전기화학적 특성과 소결 및 creep특성이 양극조건의 분위기 $650^{\circ}C$에서 조사되었다. 이들 전극재료의 전류밀도는 100 mV의 과전압에서 약 100~150㎃/$\textrm{cm}^2$의 크기이었다. Ni-Al 합금에서는 Ni 표면에 형성된 $Al_2$O$_3$의 영향으로 소결저항성이 큰 것으로 나타났으며, Creep 특성도 Al 첨가량의 증가에 의해 향상되었다.