• Title/Summary/Keyword: C-flux

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A Study on the Comparison of Chloride Ion Quantification Methods for Magnesium-Aluminum (Mg-Al) Alloy Powder (마그네슘-알루미늄(Mg-Al) 합금 분말의 염소이온 정량법의 비교에 관한 연구)

  • Yunhwan, Kim;Youngson Choe
    • Applied Chemistry for Engineering
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    • v.34 no.4
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    • pp.450-454
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    • 2023
  • Chloride ions in the alloy powder used as flux in Flux Cored Arc Welding (FCAW) can cause pores on the bead surface of the welding metal to cause defects, or chloride remaining in the alloy powder can cause corrosion of the metal. Combustion-ion chromatography is mainly used to quantify the chloride ions in alloy powder, but there is a limitation in that the equipment is expensive and requires a high degree of expertise. Therefore, this study aims to find an easy and accurate quantification method in the field by comparing combustion-ion chromatography (C-IC), which is mainly used for chloride ion quantification of alloy powder, X-ray fluorescence analysis (XRF), and potentiometric titration. In this article, magnesium-aluminum alloy powder is applied to the quantification of chloride ions because it is most commonly used as flux. This study confirmed that potentiometric titration can be applied to the quantification of chloride ions in the alloy powder in the industry field.

Melting Characteristics for Radioactive Aluminum Wastes in Electric Arc Furnace (아크 용융로에서 방사성 알루미늄 폐기물의 용융특성)

  • Min, Byung-Youn;Song, Pyung-Seob;Ahn, Jun-Hyung;Choi, Wang-Kyu;Jung, Chong-Hun;Oh, Won-Zin;Kang, Yong
    • Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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    • v.4 no.1
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    • pp.33-40
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    • 2006
  • The characteristics of the aluminum waste melting and the distribution of the radioactive nuclides have been investigated for the estimation on the volume reduction and the decontamination of the aluminum wastes from the decommissioning of the TRIGA MARK it and III research reactors at the Korea Atomic Energy Research Institute(KAERI). The aluminum wastes were melted with the use of the fluxes such as flux $A:NaCl-KCl-Na_3AlF_6$, flux B:NaCl-NaF-KF, flux $C:CaF_2$, and flux $D:LiF-KCl-BaCl_2$ in the DC graphite arc furnace. For the assessment of the distribution of the radioactive nuclides during the melting of the aluminum, the aluminum materials were contaminated by the surrogate nuclides such as cobalt(Co), cesium(Cs) and strontium(Sr). The fluidity of aluminum melt was increased with the addition of the fluxes, which has slight difference according to the type of fluxes. The formation of the slag during the aluminum melting added the flux type C and D was larger than that with the flux A and B. The rate of the slag formation linearly increased with increasing the flux concentration. The results of the XRD analysis showed that the surrogate nuclide was transferred to the slag, which can be easily separated from the melt and then they combined with aluminum oxide to form a more stable compound. The distribution ratio of cobalt in ingot to that in slag was more than 40% at all types of fluxes. Since vapor pressures of cesium and strontium were higher than those that of the host metals at the melting temperature, their removal efficiency from the ingot phase to the slag and the dust phase was by up to 98%.

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Iontophoretic Delivery of Levodopa: Permeation Enhancement by Oleic Acid Microemulsion and Ethanol (Levodopa의 이온토포레시스 경피전달: 올레인산 아이크로에멀젼 및 에탄올의 투과증진)

  • Jung, Shin-Ae;Gwak, Hye-Sun;Chun, In-Koo;Oh, Seaung-Youl
    • Journal of Pharmaceutical Investigation
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    • v.38 no.6
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    • pp.373-380
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    • 2008
  • In order to develop optimal formulation and iontophoresis condition for the transdermal delivery of levodopa, we have evaluated the effect of two permeation enhancers, ethanol and oleic acid in microemulsion, on transdermal delivery of levodopa. In vitro flux studies were performed at $33^{\circ}C$, using side-by-side diffusion cell and full thickness hairless mouse skin. Current density applied was $0.4\;mA/cm^2$ and current was off after 6 hours application. Levodopa was analysed by HPLC at 280 nm. The o/w microemulsions of oleic acid in buffer solution (pH 2.5 & 4.5) were prepared using oleic acid, Tween 80 and ethanol. The existence of microemulsion regions were investigated in pseudo-ternary phase diagrams. Contrary to our expectation, cumulative amount of levodopa transported from microemulsion (pH 2.5) for 10 hours was similar to that from aqueous solution in all delivery methods (passive, anodal and cathodal). When pH of the micro-emulsion was pH 4.5, cumulative amount of levodopa transported for 10 hours increased about 40% (anodal) to 50% (cathodal), when compared to that from aqueous solution. Flux from pH 4.5 microemulsion showed higher value than that from pH 2.5 in all delivery methods. These results seem to indicate that electroosmosis plays more dominant role than electrorepulsion in the flux of levodopa at pH 2.5. The effect of ethanol on iontophoretic flux was studied using pH 2.5 phosphate buffer solution containing 3% or 5% (v/v) ethanol. Flux enhancement was observed in passive and anodal delivery as the concentration of the ethanol increased. Without ethanol, cathodal delivery showed higher flux than anodal delivery. Anodal delivery increased the cumulative amount of levodopa transported 1.6 fold by 5% ethanol after 10 hours. However, in cathodal delivery, no flux enhancement of levodopa was observed during current application and only marginal increase in cumulative amount transported after 10 hours was observed by 5% ethanol. These results seem to be related to the decrease in dielectric constant of the medium and the lipid extraction of the ethanol, which decrease the electroosmotic flow, and thus decrease the flux. Overall, the results provide important insights into the role of electroosmosis and electrorepulsion in the transport of levodopa through skin, and provide some useful informations for optimal formulation for levodopa.

Errors in Net Ecosystem Exchanges of CO2, Water Vapor, and Heat Caused by Storage Fluxes Calculated by Single-level Scalar Measurements Over a Rice Paddy (단일 높이에서 관측된 저장 플럭스를 사용할 때 발생하는 논의 이산화탄소, 수증기, 현열의 순생태계교환량 오차)

  • Moon, Minkyu;Kang, Minseok;Thakuri, Bindu Malla;Lee, Jung-Hoon
    • Korean Journal of Agricultural and Forest Meteorology
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    • v.17 no.3
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    • pp.227-235
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    • 2015
  • Using eddy covariance method, net ecosystem exchange (NEE) of $CO_2$ ($F_{CO_2}$), $H_2O$ (LE), and sensible heat (H) can be approximated as the sum of eddy flux ($F_c$) and storage flux term ($F_s$). Depending on strength and distribution of sink/source of scalars and magnitude of vertical turbulence mixing, the rates of changes in scalars are different with height. In order to calculate $F_s$ accurately, the differences should be considered using scalar profile measurement. However, most of flux sites for agricultural lands in Asia do not operate profile system and estimate $F_s$ using single-level scalars from eddy covariance system under the assumption that the rates of changes in scalars are constant regardless of the height. In this study, we measured $F_c$ and $F_s$ of $CO_2$, $H_2O$, and air temperature ($T_a$) using eddy covariance and profile system (i.e., the multi-level measurement system in scalars from eddy covariance measurement height to the land surface) at the Chengmicheon farmland site in Korea (CFK) in order to quantify the differences between $F_s$ calculated by single-level measurements ($F_s_{-single}$ i.e., $F_s$ from scalars measured by profile system only at eddy covariance system measurement height) and $F_s$ calculated by profile measurements and verify the errors of NEE caused by $F_s_{-single}$. The rate of change in $CO_2$, $H_2O$, and Ta were varied with height depending on the magnitudes and distribution of sink and source and the stability in the atmospheric boundary layer. Thus, $F_s_{-single}$ underestimated or overestimated $F_s$ (especially 21% underestimation in $F_s$ of $CO_2$ around sunrise and sunset (0430-0800 h and 1630-2000 h)). For $F_{CO_2}$, the errors in $F_s_{-single}$ generated 3% and 2% underestimation of $F_{CO_2}$ during nighttime (2030-0400 h) and around sunrise and sunset, respectively. In the process of nighttime correction and partitioning of $F_{CO_2}$, these differences would cause an underestimation in carbon balance at the rice paddy. In contrast, there were little differences at the errors in LE and H caused by the error in $F_s_{-single}$, irrespective of time.

Study on R-l34a, R-407C, and R-410A Condensation Performance in the Oblong Shell and Plate Heat Exchanger (오블롱 셀 플레이트 열교환기에서의 R-l34a, R-407C, R-410A의 응축성능에 관한 실험적 연구)

  • Park, Jae-Hong;Kim, Young-Soo
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.28 no.12
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    • pp.1535-1548
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    • 2004
  • Condensation heat transfer experiments were conducted with the oblong shell and plate heat exchanger without oil in a refrigerant loop using R-l34a, R-407C and R-410A. An experimental refrigerant loop has been developed to measure the condensation heat transfer coefficient h$_{r}$ and frictional pressure drop $\Delta$p$_{f}$ of the various refrigerants in a vertical oblong shell and plate heat exchanger. The effects of the refrigerant mass flux(40∼80kg/$m^2$s), average heat flux(4∼8kW/$m^2$), refrigerant saturation temperature(30∼4$0^{\circ}C$) and vapor quality of refrigerants on the measured data were explored in detail. Similar to the case of a plate heat exchanger, even at a very low Reynolds number, the flow in the oblong shell and plate heat exchanger remains turbulent. A comparison of the performance of the various refrigerants revealed that R-410A had the highest heat transfer performance followed by R-l34a, and R-407C had the lowest performance of the refrigerants tested. The pressure drops were also reported in this paper. The pressure drops for R-410A were approximately 45% lower than those of R-l34a. R-407C had 30% lower pressure drops than R-l34a. Experimental results were compared with several correlations which predicted condensation heat transfer coefficients and frictional pressure drops. Comparison with the experimental data showed that the previously proposed correlations gave unsatisfactory results. Based on the present data, empirical correlations of the condensation heat transfer coefficient and the friction factor were proposed.tor were proposed.sed.

Investigation on Minimum Film Boiling Point of Highly Heated Vertical Metal Rod in Aqueous Surfactant Solution (계면활성제 수용액 내 고온 수직 금속봉의 최소막비등점에 대한 연구)

  • Lee, Chi Young;Kim, Jae Han
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.41 no.9
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    • pp.597-603
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    • 2017
  • In this study, experiments were conducted on the MFB(minimum film boiling) point of highly heated vertical metal rod quenched in aqueous surfactant solution at various temperature conditions. The aqueous Triton X-100 solution(100 wppm) and pure water were used as the liquid pool. Their temperatures ranged from $77^{\circ}C$ to $100^{\circ}C$. A stainless steel vertical rod of initial center temperature of $500^{\circ}C$ was used as a test specimen. In both liquid pools, as the liquid temperature decreased, the time to reach the MFB point decreased with a parallel increase in the temperature and heat flux of the MFB point. However, over the whole present temperature range, in the aqueous Triton X-100 solution, the time to reach the MFB point was longer, while the temperature and heat flux of the MFB point were reduced when compared with pure water. Based on the present experimental data, this study proposed the empirical correlations to predict the MFB temperature of a high temperature vertical metal rod in pure water and in aqueous Triton X-100 solution.

Pervaporation Separation of Water-Isopropyl Alcohol Mixtures Using PVA/PAN Hollow Fiber Composite Membranes (PVA/PAN 중공사 복합막을 이용한 IPA수용액의 투과증발분리)

  • Kim, Ji Seon;Cho, Eun Hye;Kang, Su Yeon;Cheong, Seong Ihl;Park, Hun Whee;Seo, Chang Hee;Rhim, Ji Won
    • Membrane Journal
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    • v.23 no.2
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    • pp.170-175
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    • 2013
  • Poly (vinyl alcohol) (PVA) solution containing the glutaraldehyde (GA) as a crosslinking agent was coated onto the polyacrylonitrile (PAN) hollow fiber membrane as the supporter. Pervaporation experiments were carried out to characterize the prepared PVA/PAN composite membrane for water-isopropyl alcohol mixture. The flux and separation factor were measured at 30, 50, $90^{\circ}C$ for the feed mixture of aqueous 85 wt% IPA solution with varying the reaction temperature and composition of coating solutions. Typically the flux showed 1,870 $g/m^2{\cdot}hr$ at $90^{\circ}C$ feed mixture and the coating concentration of 3.5 wt% and the highest separation factor of 804 was obtained at $30^{\circ}C$ feed mixture and the coating concentration of 7 wt% as well.

Mechanical and electrical properties of ta-C coating Using the Filtered Vacuum Arc System (FVAS 시스템을 이용한 기계적 및 전기적 특성이 우수한 ta-C 코팅막 형성 연구)

  • Gang, Yong-Jin;Jang, Yeong-Jun;Kim, Jong-Guk
    • Proceedings of the Korean Institute of Surface Engineering Conference
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    • 2016.11a
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    • pp.155-155
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    • 2016
  • DLC (Diamond like Carbon)는 Diamond와 유사한 물리화학적 특성을 보유한 막으로 고경도 및 우수한 내마모성, 화학적 안정성의 특성을 가지고 있다. DLC는 크게 카본의 막 형성 공정에서 카본 소스에 따라 수소가 포함된 DLC와 무수소 DLC 로 구분된다. Tetrahedral amorphous carbon (ta-C) 박막은 DLC 박막 중에서 가장 다이아몬드와 유사한 특성을 가지는 박막으로, a:C-H에 비해 고온안정성, 높은 경도 (30~80 GPa) 및 내마모 특성이 우수하여, 현재 다양한 응용분야에 적용되고 있으며, 최근에는 고내구성을 보유하면서 전기적 특성을 가지는 기능성 DLC막의 요구가 증대하고 있다. 본 연구에서는 무수소 DLC 형성을 위해 자장필터가 장착된 Filtered Vacuum Arc Source (FVAS)를 자체적으로 개발하여 연구를 수행하였다. FVAS 장비는 카본 이온 발생부와 Plasma Duct 부위, 전자석부위 구성되어 있으며, 본 연구에서는 Plasma Duct 부위의 Bias 제어를 통한 음극에서 기판으로 이동하는 카본이온의 에너지 및 flux 변화를 통해 ta-C 막의 전기적, 기계적 물성 연구를 진행하였다. Plasma Duct Bias 변화는 각 0 ~ 20 V 조건으로 진행하였으며, 물성 평가는 경도 (Hardness), 마찰계수, 전기적 특성에 대한 분석을 진행하였다. 박막의 증착 거동에서는 Plasma Duct bias 변화에 따라 10 V에서 가장 높은 증착 거동을 가지다 감소하는 경향을 확인 하였으며, 박막의 물성 특성 평가 시에도 이와 유사하게 특성의 차이를 관찰하였다. 이는 음극부위에서 형성된 카본이온이 기판에 도달 시에 Plasma Duct Bias 변화에 따라 이온의 Flux 및 에너지 변화로 인한 박막의 밀도 및 ta-C 막의 물성 변화로 예상되며, 이를 분석하기 위해 라만 분석법을 통해 증명하였다.

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Pilot Test with Pervaporation Seperation of Aqueous IPA Using a Composite PEI/PDMS Membrane Module (IPA/물 혼합액의 PEI/PDMS 복합막 모듈을 이용한 투과증발 파일롯 분리특성)

  • Cheon, Bong Su;Cheong, Seong Ihl;Rhim, Ji Won
    • Membrane Journal
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    • v.25 no.5
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    • pp.385-390
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    • 2015
  • To determine the pervaporation separation characteristics of IPA/water mixtures, PEI/PDMS hollow fiber membrane module commercialized by Airrane Co. was subjected to both lab and pilot tests. The flux of $0.52kg/m^2h$ and IPA concentration of 68.5% at $25^{\circ}C$ were obtained whereas the $1.368kg/m^2h$ and 61.2% were measured at $55^{\circ}C$. In order to realized the durability of the module, the long-term test (at $50^{\circ}C$) of 100 days has been conducted and as a result, the flux $1.03{\sim}1.15kg/m^2h$ and IPA concentration 61.8~62.5% were maintained with the initial values.

Condensation Heat Transfer Characteristics of Tube-in-Tube Heat Exchanger using Small Diameter Tubes with R-22, R-407C and R-410A (세관을 이용한 Tube-in-Tube 열교환기내 R-22, R-407C 및 R-410A 응축열전달 특성)

  • Park, Woo-Jong;Choi, Kwang-Il;Park, Ki-Won;Oh, Jong-Taek
    • Proceedings of the SAREK Conference
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    • 2006.06a
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    • pp.657-662
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    • 2006
  • The present paper dealt with an experimental study of condensation heat transfer coefficients with refrigerant R-22, R-407C and R-410A, and was focused on pressure gradient and heat transfer coefficient in horizontal tube-in-tube heat exchangers using inner diameter of 4 mm, 3 mm and 2 mm in a 16.91 mm tube and length of 3,000 mm. Experiments were performed at inlet saturation temperature of 35 to $45^{\circ}C$ and mass flux ranges from 200 to $600 kg/m^2s$. The pressure gradient with inner tube diameter of 4.0 mm is higher 2.5 times than that of 8.0 mm. In tube-in-tube HEX, the pressure gradient of R-410A were lower than those of R-22 and R-407C. The condensation heat transfer coefficients increased with mass flux increase, but they decreased with saturation temperature increased. Condensation heat transfer coefficients of R-410A were a little higher than those of R-22 and R-407C. The condensation heat transfer coefficients of tube-in-tube HEX were about 40% higher than those of double tube HEX.

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