• 대한설비공학회지:설비저널
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• 제12권4호
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• pp.252-263
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• 1983

In the briquet-burning hot water boiler the $SO_x$-dew point is calculated and found to be between $130^{\circ}C\;and\;154^{\circ}C$. The corrosion rate depends on the surface temperature and the concentration of the condensate on the surface. The concentration of the condensate is decided acoording to the difference detween $SO_x$-dew point and the surface temperature. When the surface temperature is $80^[\circ}C$, the concentration of the condensate is also high (0.15N). Therefore the high concentration and high temperature promote the high corrosion rate of $14{\times}13^{-3}g/100cm^2{\cdot}hr$ on the SS41 material. On the other hand, when the surface temperatures are $60^{\circ}C\;and\;40^{\circ}C$, the concentrations and the co..sion rates are reduced dramatically to $0.11\;N,\;8.6{\tiems}10^{-3}g/100cm^2{\cdot}hr$ and $5{\tiems}10^{-4}g/100cm^2{\cdot}hr$ respectively.

• Nuclear Engineering and Technology
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• 제56권3호
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• pp.1091-1099
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• 2024

Fluoride-salt-cooled High-temperature Reactor (FHR) is a promising nuclear reactor technology. Among many challenges presented by the molten fluoride salts is the corrosion of salt-facing structural components. Higher moisture contents, in the FLiNaK (LiF-NaF-KF, 46.5-11.5-42 mol%) salt, aggravate intergranular corrosion and pitting for the given alloys. Therefore, several thermal dehydration tests of FLiNaK salt were performed with a batch size suitable for thermal-hydraulic experiments. Thermogravimetric Analysis (TGA) was performed for the three constituent fluoride salts individually. Preliminary thermal dehydration plans were then proposed for NaF and KF salts based on the TGA curves. However, the dehydration process may not be required for LiF since its low mass loss (<1.3 wt%). To evaluate the performance of these thermal dehydration plans, a batch-scale salt dehydration test facility was designed and constructed. The preliminary thermal dehydration plans were tested by varying the heating rates, target temperature, and holding time. The sample mass loss data showed that the high temperatures (>500 ℃) were necessary to remove a significant amount of moisture (>1 wt%) from NaF salt, while relatively low temperatures (around 300 ℃) with a long holding time (>10 h) were sufficient to remove most of the moisture from KF salt.

• Nuclear Engineering and Technology
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• 제28권1호
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• pp.79-92
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• 1996

방사성폐기물 처분후 처분장내에서는 금속의 부식과 셀룰로스 물질의 미생물 분해에 의한 기체가 발생하게 된다. 이 논문에서는 금속부식과 미생물 분해에 의해 발생되는 기체의 발생률을 예측하는 수학적 모델을 검토하고, 그로부터 저준위 방사성폐기물 처분장에 대한 기체 발생률을 예측하여 보았다. 금속성 물질의 부식은 3단계로 일어나며 그중 마지막 단계에서 H$_2$가 발생하게 된다. 셀룰로스 물질의 미생물 분해는 8가지 형태의 박테리아에 의해 일어나는 화학반응에 따라H$_2$, $CO_2$, CH$_4$등이 발생하게 되는데 이는 처분장내의 pH 및 몇몇 화학종의 농도에 따라 반응률이 결정되게 된다. 이 논문에서는 처분후 약10,000년 동안 발생되는 주요 기체의 발생률 및 누적발생 량을 예측하여 보았다. 평가 결과, 중저준위 방사성폐기물 처분장내에서 발생되는 기체는 H$_2$가 가장 많이 발생되는 것을 알 수 있었다.

• 한국표면공학회지
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• 제50권6호
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• pp.531-535
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• 2017

Enormous amount of waste oyster-shell (OS) has a major disposal problem in coastal regions. OSs have attracted much attention for recycling, because these are mainly composed of calcium carbonate with rare impurities. In this study, we demonstrate the calcareous deposit films on steel plate by using OSs on the basic of cathodic protection technique. The composition of the OSs was analyzed by wavelength dispersive X-ray fluorescence spectrometer. Carbon dioxide gas was pumped into distilled water to make carbonic acid solution for dissolution of OS. The calcareous deposit was characterized by second electron microscope (SEM), energy dispersive X-ray analysis (EDX) and X-ray diffraction. Corrosion rates were estimated by measurements of anodic polarization and immersion test. It is confirmed that calcareous deposits on steel plate are formed under all condition of cathodic protection by using waste OS from the SEM and EDX results. Calcareous deposits on steel by OS provide good corrosion resistance by acting as a barrier to oxygen supply to the steel surface.

• 한국수자원학회논문집
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• 제54권8호
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• pp.589-597
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• 2021

본 논문에서는 부식깊이의 실측 데이터를 통해 부식깊이 예측식을 수립하고 상수관망의 노후도 및 안전도 등을 결정할 수 있는 운영인자를 수립하여 실제 관망에 적용하였다. 신뢰성해석과 운영인자 분석을 통해 노후도를 비교·분석 하였다. 신뢰성해석결과 가덕의 직경 200 mm 관의 경우 시간이 경과함에 따라 4.36%, 6.18%, 8.23%로 증가하는 것으로 나타났고 남이의 직경 200 mm 관의 경우 시간이 경과함에 따라 7.35%, 9.51%, 12.99%로 증가하는 것으로 나타났다. 운영인자를 결정하여 방사형 차트 면적을 통해 노후도를 비교한 결과 가덕은 1.009, 남이는 1.174로 남이 지역이 노후도가 큰 것으로 나타났다. 신뢰성해석과 운영인자를 통해 교체 우선순위를 결정할 수 있었다.

• 생물환경조절학회지
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• 제24권4호
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• pp.333-340
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• 2015

간척지 내 토양은 염분농도 및 함수비가 일반지역에 비해 상당히 높기 때문에 간척지에 매입된 온실의 부재는 높은 부식 환경에 노출된다. 염해의 환경에서는 파이프 골조로 이루어진 온실의 기초 및 기초와 이어진 파이프에 부식을 촉진시키기 때문에 이에 대한 보수/보강기술개발 및 효율적인 유지 관리가 필요하다. 본 연구에서는 염해의 위험성이 높은 간척지에 적합한 온실의 유지관리, 보수/보강에 대한 기준을 마련하기 위한 기초자료로서 토양염분환경에서 온실부재의 부식속도를 측정하였다. 각 온실파이프는 염분농도가 0%, 0.1%, 0.3% 및 0.5%인 토양 및 수중환경에 관찰기간동안(480일) 노출시켜 부식속도를 측정하였으며, 그 결과 육안으로도 염분 농도에 따른 부식정도의 차이가 뚜렷하게 관찰되었으며, 시험편의 표면이 검은색의 부식현상과 함께 비교적 고르게 부식되는 균일부식의 형태를 나타내었다. 논토양의 경우 염분농도 0, 0.1, 0.3, 0.5%에서 각각 0.008, 0.027, 0.036, $0.043mm{\cdot}yr^{-1}$로 염분농도가 증가할수록 부식속도가 뚜렷하게 증가하는 경향을 나타내었고 밭토양의 경우, 염분농도 0, 0.1, 0.3, 0.5%에서 각각 0.0002, 0.039, 0.040, $0.039mm{\cdot}yr^{-1}$의 부식속도를 나타내었다. 상대적으로 세립질이 많은 논토양에서 부식속도가 더 높은 것으로 나타났으며, 이는 입경이 작고 고르게 분포하는 토양에서 부식속도가 높은 일반적인 특성이 그대로 반영된 것으로 판단되었다. 간척지의 경우 토양의 입자의 세립정도는 일반 내륙지역의 농경지 토양보다 높을 것으로 예상되기 때문에 파이프 부식에 대한 철저한 대비가 있어야 할 것으로 판단되었다.

• 한국재료학회지
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• 제14권8호
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• pp.547-551
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• 2004

The sulfidation behaviour of Fe-XAl-0.3Y(X=5, 10, 14, 25 $wt.\%$) alloys was investigated at 1123 K in $H_2/H_{2}S$ gas atmosphere for $1\sim24$ hrs using SEM/EDX, XRD and EPMA. The weight changes of Fe-XAl-0.3Y alloys followed the parabolic rate law, Sulfidation rates of iron aluminide alloys with high Al content were one-twentieth lower than that of 5Al alloys. This is due to the formation of protective $Al_{2}O_3$ oxides on the surface of 10Al, 14Al and 25Al alloys. By calculating partial pressure of impurity oxygen contained $H_2/H_{2}S$ gas, the $Al_{2}O_3$ oxides formation could be explained using Fe-Al-S-O thermodynamic stability diagram. The sulfidation product scales of the 5Al alloy showed that thick iron sulfide scale(FeS) containing porosities formed during early stages of sulfidation. With continued sulfidation, aluminum sulfide was formed at the alloy/scale interface.

• 대한치과보철학회지
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• 제33권3호
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• pp.584-609
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• 1995

The purpose of this study was to evaluate the difference of the galvanic corrosion behaviour of the titanium in contact with gold alloy, silva-palladium alloy, and nickel-chromium alloy using the immersion and electrochemical method. And the effects of galvallit couples between titanium and the dental alloys were assessed for their usefulness as materials for superstructure. The immersion method was performed by measuring the amount of metal elementsreleased by Inductivey coupled plasma emission spectroscopy(ICPES) The specimen of fifteen titanium plates, the five gold alloy, five silver-palladium, five nickel-chromium plates, and twenty acrylic resin plates ware fabricated, and also the specimen of sixty titanium plugs, the thirty gold alloy, thirty silver-palladium, and nickelc-hromium plugs were made. Thereafter, each plug of gold alloy, silver-palladium, and nickel-chromium inserted into the the titanium and acrylic resin plate, and also titanium plug inserted into the acrylic resin plate. The combination specimens uf galvanic couples immersed in 70m1 artificial saliva solution, and also specimens of four type alloy(that is, titanium, gold, silver-palladium and nickel-chromium alloy) plugs were immersed solely in 70m1 artificial sativa solution. The amount of metal elements released was observed during 21 weeks in the interval of each seven week. The electrochemical method was performed using computer-controlled potentiosta(Autostat 251. Sycopel Sicentific Ltd., U.K). The wax patterns(diameter 11.0mm, thickness,in 1.5mm) of four dental casting alloys were casted by centrifugal method and embedded in self-curing acrylic resin to be about $1.0cm^2$ of exposed surface area. Embedded specimens were polished with silicone carbide paper to #2,000, and ultrasonically cleaned. The working electrode is the specimen of four dental casting alloys, the reference electrode is a saturated calmel electrode(SCE) and the ounter electrode is made of platinum plate. In the artificial saliva solution, the potential scanning was carried out starting from-700mV(SCE) TO +1,000mV(SCE) and the scan rate was 75mV/min. Each polarization curve of alloy was recorded automatically on a logrithmic graphic paper by XY recorder. From the polarization curves of each galvanic couple, corrosion potential and corrosion rates, that is, corrosion density were compared and order of corrosion tendency was determined. From the experiments, the following results were obtained : 1. In the case of immersing titanium, gold alloy, silver-palladium alloy, and nickel-chromium alloysolely in the artificial saliva solution(group 1, 2, 3, and 4), the total amount of metal elements released was that group 4 was greater about 2, 3 times than group 3, and about 7.8 times than group 2. In the case of group 1, the amount of titanium released was not found after 8 week(p<0.001). 2. In the case of galvanic couples of titanium in contact with alloy(group 5, 6), the total amount of metal elements released of group 5 and 6 was less than that of group 7, 8, 9, and 10(p<0.05). 3. In the case of galvanic couples of titanium in contact with silver-palladium alloy(group 7, 8), the total amount of metal elements released of group 7 was greater about twice than that of group 5, and that of group 8 was about 14 times than that of group 6(p<0.05). 4. In the case of galvanic couples of titanium in contact with nickel-chromium alloy(group 9, 10), the total amount of metal elements released of group 9 and 10 was greater about 1.8-3.2 times than that of group 7 and 8, and was greater about 4.3~25 times than that of group 5 and 6(p<0.05). 5. In the effect of galvanic corrosion according to the difference of the area ratio of cathode and anode, the total amount of metal elements released was that group 5 was greater about 4 times than group 6, group 8 was greater about twice than group 7, and group 10 was greater about 1.5 times than group 9(p<0.05). 6. In the effect of galvanic corrosion according to the elasped time during 21 week in the interval of each 7 week, the amount of metal elements released was decreased markedly in the case of galvanic couples of the titanium in contact with gold alloy and silver-palladium alloy but the total amount of nickel and beryllium released was not decreased markedly in the case of galvanic couples of the titanium in contact with nickel-chromium alloy(p<0.05). 7. In the case of galvanic couples of titanium in contact with gold alloy, galvanic current was lower than any other galvanic couple. 8. In the case of galvanic couples of titanium in contact with nickel-chromium alloy, galvanic current was highest among other galvanic couples.

• 한국표면공학회지
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• 제50권1호
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• pp.35-41
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• 2017

$TiO_2$, $Al_2O_3$, and $TiO_2-Al_2O_3$ nanolaminated films were grown by atomic layer deposition (ALD) on the 316L stainless steel (SS316L) substrates at a temperature of $150^{\circ}C$. The growth kinetics of $ALD-TiO_2$ and $Al_2O_3$ thin films were systematically investigated in order to precisely control the thickness of each layers in the $TiO_2-Al_2O_3$ nanolaminated films using a high-resolution transmission electron microscopy. And, the exact deposition rates of $ALD-TiO_2$ on $Al_2O_3$ surface and $ALD-Al_2O_3$ on $TiO_2$ surface were revealed to be 0.0284 nm/cycle and 0.11 nm/cycle, respectively. At given growth conditions, the microstructures of $TiO_2$, $Al_2O_3$ and $TiO_2-Al_2O_3$ nanolaminated films were amorphous. The potentiodynamic polarization test revealed that the $TiO_2-Al_2O_3$ nanolaminated film coated SS316L had a best corrosion resistance, although all ALDcoated SS316L exhibited a clear improvement of the corrosion resistance compared with a bare SS316L.

• 설비공학논문집
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• 제3권2호
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• pp.142-151
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• 1991

In the present investigation, it has been proposed to utilize a direct contact heat exchanger as an evaporator to solve the difficulties such as scaling, corrosion and law thermal efficiencies, associated with the conventional evaporator. Liquified nitrozen was utilized as a working fluid to investigate basic natures of bubble dynamics in the evaporator, and spray nozzles were adopted to inject liquified nitrozen into the spray column with varying flow rates of dispersed phase fluids. Experimentations were carried out in the range of $6.54{\times}10^{-4}kg/s$ - 0.030 kg/s for dispersed phase flow rates with one, three and five nozzle holes. Observing the bubble dynamics for the evaporator the feasibility of utilizing a direct contact heat exchanger as a LNG evaporator has been evaluated. The results show that no eruption phenomena was observed in the present investigation with $LN_2$ and the interface between $N_2$ bubbles and water was fully turbulent. It is believed that the high injection velocity of $LN_2$ through the spray nozzles provide good mixing effects for both heat and mass transfers between water and $N_2$ bubbles. Ice was formed on the surface of the spray nozzle for higher $LN_2$ flow rates. However, even in this case, it is observed that the ice was detached as soon as it was formed. Under the present experimental conditions, the shapes of $LN_2$ bubbles were in the spherical-cap region according to the Clift, Grace and Weber Graphs. The height of foam region caused by the breakup of larger bubbles keeps increasing with high injection velocities until it reaches it's maximum height.