• Proceedings of the Korean Nuclear Society Conference
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• 1995.05a
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• pp.759-764
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• 1995

여러 가지 Zr합금의 부식거동을 LiOH, NaOH, KOH, RbOH, CsOH 용액조건에서 autoclave를 이용하여 조사하였다. 용액내의 알칼리 농도는 0.3mmol 4.3mmol 31.5mmo1를 선택하였는데, 이는 Li의 경우에 2.2ppm 30ppm, 220ppm에 해당되는 농도이다. Zr합금은 ZrSn-TRM(천이원소)과 ZrSnNb-TRM(천이원소)의 두 종류의 합금을 사용하였다. 알칼리 분위기에서 Zr함금의 부식을 지배하는 이온은 양이 온인 것으로 밝혀졌으며, 양이온의 반경이 Zr합금의 천이전 영역에서의 부식을 지배하는 것으로 나타났다. Nb첨가 합금은 Zircaloy형 합금보다 내식성이 떨어진다. LiOH가 부식을 가장 가속시키는 알칼리로 밝혀졌으며 CsOH나 KOH는 거의 Zr합금의 부식을 가속시키지 않는다. 따라서 CsOH나 KOH는 PWR에 적응 가능한 대체 알칼리로서 가능성을 보였다.

• Transactions of the Korean Society of Mechanical Engineers A
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• v.40 no.9
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• pp.767-773
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• 2016

A Weibull statistical analysis of the mechanical properties of SiC ceramics was carried out by immersion in acidic and alkaline solutions. The heat treatment was carried out at 1373 K. The corrosion of SiC was carried out in acidic and alkaline solutions under KSL1607. The bending strength of corroded crack-healed specimens decreased 47% and 70% compared to those of uncorroded specimens in acidic and alkaline solutions, respectively. The corrosion of SiC ceramics is faster in alkaline solution than in acid solution. The scale and shape parameters were evaluated for the as-received and corroded materials, respectively. The shape parameter of the as-received material corroded in acidic and alkaline solutions was significantly more apparent in the acidic solution. Further, the heat-treated material was large in acidic solution but small in alkaline solution. The shape parameters of the as-received and heat-treated materials were smaller in both acidic and alkaline solutions.

• Proceedings of the Korean Nuclear Society Conference
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• 1998.05b
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• pp.136-141
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• 1998

재결정된 Zircaloy-4 합금을 35$0^{\circ}C$ 의 여러가지 알칼리 금속 수산화물 수용액에서 부식시켜 동일한 무게증가량을 갖도록 조절한 뒤, 1M H$_2$SO$_4$ 용액에서 그 시편에 대한 임피던스 특성을 분석하였다. LiOH, NaOH, KOH 순서로 알칼리 금속의 이온반경이 클수록 수소이온의 이동에 대한 임피던스가 증가함에 따라 산화막을 통한 수소이온의 흡수가 점차로 어려워졌다. 이것은 Zr$^4$$^{+}$와 이온반경이 비슷한 알칼리 금속 수용액 조건에서 얻은 부식시편은 open grain boundary 와 equiaxed microstructure의 산화막을 갖기 때문이었고, 반면에 Zr$^4$$^{+}$와 이온반경의 차이가 큰 알칼리 금속 수용액 조건에서 얻은 부식시편은 compact 한 columnar microstructure의 산화막을 갖기 때문인 것으로 생각된다.

• Journal of the Korean Electrochemical Society
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• v.2 no.3
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• pp.117-122
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• 1999

This study investigated the corrosion rate of aluminum in alkaline solution. It was performed to observe the effects of alloy element, alkalinity (KOH concentration), solution temperature, and inhibitor and its concentration in the solution. Among species of aluminum, AA-1050 showed the lowest corrosion rate due to its high purity $(>199\%)$, whereas alloys containing Mg anuor Mn were highly corroded, relatively. The corrosion rate could be reduced over than $50\%$ by saturating the solution with ZnO, while ZnAc did not work as an inhibitor. The inhibition effect of ZnO increased with increasing the alkalinity and solution temperature. It was found that the corrosion rate linearly increased with the concentration of KOH in first order and exponentially decreased with the inverse of the solution temperature. An analysis of the corroded material covered the surface of aluminum was made by SEM and EDS. According to the analytical results by using XRD, it was confirmed that $Al(OH)_3$ was produced from the corrosion of aluminum in KOH solution.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.4
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• pp.661-669
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• 2000

This research was carried out to evaluate effect of metallic release and change of water corrosive indices by the pH and alkalinity adjustment using the SDLS (Simulated Distribution Loop System) which consist of six types of pipe loop with DCIP, PVC, PE, STS304, CP, GSP, respectively, and its effects on water quality changes which were microbes quality(SPC), residual chlorine. THMs and other parameters. And it was to propose optimal criteria of water quality control for the field application. According to the results, water control system by pH and alkalinity adjustment showed the changing of corrosive water and reducing of metallic release rate and it was not affects of THMs formation, microbes regrowth and variation of other parameters. Water quality stability and corrosion control were due to calcium carbonate precipitation film formation of pipe inner by water quality control. Therefore, corrosive water control system by pH and alkalinity adjustment can be attributed to effective water quality management in water distribution system according to water quality stability of pH and TIC(Total Inorganic Carbonate concentration) that affect the precipitation and dissolution of solids.

• Journal of Korean Society of Water and Wastewater
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• v.20 no.2
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• pp.215-223
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• 2006

The internal corrosion of water distribution systems is the main cause for the problem of the public health threat as well as water leakage in the damaged pipeline, red water, and odor and taste of the tap water. This study was examined the effect of chemicals used for pH and alkalinity control and corrosion inhibitors for producing the optimal corrosion control method. Corrosion study at different pH and alkalinity indicated that these control using alkaline chemicals was effective in corrosion rate, Fe release reduction, but examined to be increased in turbidity and corrosion-by-products(TTHMs) problems. The turbidity was slightly increased, requiring caution in controlling corrosion with $Ca(OH)_2$. At pH 9.0, TTHMs concentration is increased two times corn pared with non-control of pH. Using the pipe which had experienced 28 years of exposure, iron release was decreased with the corrosion inhibitor. Consequently, pH, Alkalinity control method using alkaline chemicals must be complemented by corrosion inhibitor application for efficient corrosion control.

• Clean Technology
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• v.24 no.4
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• pp.339-347
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• 2018

In order to cope with environmental problems and climate change caused by fossil fuels, renewable energy supply is increasing year by year. Currently, waste energy accounts for 60% of renewable energy production. However, waste has a lower calorific value than fossil fuels and contains various harmful substances, which causes serious problems when applied to power generation boilers. In particular, the chlorine in the waste fuel increases slagging and fouling of boiler heat exchangers, leading to a reduction in thermal efficiency and the main cause of high temperature corrosion, lowering facility operation rate and increasing operating cost. In this study, the high temperature corrosion experiments of superheater materials (ASME SA213/ASTM A213 T2, T12 and T22 alloy steel) by alkali chlorides were conducted, and their corrosion characteristics were analyzed by the weight loss method and SEM-EDS. Experiments show that the higher the temperature and chloride content, the more corrosion occurs, and KCl further corrodes the materials compared to NaCl under the same condition. In addition, the higher the chromium content of the material, the better the corrosion resistance to the alkali chlorides.

• Journal of Korean Society of Environmental Engineers
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• v.27 no.4
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• pp.362-368
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• 2005

The pH, alkalinity and calcium hardness could be adjusted by $CO_2$, $Ca(OH)_2$, and $Na_2CO_3$ addition in the water treatment process for corrosion protection of the water pipes. This research was performed to investigate the effect on the variation of water quality on the unit process by addition $CO_2$, $Ca(OH)_2$, and $Na_2CO_3$ in water treatment process. Carbon dioxide and lime were added before the coagulation basin and soda ash was added after the BAC process. pH and aklainity were increased at coagulation basin then after the water qualities had sustained similiarly to BAC process. There was no effect on turbidity and DOC removal efficiency during experimental period by addition\ $CO_2$, $Ca(OH)_2$, and $Na_2CO_3$ solution was added into clear well, the last process for optimum control of CCPP and is used mainly to control pH and alkalinity. In this research, average pH, alkalinity, and calcium hardness in treated water were 8.39, 61.4 mg/L as $CaCO_3$, 59.4 mg/L as $CaCO_3$, respectively and CCPP of treated water was higher than 29.5 mg/L to BAC process water, so adjusted water was expected to prevent internal corrosion of water pipe.

• Journal of Energy Engineering
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• v.11 no.2
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• pp.114-121
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• 2002

Alkali metal compounds existed in original coal or sorbents are exhausted as vapor or small particle at the outlet of combustor when operating PFBC power plant. These compounds can be removed with dust removal equipment, but total generation efficiency will be decreased because of lower operating temperature of dust removal equipment. Alkali metal contained in vapor phase is initially deposited onto turbine blade results in serious corrosion. The concentration of alkali vapor in the PFBC flue gas is 20∼40 ppm which is dependent on mineral characteristics and composition as well as operating condition of PFBC. However, the allowance limit of alkali metal vapor is assigned as less than 50 ppb for gas turbine when coal or oil is used as fuel. Therefore, alkali metal vapor in PFBC or IGCC process should be removed by solid sorbents to prevent corrosion of turbine blade and improve plant efficiency. In the present investigation, powder of Bauxite, Kaolinite and Limestone is used in the preparation of cylinder-type pellet which is inserted into the pressurized alkali removal reactor for the alkali absorption experiment. Experimental results showed that the alkali removal efficiency in the order of Bauxite, Kaolinite and Limestone. Alkali vapor removal efficiency is related with reaction temperature, porosity of pellet and alkali vapor concentration of flue gas.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2016.11a
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• pp.151-151
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• 2016

수소는 친환경 에너지원으로 주목 받고 있으며 미래 화석연료의 고갈에 대비할 수 있는 물질이다. 수전해는 natural gas steam reforming 또는 coal gasification 같은 방법에 비해 공해 물질의 방출이 없어 미래지향적인 기술로 간주된다. 저온형 수전해는 크게 알칼리 수전해와 고분자 전해질막 수전해로 구분되며 각각의 기술은 장단점을 가지고 있다. 알칼리 수전해는 비백금계 물질을 촉매로 사용할 수 있는 이점이 있으나 알칼리 용액으로 인한 부식, 높은 과전압에 의한 효율저하 그리고 간헐적인 사용에 적합하지 않다. 고분자 전해질막 수전해는 간헐적인 사용이 용이하고 높은 에너지 밀도를 가지지만 산성분위기로 인한 백금계 촉매를 사용해야 하므로 수소 생산 비용이 증가하게 된다. 본 연구에서는 알칼리 수전해와 고분자 전해질막 수전해 방식의 이점을 최대한 이용하고 단점을 극복하기 위한 방법으로 음이온 교환막(anion exchange membrane, AEM)을 적용한 셀 구조를 소개한다. 본문에서는 AEM 수전해 단위 셀의 구성요소들인 AEM 종류, 가스 확산층의 밀도와 운전조건인 알칼리 수용액 농도, 온도의 조건을 다르게 하여 최상의 구성 요소 조건 및 운전조건을 알아보았다.