• Journal of the Korean Society of Food Science and Nutrition
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• v.17 no.2
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• pp.85-94
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• 1988

This experiment was carried out to obtain the basic data for removal the astringency and off-flavor in soybean milk, by means of soaking of soybean in NaOH and $NaHCO_3$ solutions. The changes of phenolic compounds in soybean during soaking were investigated with HPLC and also the changes of flavor and sensority of soybean milk, prepared from soaked soybean were studied. Phenolic compounds of soybean were identified as chlorogenic, p-hydroxybenzoic, p-coumaric, ferulic and gentisic acid and, chlorogenic acid content was greater than the others. The chlorogenic acid of soybean was mainly neutral type and the other compounds were almost acidic type. Up to 85% of the chlorogenic acid was removed by soaking of soybean in 0.1% of NaOH solution for 8 hrs. Phenolic compounds of soybean was almost removed by soaking in 0.1% of NaOH solution at $90^{\circ}C$ for 1 hr. Chemical composition of soybean milks prepared from soaking of soybean in water, 0.1% NaOH and 0.5% $NaHCO_3$ solution were similar. Hexanol content of beany flavor in soybean milk was increased by soaking of soybean in NaOH solution, where as hexanal, propanal, pentanal contents were removed up to 60%. Color of soybean prepared from soaking of soybean in NaOH solution at high temperature were deep yellow but were high whiteness in soybean milk prepared from soaking of soybean in water at low temperature. Sensority of soybean milk prepared from soaking of soybean in 0.1% of NaOH solution at $90^{\circ}C$ for 1 hr was more favorable than the others.

• FLOWER RESEARCH JOURNAL
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• v.16 no.1
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• pp.17-22
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• 2008

Four kinds of leaves with different shapes of leaf blade were used as experimental materials to establish an optimum condition for treating leaves to obtain skeleton leaves. Effective concentration and length of soaking time in a hot NaOH solution, which resulted in high valued ornaments, were 60% (v/v) for 50 minutes for Acer buergerianum (palmatifid), 20% (v/v) for 50 minutes for Ilex cornuta (serrate), 20-60% (v/v) for 70 minutes for Quercus mongolia (lobed), and 20-40% (v/v) for 70 minutes for Quercus palustris (parted). Through a series of the process of soaking leaves in a hot NaOH solution, rinsing or brushing to remove mesophyll, drying, and dying, high quality ornaments could be obtained.

• Proceedings of the Korean Nuclear Society Conference
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• 1997.05b
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• pp.201-206
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• 1997

본 연구에서는 Ni-기 합금인 합금 600과 합금 690, Fe-기 합금인 합금 800 및 초내식성 오스테나이트계 스테인리스강인 SR-50A에 대하여 부식 환경의 변화에 따른 특성 평가를 행하였다. 전기화학적 부식 평가는 양극 분극 시험을 통하여 행하였으며 부식 환경은 NaCl, HCI, NaOH(+$Na_2$SO$_4$) 액이었다. 응력 부식 균열 시험으로는 CERT(Constant Extension Rate Test)를 행하였으며 부식환경은 40%NaOH, 40%OH+12%$Na_2$SO$_4$ 용액이었다. CERT시험 후 그 파면을 SEM관찰하여 파괴 양상을 관찰하였다. 각 합금의 양극 분극 특성을 부식 환경에 따라 평가한 결과, 부식 용액의 증류에 따라 서로 다른 분극 거동을 보이고 있는데 산성과 중성 용액에서는 SR-50A가 가장 큰 저항성을 보이는 반면, 강 알카리용액인 NaOH용액에서는 Ni-기 합금의 저항성이 Fe-기 합금의 저항성보다 우수하게 나타났다. 응력 부식 균열 저항성은 전반적으로 Fe-기 합금보다 Ni-기 합금이 우수하게 나타났다. 파단면을 SEM관찰한 결과 합금 800과 SR-50A(tube)는 용액에 관계없이 입내 파괴 모드를 나타내고 있으며, 합금 600과 SR-50A판재는 입계 파괴 양상을 보이고 있다. 또한 가성 용액 중에 $Na_2$SO$_4$를 첨가할 경우, 부식 속도를 가속화시키고 응력 부식 균열 저항성을 감소시키고 있다.

• Resources Recycling
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• v.28 no.2
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• pp.54-61
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• 2019

In order to recover pure alumina from black dross, leaching of mechanically activated black dross with NaOH solution resulted in an aluminate solution containing a small amount of Si(IV). Selective adsorption of Si(IV) onto hydrotalcite was investigated from 5 M NaOH solution where the concentration of Al(III) and Si(IV) was 13000 and 150 mg/L, respectively. Only Si(IV) was selectively loaded onto hydrotalcite, while Al(III) remained in the solution. Effect of the calcination treatment of hydrotalcite and concentration of calcined hydrotalcite and NaOH on the loading of Si(IV) was investigated. Although the loading percentage of Si(IV) was low from 5 M NaOH solution, most of the Si(IV) was removed by adjusting the concentration of NaOH by 48 times dilution with water when the concentration of calcined hydrotalcite was higher than 4.5 g/L. The loading of Si(IV) onto calcined hydrotalcite followed Freundlich adsorption isotherm.

• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 1999.10a
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• pp.99-102
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• 1999

본 연구에서는 대표적인 물리 화학적 토양정화방법인 토양세척기법의 효율증진을 위하여, Fe를 다량 함유한 고농도 윤활유 오염토양을 대상으로 알카리 용액과 산성용액의 세척효율을 비교 검토하고, 과산화수소의 첨가에 따른 세척효율의 향상효과를 알아보았다. 세척용제인 NaOH와 HCl를 이용하여 세척효율 검토 결과 NaOH를 이용한 경우에 약 60% 의 세척효율을 나타냈다. 또한 NaOH 농도에 따른 정화 효율은 각각 0.5% > 1% $\geq$ 2% 순서로 증가하였다. 기존의 세척효율을 향상시키기 위하여 과산화수소를 첨가하고 오염토양의 정화효율을 비교 검토한 결과 NaOH용액에서는 과산화수소의 농도가 증가할수록 정화효율이 증가하였으나 NaOH의 농도증가에 대해서는 큰 영향을 보이지 않았으며, NaOH 3%의 농도에서 과산화수소 1%를 첨가했을 때 85%의 정화효율을 나타냈다. 또한 과산화수소 주입시기에 따른 영향을 검토한 결과 세척 후 과산화수소를 주입한 경우에 정화효율이 높았다. 반면에 HCl의 경우는 HCl의 농도가 증가할수록 정화효율이 증가하였고, 세척하지 않고 과산화수소를 주입한 경우에 정화효율이 증가하였다. 고농도의 윤활유 오염토양의 세척효율을 증진시키기 위한 처리로서 과산화수소의 주입은 NaOH 상태에서 그 효율이 약 15%정도 증진되었으며, 일정시간에 이르면 정화효율이 평형에 도달하는 것을 알 수 있었다. HCl 상태에서는 25%의 정화효율이 증진되는 것을 알 수 있었다.

• Journal of Korean Society of Environmental Engineers
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• v.22 no.5
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• pp.827-835
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• 2000

Adsorption characteristics of uranium on activated carbon whose surface is modified with $HNO_3$ and/or NaOH were investigated. Na-OAC, which was the activated carbon treated with both $HNO_3$ and NaOH. showed higher adsorption capacity than OAC, which was treated with $HNO_3$, as well as Na-AC, which was treated with only NaOH. This can be explained based on the surface functional groups increased by surface modification of activated carbon and the change of solution pH as adsorption proceeds. From these experimental results, it is thought that the pH of uranium solution and surface functional groups on the activated carbon surface are the governing factors in the uranium adsorption system.

• Journal of the Korean Chemical Society
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• v.16 no.4
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• pp.241-248
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• 1972

The adsorption of Methylene Blue on Yeong-Il bentonite which was treated by aqueous NaOH, $Na_2SO_4 or NaHSO_4 solution respectively, varying concentrations, temperature and time, was studied. In case of treatment with NaHSO_4 solution, slight improvement of the adsorption of Methylene Blue on bentonite was observed. With Na_2SO_4$ solution, the best results obtained when bentonite was treated with 1 N of the solution for 2hr at $100^{\circ}C$, and the adsorption capacity of the product was 3 times better than that of original bentonite. At the higher concentration and the higher temperature than above, faujasite was formed. With NaOH solution, the best condition was in 1N solution for 1hr at $100^{\circ}C$ and the adsorption capacity of the product was 3.3 times better than that of original bentonite. At the higher concentration of the treating agent and at the higher temperature than above, hydroxysodalite was formed.

• Korean Chemical Engineering Research
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• v.49 no.6
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• pp.810-815
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• 2011

Concentrated water discharged from seawater desalination process contains a high concentration of $Na^+$ ion. Electrolysis was applied to synthesize NaOH solution from the highly concentrated NaCl solution. The effect of various operating parameters of composited laboratory-scale chlor-alkali (CA) membrane cell was investigated. The operating parameters such as membrane types (CIMS and Nafion membranes), pretreatment of the membrane, flow rate (73 mL/min~200 mL/min), initial $Na^+$ ion concentration (1.5 M, 3M and 5 M) and current (1.5A and 2A) were evaluated. It was observed that synthesis efficiency of NaOH solution with CIMS membrane was higher than that with Nafion membrane, but the durability of CIMS membrane on $Cl_2$ gas was poor. The synthesis efficiency of NaOH solution increased with increasing initial $Na^+$ ion concentration and current, while the efficiency decreased with increasing flow rate using Nafion membrane.

• Journal of the Mineralogical Society of Korea
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• v.5 no.2
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• pp.61-71
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• 1992

Through the low-temperature(60-150${\circ}C$) hydrothermal treatment of perlite with the alkaline solution at various NaOH concentrations, the mode of volcanic glass alteration and resultant zeolite formation were investigated in a closed system. At a temperature of 80${\circ}C$ and alkalinities of pH range 8 to 12, corresponding to the natural environments of diagenetic zeolite formation, only weak dissolution of perlitic glass occurs without zeolite formation despite the residence time of 100 days. Activities of Si and Al increase progressively, as a consequence of increasing pH, whereas activity ratios of Si/Al decrease. Zeolites were synthesized from perlite in the alkaline solution at above 0.1M NaOH concentrations. Below the temperature of 100${\circ}C$ Na-P was mainly formed, whereas analcime was the dominant zeolite at the temperature range of 100-150${\circ}C$. During Na-P synthesis chabazite and Na-X were also formed as by-products in case of lower proportion of solution/sample(<10ml/g) and higher NaOH concentraion (>3M), respectively. The alteration modes of perlite in the zeolite synthesis reflect that the formation of synthetic zeolites occurs as an incongruent dissolution likely with the diagenetic formation of natural zeolites from volcanic glass. Considering much difference in reaction kinetics between natural and synthetic systems, however, the evaluated synthetic conditions in these experiments were not directly applicable to the natural diagenetic system.

• Applied Chemistry for Engineering
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• v.10 no.8
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• pp.1104-1108
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• 1999

In this study it was focused that if the chrome could be removed in the shaving dust, the reusable protein resource could be recycled from the shaving dust. As the chrome forms a Cr-collagenate by cross linking of collagen in the shaving dust, the dust was steeped for swelling and plumping by $Ca(OH)_2$ solution and then chromium in dust was resolved out by $H_2SO_4$ solution in the first stage process. In the second stage one, dust was swelled and plumped by NaOH solution and then the chromium in dust was oxygenated to a hexavalent chrome, which has high solubility in $H_2O_2$ solution. And then the chromium was removed byt he steeping of $H_2SO_4$ solution as the last process. The first stage process was consisted of the sequential steeping of 3%-$Ca(OH)_2$ and $0.8%-H_2SO_4$. In the second stage the total chrome was effectively removed by the sequential steeping of 0.1%-NaOH, $3%-H_2O_2$ and $1%-H_2SO_4$. In the completely dechromated dust, the humidity was measured as 10.68% and the crude protein was contained by 79.81%. Steeping solutions were reused 3 times for chrome removal process, the chrome was entirely removed in shaving dust.