• Bulletin of the Korean Chemical Society
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• 제21권1호
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• pp.75-80
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• 2000

The positions of Xe atoms encapsulated in the molecular-dimensioned cavities of fully dehydrated Na-A have been determined. Na-A was exposed to 1050atm of xenon gas at 400 $^{\circ}C$ for seven days, followed by cooling at pressure to encapsulate Xe atoms. The resulting crystal structure of Na-A(7Xe) (a = 12.249(1) $\AA$, $R_1$ = 0.065, and $R_2$ = 0.066) were determined by single-crystal X-ray diffraction techniques in the cubic space group Pm3m at 21(1) $^{\circ}C$ and 1 atm. In the crystal structure of Na-A(7Xe), seven Xe atoms per unit cell are distributed over four crystallographically distinct positions: one Xe atom at Xe(1) lies at the center of the sodalite unit, two Xe atoms at Xe(4) are found opposite four-rings in the large cavity, and four Xe atoms, two at Xe(2) and others at Xe(3), respectively, occupy positions opposite and between eight- and six-rings in the large cavity. Relatively strong interactions of Xe atoms at Xe(2) and Xe(3) with $Na^+$ ions of four-, eight-, and six-rings are observed:Na(1)-Xe(2) = 3.09(6), Na(2)-Xe(3) = 3.11(2), and Na(3)-Xe(2) = 3.37(8) $\AA$. In each sodalite unit, one Xe atom is located at its center. In each large cavity, six Xe atoms are found, forming a distorted octahedral arrangement with four Xe atoms, at equatorial positions (each two at Xe(2) and Xe(3)) and the other two at axial positions (at Xe(4)). With various reasonable distances and angles, the existence of $(Xe)_6$ cluster is proposed (Xe(2)-Xe(3) = 4.78(6) and 4.94(7), Xe(2)-Xe(4) = 4.71(6) and 5.06(6), Xe(3)-Xe(4) = 4.11(3) and 5.32(4) $\AA$, Xe(2)-Xe(3)-Xe(2) = 93(1), Xe(3)-Xe(2)-Xe(3) = 87(1), Xe(2)-Xe(4)-Xe(2) = 91(4), Xe(2)-Xe(4)-Xe(3) = 55(2), 59(1), 61(1), and 68(1), and Xe(3)-Xe(4)-Xe(3) = 89($^{\circ}1$)). These arrangements of the encapsulated Xe atoms in the large cavity are stabilized by alternating dipoles induced on Xe(2), Xe(3), and Xe(4) by eight- and six-ring $Na^+$ ions as well as four-ring oxygens, respectively.

• 한국물환경학회지
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• 제25권4호
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• pp.522-529
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• 2009

To supply safe drinking water to areas lacking in water supply and drainage system, such as rural area and military bases in proximity to Demilitarized Zone, effective method for treating organic contaminants such as MTBE is required. This study focuses on seeking optimal conditions for effective degradation of MTBE using a bath type ultrasound reactor. Effectiveness of MTBE degradation by ultrasound is dependent on the frequency, power, temperature, treatment volume, initial concentration, catalyst, etc. In this study the degradation rate of MTBE by ultrasound was proportional to power/unit volume ratio and removal is relatively more efficient for 0.1 mM than for 1 mM of MTBE solution. Efficiency of ultrasound treatment for 1 mM MTBE solution was enhanced under bath temperature of $30^{\circ}C$ compared to $4^{\circ}C$, but the temperature effect was negligible for 0.1 mM MTBE solution. Also for 0.1 mM MTBE solution, effect of catalyst such as $TiO_2$ and $Fe^0$ on treatment speed was negligible, and zeolite even increases the time taken for the degradation. Under these specific experimental conditions of this study, the most determinant factor for degradation rate of MTBE in solution was frequency and power of ultrasound. The results have shown that a continuous ultrasound reactor system can be used for small scale remediation of organically polluted groundwater, under optimal conditions.

• 한국산업보건학회지
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• 제27권4호
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• pp.291-301
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• 2017

Objectives: In order to improve the working environment and solve the complaints, many efforts have been made to remove the odor from the industrial process. There are many disposal methods to remove odor, but there are many disadvantages and inadequate applications. The Purpose of this study was to develop a bag-filer system for odor removal using powder adsorbent. Methods: The bag-filter system is composed of a shear bag filter, an absorbent spraying system and an absorbent circulation system. The spraying absorbent system was connected with the inlet duct of the shear bag filter for inputting adsorbent. And the absorbent circulation system can transport the collecting adsorbent from hoper to the inlet duct of the system. As a result, the adsorbent can remove odor with recycling in the system. Also affective factors like the powdered absorbent combination and injection method was researched for maximization of system efficiency. The study was conducted in two stages. The first step was testing equipment made and the second is to evaluate the efficiency of the odor control by connecting to the actual odor generation process. Results: Both experiment stages showed efficient odor control ability. The adsorption efficiency of the system is demonstrated and the odor was adsorbed well by the powder adsorbent. It is essential to accurately understand the characteristics of the odorous and use the appropriate adsorbent. Although the powder adsorbent was used in the experiment, the problem of scattering did not occur due to the high degree of system sealing. Also the system manufactured in this study was designed to recycle the adsorbent, so adsorbent reuse or batch processing is convenient. Conclusions: The applicability of the system has been proven through this research. Customized systems for industrial process and the appropriate adsorbent base on the characteristics of pollutant generation will show efficient odor collection ability.

• Korean Chemical Engineering Research
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• 제57권4호
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• pp.565-574
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• 2019

Fischer-Tropsch 합성공정은 합성가스로부터 탄화수소를 합성하는 대표적인 방법이며, 주로 철(Fe)계와 코발트(Co)계 촉매로 알려져 있다. 현재 생성물에 따라 일부 기술(CTL, GTL 등)은 상용 규모로 운전되고 있으나, 경질탄화수소와 중간유분을 직접 생산하는 연구는 아직 상용화되지는 않았다. 그러므로, 본 연구에서는 국내에서 현재까지 경질탄화수소와 중간유분을 직접 생산하기 위한 연구들을 정리하였으며, 촉매의 제조법, 조촉매 첨가, 제올라이트의 조합과 같은 영향이 생성물의 선택도에 미치는 영향을 고찰하였다.

• 공업화학
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• 제4권4호
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• pp.776-784
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• 1993

유기 템플레이트인 $TPA^+$ 이온의 배제 하에 pentasil 계열의 제올라이트인 ZSM-5를 $210^{\circ}C$에서 합성하였다. 본 연구에서 얻어진 결론에 의하면 유기 템플레이트가 사용되지 않는 합성조건 하에서는 기존의 방법으로는 합성이 되지 않는 것을 알 수 있었다. 결과에 의하면 유기 템플레이트 배제 하에서 ZSM-5의 결정화 반응에 적합한 조성영역은 매우 좁고 $Na_2O/SiO_2$및 $SiO_2/Al_2O_3$몰비 조절에 세심한 주의를 요해야 하는 것을 보여주고 있다. 이외에도 ZSM-5 결정화 반응에 미치는 혼합방법, 숙성 및 반응시간의 영향이 매우 큰 것을 알 수 있었다.

• Nuclear Engineering and Technology
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• 제20권2호
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• pp.105-111
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• 1988

과망간산염들, 즉 과망간산 칼륨, 과망간산 암모늄, 과망간산 바륨에서 망간의 중성자 포획으로 야기되는 화학적 효과를 고찰하였다. $^{55}$Mn(n, ｒ) $^{56}$ Mn 반응에서 생성된 방사성 망간 화학종, 즉 양이온 56/Mn, $^{56}$ MnO$_2$ 그리고 $^{56}$ MnO$_4$$^{-}$의 분포에 미치는 용제의 pH효과를 여러 가지 흡착제들과 이온교환체, 즉 제올이프 A-3, 카올리나이트, 알루미나, 이산화망간 그리고 도엑스 -50을 이용하여 고찰하였다. 카올리나이트와 알루미나에서 방사성 MnO$_4$$^{-}$의 분포가 대표적인 pH값인 4, 7 그리고 9 각각에서 다른흡착제와 이온교환체보다 높게 나타나며 동일한 흡착제일경우에는 pH 4 는 및 pH 9에서가 pH 7에서보다 높게 나타난다. $^{55}$Mn(n, ｒ) $^{56}$ Mn 반응에 의하여 과망간산염에서 생성된 반조망간원자들의 열-어니어링 거동 또한 고찰하였다. 열-어니어링에서 $^{56}$ MnO$_4$$^{-}$의 잔류율은 10$0^{\circ}C$ 및 13$0^{\circ}C$ 처리에서 온도가 높아질수록 증가함을 보였다. 망간염의 반조효과는 hot zone model로 설명하였다.

• 한국환경과학회지
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• 제11권3호
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• pp.241-246
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• 2002

One of the Musty and earthy smell compounds in raw water is generally attributed to 2-methylisoborneol (2-MIB). It is well known that activated carbon and oxidants such as $O_3$, Cl $O_2$, are effective ways to control 2-MIB. In isotherm equilibrium experiments, 2-MIB in distilled water was much more adsorbed to the activated carbon(A/C) than raw water containing dissolved organic carbon (DOC). The Freundlich constants(k) of distilled water and raw water were 3.36 and 0.049, and 1/n values were 0.80 and 0.42, respectively. The 2-MIB residual rate were Y = $e^{-0}$.55x/~ $e^{-0}$.54x/ with Ozone( $O_3$) dose by 5 minutes contact time at the 241 and 353 ng/L initial concentrations. The 2-MIB residual rate were Y = $e^{-0}$.32x/~ $e^{-0}$.35x/ with Chlorine dioxide(Cl $O_2$) dose by 15 minutes contact time at the 89 and 249 ng/L initial concentrations. 2-MIB was decreased from 1911 ng/L to 569ng/L by post-ozonation(70%removal efficiency) and removal efficiencies of 2-MIB by the following 4 kinds Granular Activated Carbon(GAC) process such as coal base, coconut base, wood base and zeolite＋carbon base were 95.8, 89.5, 88.4, and 93.7% respectively.ely.

• 자원환경지질
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• 제5권4호
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• pp.221-229
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• 1972

Through the series of study on the above subjects, the following were founded. 1. Soluble silica in paddy top-soil (xppm) and maxium possible yield (y) is expressed as following equatic $y=63.97+0.425x-0.00114x^2$ It is known that soluble silica in paddy top-soil in South Korea is limited as 130ppm. 2. Gnder the present Korean condition 90% of paddy-top-soil is estimated to be short in available silica content and the country average to only 78ppm. 3. The total area of Korean paddy-top-soil is about 1,036,710 ha. All requirements of wollastonite in South Korea estimated from the equation $Y=0.94-0.033{\times}$are about 2 million M/T 4. Silicates fertilizer minerals are Bentonite, Zeolite, Wollastonite, Serpentine, and Chlorite. But Wollastonite is most economic and can be supplied to using Korea. 5. Wollastonite is formed in contact metomorphic deposits. Limestone is the country rock of wollastonite. Limestone in Korea is in Ryunchcon system, (Pre-cambrian) Okcheon system, (unknown), Great limestone series (paleozoic), Hongjum series (Paleozoic) and Kyungsang system (mesozoic) so that the zones of these limestone and igneous rock are the possible area which wollastonite can be produced. 6. According to the published geologic map (scale 1/5000), about 25 provinces will be possible area which wollastonite can be produced. In future, I believe that many possible area will be increased. 7. According to this survey at Danyang, total wollastonite resources are about 179,000 M/T and average of soluble $SiO_2$ is 29.84%. 8. According to this survey at Daijeon, total resources are about 57,600 M/T and average of soluble $SiO_2$ is 21.53%. 9. Total wollastonite resources including Danyang, Yangduk, and Daijeon are about 1,172,200 M/T. Considering possible resources, it will be over 20 million M/T and I can say that it is possible to be supply for a score.

• 공업화학
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• 제29권4호
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• pp.468-473
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• 2018

본 연구에서는 접촉식 가수열분해 반응을 이용하여 원유를 감압증류한 후 생산되는 고점도의 감압잔사유(VR)의 개질반응을 실시하였다. 감압잔사유는 30 bar, $300^{\circ}C$ 이상에서 24 h 동안 수증기(steam)와 반응하면, 구성성분 중에서 레진류와 아스팔텐류가 감소하고, 포화탄화수소류(saturates)나 방향족탄화수소류(aromatics)가 증가하는 경향을 보였다. 이때 스팀 양이 적은 경우에는 가수열분해 반응 후 아스팔텐 함량이 증가되는 역반응 효과도 관측되었다. 수소공여제인 데칼린을 사용하며 메탈옥사이드-제올라이트계 촉매를 사용하는 접촉식 가수열분해 반응 결과 레진과 아스팔텐류가 10% 정도 줄고 방향족 탄화수소류가 10% 증가하면서 점도 감소효과도 70% 정도로 우수하였다. GC-Mass spectroscopy를 이용하여 촉매 사용 시 가수열분해 반응 결과 분자량이 적은 물질로의 분해효과가 우수함을 확인할 수 있었다.

• Bulletin of the Korean Chemical Society
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• 제15권11호
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• pp.940-944
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• 1994

The crystal structure of an ethylene sorption complex of dehydrated $Ag_{12}-A $reacted with bromine vapor has determined by single-crystal X-ray diffraction techniques in the cubic space group of Pm3m at 22(l)$^{\circ}$C (a=12.180(2) ${\AA}$). The crystal was prepared by dehydration of $Ag_{12}$-A at 400 $^{\circ}$C and $2 {\times} l0^{-6}$ Torr for 2 days, followed by exposure to 200 Torr of ethylene gas at 24(l) $^{\circ}$C for 1 hr. After the ethylene gas was evacuated for 1 hr, the crystal was exposed to 180 Torr of bromine vapor at 24(l) $^{\circ}$C for 1.5 h. The structure was refined to the final error indices, $R_1=0.066\;and\;R_2$ (weighted)=0.055, using 137 independent reflections for which I>3${\sigma}$I. About 55% of the sodalite unit contain two 6-ring $Ag^+$ ions and the remaining 45% contain $Ag_6$ molecules complexed to 2 $Ag^+$ ions at 6-ring sites to give $(Ag^+)_2(Ag_6).$ Upon sorption of ethylene, 4.75 ethylene molecules were sorbed per unit cell and of these, only 1.25 ethylene molecules were brominated by treatment of dibromine because of the limitation of the available space for the reaction products in the large cavity. In the large cavity, each of 3.5 $Ag^+$ ions forms a lateral ${\pi}$ complex with an ethylene molecule. About 2.5 8-ring $Ag^+$ ions per unit cell interact with 1.25 1,2-dibromoethane and each of ca. 1.25 6-ring $Ag^+$ ions also interacts with one of bromine atoms of 1,2-dibromoethane. Each bromine atom approaches a carbon atom with C-Br(l)=2.07(20) ${\AA}$ and C-Br(2)=2.07(10) ${\AA}$, respectively.