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염화알미늄수화물의 부분열분해에 의한 PAC ( Polyaluminum Chloride ) 응집제 제조
박균영,이규철,김진권,( Kyun Young Park,Kyu Chul Lee,Jin Kwon Kim ) 한국화학공학회 1994 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.32 No.5
Presented is a new method of manufacturing PAC(polyaluminum chloride) used as flocculant for water treatments : PAC is obtained through partial decomposition of aluminum chloride hexahydrate at 180℃ to give basic aluminum chloride followed by dissolving the basic chloride in water. With varying the extent of decomposition, properties of the solid-state basic chloride and the PAC solution were analyzed. The IR analysis showed that at an extent of decomposition of 33.4% an absorption band appeared at 980 ㎝^(-1) indicating the formation of basic aluminum chloride. The basicity of the PAC solution was observed to increase with increasing the extent of decomposition. In order to meet the basicity of 45% required for commercial grade PAC, it was found necessary to have an extent of decomposition higher than 45%. According to the NMR analysis, both [Al(H₂O)_6]^(3+) monomer and aluminum chloride polymers were present in the PAC solution. The molar ratio of the polymers to the monomer increased with an increase in the extent of decomposition. The PAC manufactured by the present method was tested on the water taken from the Kum river.
박균영 ( Kyun Young Park ) 한국화학공학회 1996 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.34 No.2
According to the classical model, one or two iron atoms may be enough to form a critical nucleus in the production of iron powders by reducing ferrous chloride with hydrogen. In. the present work, the nucleus size was calculated using the atomistic model and compared with that by the classical model. For a supersaturation ratio of 500,000, the number of iron atoms constituting a critical nucleus was calculated to be 1.32 with the classical model and 48.1 with the atomistic model. The dependency of the nucleus size on the supersaturation ratio was relatively less with the atomistic model. In the calculation of critical nucleus size of materials like iron, the vapor pressure of which is very low, it would be desirable to use the atomistic model, rather than the classical model.
박균영 ( Kyun Young Park ),이미선 ( Mi Sun Lee ),김민철 ( Min Cheol Kim ),이찬희 ( Chan Hee Lee ),박회경 ( Hoey Kyung Park ),강태원 ( Tae Won Kang ),정해성 ( Hae Seong Jeong ),한경아 ( Kyoung Ah Han ),허원회 ( Weon Hoe Huh ),유지 한국화학공학회 2013 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.51 No.3
직경 25 mm의 파이렉스 튜브 내에서 실리콘의 유동층 염소화 반응이 수행되었다. 반응기에 공급되는 질소 유량0.8~1.0 L/min, 염소 유량 0.2 L/min, 반응온도 450℃, SiCl4 응축기의 냉매온도는 -5℃로 설정하였다. 반응기에 도입되는 가스 내 염소의 몰분율이 증가하면 SiCl4의 수율이 증가하였다. 반응가스 중 염소의 몰분율 0.2의 조건에서 SiCl4의 수율은 28% 이었다. 염소의 몰분율 증가는 반응열 상승에 의해 반응온도 상승을 가져옴으로써 안전을 고려하여 염소의 몰분율을 0.2 이상으로 올리지 못했다. 실리콘의 유동층 염소화 반응에 의한 사염화실리콘의 제조 가능성이 입증되 었으며, 향후 보다 가혹한 조건에서의 실용화 연구를 위한 기초로 활용될 수 있을 것으로 기대된다. The chlorination of a metallurgical-grade silicon was carried out in a fluidized bed reactor, 25 mm in diameter. The flow rate of the chlorine admitted into the reactor was 0.2 L/min and that of the carrier nitrogen was 0.8~1.0 L/ min. The reactor temperature was maintained at 450℃ and the temperature of the coolant at the SiCl4 condenser was at -5℃. The SiCl4 yield increased with increasing the mole fraction of chlorine in the feed gas, exhibiting 28% at the mole fraction of 0.2. Further increase of the chlorine mole fraction was not attempted in a worry that the reactor might be failed due to the high exothermicity of the reaction. The production of SiCl4 from silicon by fluidized bed chlorination was demonstrated on a laboratory scale, which is a stepping stone for future studies under more severe conditions toward industrial application.
에어로졸 마이크로반응기에 의한 Titanium Tetraisopropoxide로부터 TiO<sub>2</sub> 나노입자 제조
최재길,박균영,Choi, Jae Gil,Park, Kyun Young 한국화학공학회 2005 Korean Chemical Engineering Research(HWAHAK KONGHA Vol.43 No.5
$1{\mu}l$ 정도의 미량 titanium tetraisopropoxide(TTIP)를 주사기를 사용하여 1 cc 부피의 증발관에 주입하여 기화시킨 후 질소에 의해 직경 4 mm, 길이 35 cm의 관형 에어로졸반응기로 운반하여 열분해 시킴으로써 30-300 nm 크기의 $TiO_2$ 나노입자를 제조하였으며, 반응온도 및 TTIP 증기 농도가 생성된 $TiO_2$ 입자의 형상, 크기, 결정성 등에 미치는 영향을 조사하였다. 전구체 증기 농도 1 mol%에서 반응온도를 300, 500, $700^{\circ}C$로 변화시킨 결과 반응온도가 증가함에 따라 응집체를 구성하고 있는 1차 입자 크기가 감소하였고, $700^{\circ}C$에서는 입자 크기분포가 bimodal 형태를 나타내었다. 반응온도를 $700^{\circ}C$로 유지하고 전구체 증기 농도를 1, 3.5, 7 mol%로 변화시킨 결과 전구체 증기 농도 3.5 mol% 이상에서는 1 mol%에서 관찰되었던 bimodal 분포가 사라지고 응집체 내 1차 입자들의 개수가 상대적으로 많이 증가하였다. 반응온도 및 전구체 농도가 입자의 형상, 크기분포에 미치는 이와 같은 영향들을 이전의 연구결과들과 함께 비교 분석하였다. $TiO_2$ particles, 30-300 nm in diameter, were prepared by thermal decomposition of titanium tetraisopropoxide (TTIP) using an aerosol microreactor, by which about $1{\mu}l$ of the liquid precursor is injected into an evaporator, 1 cc in volume, and vaporized precursor is then transported by nitrogen as a bolus to a tubular reactor 4 mm in diameter and 35 cm in length. Investigated were the effects of the reactor temperature and the concentration of TTIP vapor on the morphology, particle size distribution and crystalline structure of produced $TiO_2$ particles. With TTIP vapor concentration kept constant at 1 mol%, the reactor temperature was varied from 300 to 500 and $700^{\circ}C$. The primary particle size decreased with increasing the temperature, and the size distributions were mono-modal at 300 and $500^{\circ}C$, but bi-modal at $700^{\circ}C$. The TTIP vapor concentration was increased from 1 to 3.5 and 7 mol%, holding the reactor temperature at $700^{\circ}C$. The bi-modal distribution seen at the concentration of 1 mol% disappeared and the number of particles composing an agglomerate increased at the higher concentrations. These effects of the reactor temperature and the precursor concentration were discussed in comparison with experimental results reported earlier.
실리콘 웨이퍼 절단공정(切斷工程)에서 발생(發生)하는 실리콘 카바이드 슬러지로부터 철(鐵), 실리콘 제거(除去)
박회경,고봉환,박균영,강태원,장희동,Park, Hoey Kyung,Go, Bong Hwan,Park, Kyun Young,Kang, Tae Won,Jang, Hee Dong 한국자원리싸이클링학회 2013 資源 리싸이클링 Vol.22 No.2
실리콘 슬러지로부터 원심분리에 의해 1 단계로 실리콘(Si)을 분리 한 후 남게 되는 실리콘 카바이드(SiC) 농축물 내에 포함되어 있는 철과 잔존하는 실리콘을 추가적으로 제거함으로써 실리콘 카바이드의 순도를 향상 시킬 수 있는 가능성을 탐색해 보았다. 실리콘 카바이드 농축물을 대상으로 하여 염산(HCl)/수산화나트륨(NaOH)에 의한 액상 침출법과 염소 가스에 의한 기상 염소화법을 비교해 보았다. 실리콘 카바이드 농축물을 1 M 염산 수용액에서 $80^{\circ}C$에서 1 시간 동안 침출시킴으로써 회수된 실리콘 카바이드에 잔류하는 철의 농도를 49 ppm 까지 제거하였으며, 1 M 수산화나트륨 수용액에서 $50^{\circ}C$에서 1 시간 동안 침출시킴으로써 실리콘 카바이드 내 잔류하는 실리콘의 농도를 860 ppm 까지 제거하였다. 기상 염소화 반응은 직경 2.4 cm, 길이 32 cm의 전기로에 의해 가열되는 알루미나 튜브의 중심에 실리콘 카바이드 농축물을 위치시키고, 질소와 염소의 혼합가스를 흘려보내는 방식에 의해 이루어졌는데, 반응온도 $500^{\circ}C$, 반응시간 4 시간, 가스유량 300 cc/min, 염소 몰분율 10%의 조건 하에서 실리콘 카바이드 내 철과 실리콘의 잔류 농도를 48 ppm과 405 ppm 까지 낮출 수 있었다. In the present study, the possibility of recovering and recycling the silicon carbide(SiC) from a silicon sludge by removing Fe and Si impurities was investigated. Si and SiC were separated from the silicon sludge using centrifugation. The separated SiC concentrate consisted of Fe, Si and SiC, in which Fe and Si were removed to recover the pure SiC. Leaching with acid/alkali solution was compared with the vapor-phase chlorination. The Fe concentration removed in the SiC was 49 ppm, and it was separated by leaching with 1 M HCl solution at $80^{\circ}C$ for 1 h. The Si concentration removed in the SiC was 860 ppm, and it was separated by leaching with 1M NaOH solution at $50^{\circ}C$ for 1 h. The SiC concentrate was chlorinated in a tubular reactor, 2.4 cm in diameter and 32 cm in length. The boat filled with SiC concentrate was located at the midpoint of the alumina tube, then, the chlorine and nitrogen gas mixture was introduced. The Fe and Si concentration removed in the SiC were 48 ppm and 405 ppm, respectively, at $500^{\circ}C$ reactor temperature, 4 h reaction time, 300 cc/min gas flow rate, and 10% $Cl_2$ gas mole fraction.