• 공업화학
• /
• 제7권4호
• /
• pp.698-706
• /
• 1996

메탄올로부터 HCHO를 생성하기 위하여 연속흐름 장치하에서 알칼리금속이 혼입된 여러가지 실리카-알루미나 촉매상에서 메탄올 탈수소반응을 수행하였다. HCHO의 생성은 촉매상의 Br${\ddot{o}}$nsted산보다는 Lewis산에 의존하였다. 이를 통해 메탄올의 탈수소촉매반응은 전자반응임을 알았고, 실리카-알루미나상의 Br${\ddot{o}}$nsted산은 알칼리금속의 혼입에 의해서 중화되었으며, Br${\ddot{o}}$nsted산의 중화효과는 혼입된 알칼리금속의 전자주게능력(electron-donating capacity)에 따라 다르게 나타났다. 그리고 메탄올 탈수소반응의 활성화에너지는 촉매의 Br${\ddot{o}}$nsted산점이 K에 의해 중화되었을 때 감소하는 경향을 보여주었다.

• 한국가시화정보학회지
• /
• 제14권1호
• /
• pp.57-61
• /
• 2016

We report a finding of fast(exceeding 2,000 K/s) heating of polydimethylsiloxane(PDMS), one of the most commonly-used microchannel materials, under cyclic loadings at high(~MHz) frequencies. A microheater was created based on the finding. The heating mechanism utilized vibration damping of sound waves, which were generated and precisely manipulated using a conventional surface acoustic wave(SAW) microfluidic system, in PDMS. The penetration depths were measured to range from $210{\mu}m$ to $1290{\mu}m$, enough to cover most microchannel heights in microfluidic systems. The energy conversion efficiency was SAW frequency-dependent and measured to be the highest at around 30 MHz. Independent actuation of each interdigital transducer(IDT) enabled independent manipulation of SAWs, permitting spatiotemporal control of temperature on the microchip. All the advantages of this microheater facilitated a two-step continuous flow polymerase chain reaction(CFPCR) to achieve the billion-fold amplification of a 134 bp DNA amplicon in less than 3 min. In addition, a technique was developed for establishing dynamic free-form temperature gradients(TGs) in PDMS as well as in gases in contact with the PDMS.

• Biotechnology and Bioprocess Engineering:BBE
• /
• 제2권2호
• /
• pp.90-93
• /
• 1997

Recombinant exoinulinase was partially purified form the culture supernatant of S.cerevisiae by(NH4)2SO4 precipitation and PEG treatment. The purfied inulinase was immobilized onto Amino-cellulofine with glutaraldeyde as a cross-linking agent. Immobilization yield based on the enzyme activity was about 15%. Optimal pH and temperature of immobilized enzyme were found to be 5.0 and 6$0^{\circ}C$, respectively. The enzyme activity was stably maintained in the pH ranges of 4.5 to 6.0 at 6$0^{\circ}C$. 100% of enzyme activity was observed even after incubation for 24 hr at 6$0^{\circ}C$. In the operation of a packed-bed reactor containing 412U inulinase, dahalia inulin of 7.5%(w/w) concentration was completely hydrolyzed at flow rate of 2.0mL/min at 6$0^{\circ}C$, resulting in a volumetric productivity of 693 g-reducing sugars/L/h. Under the reaction conditions of 1.0mL/min flow rate with 2.5% inulin at 6$0^{\circ}C$, the reactor was successfully operated over 30 days without loss ofinulinase activity.

• 한국표면공학회지
• /
• 제28권3호
• /
• pp.133-141
• /
• 1995

The deposition characteristics of diamond films were investigated for three different substrates : Si, Inconel 600 and steel. Diamond films were prepared by microwave plasma CVD method using $CH_4$, $H_2$ and $O_2$ as reaction gases. The deposited films were analyzed with SEM, Raman spectroscopy and ellipsometer. For Si substrate, diamond films were successfully obtained for most of the deposition conditions used in this study. As the $CH_4$ flow rate decreased and the $O_2$ flow rate increased, the quality of the film was improved due to the reduced non-diamond phase in the film. For Inconel 600 substrate, the surface pretreatment with diamond powders was required to deposit a continuous diamond film. The films deposited at temperatures of $600^{\circ}C$ and $700^{\circ}C$ had mainly diamond phase, but they were peeled off locally due to the difference in the thermal expansion coefficient between the substrate and the deposited films. The films deposited at $500^{\circ}C$ and $850^{\circ}C$ had only the graphitic carbon phase. For steel substrate, all of the films deposited had only the graphitie carbon phase. We speculated that the formation of diamond nuclei on the steel substrate was inhibited due to the diffusion of carbon atoms into the steel substrate which has a large amount of carbon solubility.

• 한국환경과학회지
• /
• 제13권3호
• /
• pp.319-325
• /
• 2004

An experimental study on the preparation of monolithic porous polymers by environmentally friend process in supercritical carbon dioxide has been carried out. Polymerization mixture composed of a cross-linking monomer, initiator and functional co-polymer was charged in the reactor with sapphire window. After the system was purged with a flow of $CO_2$ for 15 min, the reactor was pressurized with liquid $CO_2$ up to 100 bars. The reactor was isolated from and placed back to the system via quick connector for shaking until the mixture had become fully homogeneous. The reactor was then heated and pressurized to the required reaction conditions and left overnight. After cooling and $CO_2$ evacuation, the polymer was removed from the reactor as dry, white, continuous monoliths. The effect of experimental conditions on the physical properties of porous polymer was systematically examined, and it was found that monomer content had a major effect on the physical properties of the polymers.

• International Journal of Safety
• /
• 제1권1호
• /
• pp.58-61
• /
• 2002

A preparation method of cobalt supported alumina catalyst for a emergency escape mask cartridge has been studied. Catalysts were prepared by incipient wetness impregnation method using pre-shaped $\gamma$=alumina powders of 70-100 mesh. The catalyst was tested in a continuous-flow reactor system and characterized by elemental analysis, BET and TGA-DTA techniques. Cobalt shows higher activity than platinum or nickel for carbon monoxide oxidation at room temperature. Optimum loading amount of cobalt was 10 wt.% for CO oxidation and the reaction activity increases gradually with the increase of calcination temperature up to $450^{\circ}C.

• 환경위생공학
• /
• 제13권3호
• /
• pp.141-147
• /
• 1998

Under high temperature and high pressure, cyanogen disinter gration distruction mechanism brought followings results through continuous plug flow reactor system. 1. The temperature was a important reacting factor in cyanogen disintegration. Over $612.8^{\cird}K$ high disintegration rate or 99.99% was shown even under $2000{\;}mg/{\ell}$ cyanogen density. 2. The conditions of cyanogen disintegration was gained through experimenting the supercrietical condition of water in basic. To gain 99.99% disintegration rate under $1000{\;}mg/{\ell}$ early cyanogen density, the pressure showed 52.8 seconds at $523^{\cird}K$ and 84.2 atm and gained $0.56{\;}mg/{\ell}$ operating density. 3. Here is the reaction velocity formula of cyanogen disintegration by hydrolysis: This formula indicates the high possibility of cyanogen disintegration within a short time. And it also implys the potential possibility on treating NBDICOD and the technology in developing the environment cleaning progress as small size automatic controlling equipment.

• Journal of Industrial and Engineering Chemistry
• /
• 제67권
• /
• pp.448-460
• /
• 2018

Copper nanoparticle-doped and graphitic carbon nanofibers-covered porous carbon beads were used as an efficient catalyst for treating synthetic phenolic water by catalytic wet air oxidation (CWAO) in a packed bed reactor over 10-30 bar and $180-230^{\circ}C$, with air and water flowing co-currently. A mathematical model based on reaction kinetics assuming degradation in both heterogeneous and homogeneous phases was developed to predict reduction in chemical oxygen demand (COD) under a continuous operation with recycle. The catalyst and process also showed complete COD reduction (>99%) without leaching of Cu against a high COD (~120,000 mg/L) containing industrial wastewater.

• 한국신재생에너지학회:학술대회논문집
• /
• 한국신재생에너지학회 2008년도 춘계학술대회 논문집
• /
• pp.479-482
• /
• 2008

Since late of 2000, KIER has developed a novel pyrolysis process for production of fuel oils from polymer wastes. It could have been possible due to large-scale funding of the Resource Recycling R&D Center. The target was to develop an uncatalyzed, continuous and automatic process producing oils that can be used as a fuel for small-scale industrial boilers. The process development has proceeded in three stages bench-scale unit, pilot plant and demonstration plant. As a result, the demonstration plant having capacity of 3,000 tons/year has been constructed and is currently under test operation for optimization of operation conditions. The process consisted of four parts ; feeding system, cracking reactor, refining system and others. Raw materials were pretreated via shredding and classifying to remove minerals, water, etc. There were 3 kind of products, oils(80%), gas(15%), carbonic residue(5%). The main products i.e. oils were gasoline and diesel. The calorific value of gas has been found to be about 18,000kcal/$m^3$ which is similar to petroleum gas and shows that it could be used as a process fuel. Key technologies adopted in the process are 1) Recirculation of feed for rapid melting and enhancement of fluidity for automatic control of system, 2) Tubular reactor specially-designed for heavy heat flux and prevention of coking, 3)Recirculation of heavy fraction for prevention of wax formation, and 4) continuous removal & re-reaction of sludge for high yield of main product (oil) and minimization of residue. The advantages of the process are full automation, continuous operation, no requirement of catalyst, minimization of coking and sludge problems, maximizing the product(fuel oil) yield and purity, low initial investment and operation costs and environment- friendly process. In this presentation, background of pyrolysis technology development, the details of KIER pyrolysis process flow, key technologies and the performances of the process will be discussed in detail.

• 전기화학회지
• /
• 제18권1호
• /
• pp.24-30
• /
• 2015

일반적으로 저농도의 염 용액에서 탈염성능이 우수한 축전식 탈염기술에 고농도의 염을 함유한 용액을 처리할 수 있는 가능성을 확인하기 위해 spacer와 spiral 형태의 두 가지 모양의 유로에따라 이온교환수지를 채움으로써 탈염효율을 비교분석하고 기술의 적용가능성을 평가하였다. Spacer와 spiral 형태로 이온교환수지를 채운 축전식 탈염 셀의 탈염효율은 각각 77.21 및 99.94%로, 이는 spiral 형태의 유로에 채워진 이온교환수지가 유입수와 고르게 접촉할 수 있는 유로의 모양을 구성하기 때문에 많은 이온들이 제거될 수 있었다고 판단된다. 또한 pH와 축적 전하량의 변화량에서 탈염성능을 감소시킬 수 있는 페러데이 반응이 현저하게 줄어들었다. 따라서 본 연구를 통해 에너지효율적인 축전식 탈염 기술을 이용하여 고농도의 염 용액의 탈염에 대한 가능성을 제시해주었고, 이온교환수지의 혼합비율의 최적화와 연속식 전기탈이온 기술의 재생공정의 도입에 대한 추가적인 연구를 통해 이상적인 탈염기술을 개발하는 데 큰 기반이 될 것으로 기대된다.