• Korean Chemical Engineering Research
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• v.54 no.4
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• pp.501-509
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• 2016

The economic feasibility of a commercial indirect liquefaction process with the co-gasification process of petroleum coke which has been recognized as hazardous waste because of high sulfur content and bituminous coal and sub-bituminous coal mixtures was assessed. The 2,000 ton/day scale indirect liquefaction process including co-gasification, clean up, Fischer-Tropsch conversion and so on was assumed and used to analyze economical efficiencies with various conditions. Financial data from previous studies were modified and used and economical sensitivities with various mixture ratios were evaluated in this study. As a result, economic values of petroleum coke were superior than those of coals because of increasing sulfur sale. Also, mixtures with petroleum coke and bituminous coal was more favorable that those with petroleum coke and sub-bituminous coal due to lower moisture content. In case of sub-bituminous coal, the mixture ratio with petroleum coke had to be over 40wt% for the IRR of mixture to surpass 10%.

• Applied Chemistry for Engineering
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• v.21 no.3
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• pp.333-336
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• 2010

Fe/$Al_2O_3$ granules with various compositions were prepared by combining sol-gel with oil drop method for Fishcer-Tropsh reaction to produce light olefin from synthesis gas. The granules was characterized and employed as a catalyst in the reaction. The surface area of granules was decreased with increasing Fe concentration. Especially, granule with 1.5 of Al/Fe ratios showed the highest CO conversion. However, the olefin selectivity was hardly affected by Al/Fe ratio. K concentration of granule gave a significant effect on catalytic performance. Initial CO conversion and olefin selectivity were increased with K concentration. However, the catalyst with higher K concentration was deactivated rapidly.

• Clean Technology
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• v.30 no.3
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• pp.188-194
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• 2024

This study investigates the impact of reduction temperature on the structure and performance of cobalt-manganese (CM) based catalysts in the direct hydrogenation reaction of carbon dioxide (CO₂). It was observed that at a reduction temperature of 350 ℃, these catalysts could successfully facilitate the conversion of CO₂ into long-chain hydrocarbons. This efficiency is attributed to the optimal conditions provided by the core-shell structure of the catalysts, which effectively catalyzes both the reverse water-gas shift (RWGS) and Fischer-Tropsch (FT) reactions. However, as the reduction temperature increased to 600 ℃, the effectiveness of the reaction process was hindered, and there was a shift in selectivity towards methane. This shift is due to the excessive reduction of the catalyst's outer shell, which reduces the number of RWGS sites and subsequently suppresses the production of CO. These findings highlight the importance of carefully controlling the reduction temperature in the design and optimization of cobalt-based catalysts. Maintaining a balance between the RWGS and FT reactions is crucial. This emphasizes that the reduction temperature is a key factor in efficiently generating long-chain hydrocarbons from CO₂.

• Korean Chemical Engineering Research
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• v.50 no.2
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• pp.229-237
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• 2012

Phosphorus was incorporated into Co/$Al_2O_3$ catalyst for FTS by impregnating an acidic precursor, phosphoric acid, in ${\gamma}-Al_2O_3$ support to improve the mechanical strength, the hydrothermal stability of the catalyst particle, and the catalytic performance as well. Surface characterization techniques such as FT-IR revealed that $AlPO_4$ phase was generated on the surface of the P-modified catalyst. The addition of phosphorus was found to alleviate the interaction between cobalt and alumina surface, and to increase reducibility of catalyst. The catalytic activity such as $C_{5+}$ productivity and turnover frequency (TOF) was calculated to evaluate catalytic performance. The influence of calcination temperature of the $Al_2O_3$ containing 2 wt.% P on the catalytic performance was also investigated. Through hydrothermal stability test and XRD analysis, the P-modified catalyst had strong resistant to the pressurized and hot $H_2O$. The mechanical strength of the P-modified catalyst was also examined through an in-house fluidized-bed vessel, and it was found that the catalyst fragmentation could be successfully suppressed with P. Taken as a whole, the best performance was shown to be at 1~2 wt.% P in alumina and at the calcination temperature of $500^{\circ}C$.

• Journal of the Korean Applied Science and Technology
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• v.26 no.3
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• pp.279-287
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• 2009

Fisher-Tropsch synthesis for the production of hydrocarbon from syngas was investigated on 20% cobalt-based catalysts (20% Co/HSA, 20% Co/Si-MMS), which were prepared by home-made supports with high surface areas such as high surface alumina (HSA) and silica mesopores molecular sieve (Si-MMS). In the gas phase reaction by syngas only, 20% Co/Si-MMS catalyst was shown in higher CO conversion and lower carbon dioxide formation than 20% Co/HSA, whereas the olefin selectivity was higher in 20% Co/HSA than in 20% Co/Si-MMS. In the effect of n-hexane added in syngas, the selectivities of $C_{5+}$ and olefin were increased by comparing the supercritical phase reaction with the gas phase reaction in addition to reduce unexpected methane and carbon dioxide.

• 한국도로학회지:도로
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• v.11 no.2
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• pp.26-33
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• 2009

본 특집기사는 미국 NCAT(National Center for Asphalt Technology)에서 실험한 보고서(Hurley 및 Prowell, Evaluation of Sasobit for Use in Warm Asphalt, 2005)를 정리한 것으로 아스팔트 중온포장에 대해 연구하는 사람들에게 어느 정도 도움을 주고자 일부 내용을 번역하였다. 특히, 골재와 바인더 믹싱 및 현장다짐시 온도를 낮추어 궁극적으로 $CO_2$를 저감하고자 하는 노력이 많은 아스팔트 포장관련 종사자 및 연구자들에 의해 활발히 수행되고 있다. 본 기사에서는 중온에서도 작업성을 원활하게 하기 위해 사용되는 많은 첨가제 중 Fischer-Tropsch 왁스인 Sasobit에 대해 살펴보고자 한다. 여기서 관심을 두고자 하는 점은 중온 아스팔트를 실제로 활용할 시 과연 일반 아스팔트 포장과 비교했을 때 어느 정도의 공용성(Performance)을 확보할 수 있느냐 하는 점이다. NCAT의 실내실험을 통해 알아낸 결과로는 진동다짐기를 이용하는 것이 보다 현실적이라는 것과 중온다짐에 따른 아스팔트의 동탄성 계수의 변화가 적다는 것이다. 또한 APA(Asphalt Pavement Analyzer)를 통해 소형변형의 가능성이 높지 않음을 알 수 있었으며, 중온 아스팔트를 사용함에 따른 일반적인 문제점인 수분민감성이 커지는 현상에 대해서 실험을 통해 검증한 결과, 박리방지제를 쓰는 것이 좋다는 결론을 얻었다. 전반적으로 Sasobit의 실내공용성 평가는 우수하다고 보고되고 있다.

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.77.1-77.1
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• 2011

슬러리 기포탑 반응기는 열 및 물질 전달의 용이성, 낮은 운전비용 및 장치의 간단성의 장점을 가지고 있어서 Fischer-Tropsch 반응, bio-reaction 등에 많이 응용되고 있다. 특히, 반응물은 기체 상태로 반응기에 투입이 되는데, 이 기포입자의 상승하는 힘을 바탕으로 기상/액상/고상이 균일하게 혼합되게 된다. 많은 연구자들이 이러한 기포탑 반응기의 성능을 개선하고자, 다양한 반응기 디자인에 대하여 보고하고 있다. 특히 반응기 내부에 tray를 설치함으로써, 기포 포집율을 증진시기고 액상의 역류를 최소화시키는 연구가 활발히 진행되고 있다. 본 연구에서는, 다양한 기공크기를 갖는 tray를 활용함으로써 높이에 따른 기포 포집율의 변화 및 반응기 내에 기포 입자의 거동 특성에 대하여 살펴보았다.

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.74.2-74.2
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• 2011

A simulation study on synthesis gas process in GTL process was carried out in order to find optimum operation conditions for GTL (gas-to-liquid) pilot plant design. Optimum operating conditions for synthesis gas process were determined by changing reaction variables such as feed temperature and pressure. During the simulation, overall synthesis process was assumed to proceed under steady-state conditions. It was also assumed that physical properties of reaction medium were governed by RKS (Redlich-Kwong-Soave) equation. The effect of temperature and pressure on synthesis gas process $H_2$/CO ratio were mainly examined. Simulation results were also compared to experimental results to confirm the reliability of simulation model. Simulation results were reasonably well matched with experimental results.

• 한국연소학회:학술대회논문집
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• 2012.11a
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• pp.175-176
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• 2012

As a carbon neutral fuel, biomass can be converted into various types of high-valued products such as synthetic natural gas (SNG), Hydrogen, Fischer - Tropsch (FT) diesel. and valuable chemicals. In order to make above mentioned products, gasificaion process is essential as energy utilization platform of solid biomass. In this study, state of the art and prospect for biomass gasification technologies are presented.

• Bulletin of the Korean Chemical Society
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• v.35 no.6
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• pp.1703-1705
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• 2014

Bubble column reactors are considered the reactor of choice for numerous applications including oxidation, hydrogenation, waste water treatment, and Fischer-Tropsch (FT) synthesis. They are widely used in a variety of industrial applications for carrying out gas-liquid and gas-liquid-solid reactions. In this paper, the computational fluid dynamics (CFD) model is used for predicting the gas holdup and its distribution along radial and axial direction are presented. Gas holdup increases linearly with increase in gas velocity. Gas bubbles tends to concentrate more towards the center of the column and follows a wavy path.