• Proceedings of the Korean Vacuum Society Conference
• /
• 2009.02a
• /
• pp.112.1-112.1
• /
• 2009

• Proceedings of the Korea Society for Energy Engineering kosee Conference
• /
• 2001.05a
• /
• pp.159-162
• /
• 2001

• Journal of the Korean Applied Science and Technology
• /
• v.21 no.4
• /
• pp.359-363
• /
• 2004

Reaction conditions and catalysts were investigated for direct $CF_3I$ synthesis. Optimum reaction temperature was determined by pyrolysis of $CF_3H$ and catalytic reactions. Reactions with changing oxygen concentration were performed. As a result, yield of $CF_3I$ increased with decreasing oxygen concentration. Catalytic activity was changed with the weight ratio of the used metal salts. This result was stemmed from the change in the pore size of activated carbon by the metal salts. The optimum reaction conditions were: $600^{\circ}C$, space velocity of $45hr^{-1}$, and with 7wt% KF/AC catalyst.

• Prospectives of Industrial Chemistry
• /
• v.24 no.2
• /
• pp.10-21
• /
• 2021

최근 폐플라스틱의 사용량 증가와 미세플라스틱으로 인한 해양 오염 및 생태계 축적 등의 부정적인 영향으로 인해 플라스틱 업사이클링(upcycling) 및 리파이너리(refinery) 기술에 대한 관심이 증가하고 있다. 화학적 재활용 방법 중의 하나로, 폐플라스틱의 열분해를 통해서 재생 연료 및 화학물질을 생산하는 연구는 90년도에 활발히 진행된 바 있고, 최근의 환경오염에 대한 대응으로서 다시 많은 관심을 받고 있다. 폐플라스틱을 효율적으로 분해하기 위해서는 촉매를 사용하여 분해 속도를 제어해 주어야 하며, 사용된 촉매의 특성에 따라 최종 생성물의 성상이 크게 달라진다. 본 기고문에서는 폐플라스틱의 촉매 열분해를 통해 가솔린, 디젤유 및 항공유와 같은 수송용 연료, 발전용 연료 혹은 방향족 화학 물질을 생산하는 기술들의 최신 연구 동향을 다루고 향후 전망에 대해 기술하고자 한다. 아울러 최근 몇 년간 많은 연구가 있었던 바이오매스와 폐플라스틱의 혼합열분해를 통한 하이브리드 촉매 공동 열분해 기술에 대해서도 다루고자 한다.

• Korean Chemical Engineering Research
• /
• v.54 no.1
• /
• pp.94-100
• /
• 2016

Hydrogen production via steam reforming of bio-oil from algal biomass over fast pyrolysis with commercial catalysts was carried out. Aqueous bio-oil obtained by phase separation from a crude oil over fast pyrolysis was used as a reactant and comparison studies for activity over different catalysts (FCR-4-02, POS-7, Cat. A, RUA), reaction temperature, and steam/carbon (S/C) ratios were performed. Experimental results showed that different catalytic activities were observed with different S/C ratios and catalyst composition and the highest hydrogen yield of 70% was obtained with a POS-7 catalyst at a S/C ratio of 10 and 1073 K.

• 한국연소학회:학술대회논문집
• /
• 2014.11a
• /
• pp.33-36
• /
• 2014

Gasification of biomass produces syngas containing CO, $H_2$ and/or $CH_4$, which can then be converted into energy or value-added fuels. One of key issues for efficient gasification is to minimize tar concentration in the syngas for use in a final conversion device such as gas engine. This study investigated the decomposition of primary tar by catalytic cracking using char as catalyst, of which the feature can be integrated into a fixed bed gasifier design. The pyrolysis vapor containing tar from pyrolysis of wood at $500^{\circ}C$ was passed through a reactor filled with or without char at $800^{\circ}C$ for a residence time of 1, 3 or 5 sec. Then, the condensable vapor (water and tar) and gases were analyzed for the yields and elemental composition. Four types of char particles with different microscopic surface area and pore size distribution: wood, paddy straw, palm kernel shell and activated carbon. The results were analyzed for the mass and carbon yields of tar and the composition of product gases to conclude the effects of char types and residence time.

• Journal of Sensor Science and Technology
• /
• v.29 no.2
• /
• pp.112-117
• /
• 2020

Xylene is a hazardous volatile organic compound that should be precisely measured to monitor indoor air quality. However, the selective and sensitive detection of ppm-level xylene using oxide-semiconductor gas sensors remains a challenge. In this study, pure and Cr-doped Co₃O₄ nanoparticles (NPs) were prepared using flame spray pyrolysis, and their gas-sensing characteristics to 5-ppm xylene at 250 ℃ were investigated. The 4 at% Cr-doped Co₃O₄ NPs exhibited a high gas response to 5-ppm xylene (resistance ratio to gas and air = 39.1) and negligible cross-responses to other representative and ubiquitous indoor pollutants such as ethanol, benzene, formaldehyde, carbon monoxide, and ammonia. In this paper, the enhancement of the gas response and selectivity of Co₃O₄ NPs to xylene by Cr doping was discussed in relation to the catalytic promotion of the gas-sensing reaction. This sensor can be used to monitor indoor xylene.

• Clean Technology
• /
• v.19 no.3
• /
• pp.233-242
• /
• 2013

The influences of Ca and Fe based oxides as dechlorination sorbents on the product distribution, boiling point distribution of liquid product, concentration of Cl of the products from the pyrolysis of PVC containing combustible wastes were investigated. With Fe based oxides as the sorbents, the yield of liquid product remarkably decreased whereas the decrease of the boiling point distribution of the liquid product was not noticeable. This phenomenon indicated that Fe based oxides worked as catalysts with weak catalytic activity. With Ca based oxides as the sorbents, the yield of liquid product did not decrease and the boiling point distribution of liquid product did not change significantly, but the dechlorination performance of these was much better than that with Fe based oxides.

• Journal of Industrial and Engineering Chemistry
• /
• v.68
• /
• pp.69-78
• /
• 2018

A study has been carried out of the regenerability of a commercial Ni catalyst used in the steam reforming of the volatiles from biomass pyrolysis (gases and bio-oil), determining the evolution of the reaction indices (conversion, product yields and $H_2$ production) in successive reaction-regeneration cycles. The causes of catalyst deactivation (coke deposition and Ni sintering) have been ascertained characterizing the deactivated and regenerated catalysts by TPO, TEM, TPR and XRD. Catalyst activity is not fully recovered by coke combustion in the first cycles due to the irreversible deactivation by Ni sintering, but the catalyst reaches a pseudo-stable state beyond the fourth cycle, reproducing its behaviour in subsequent cycles.

• Bulletin of the Korean Chemical Society
• /
• v.18 no.12
• /
• pp.1264-1268
• /
• 1997

The poly(methylsilene) (1) was modified with the group 4 metallocene Cp2MCl2/Red-Al (M = Ti, Zr, Hf) combination catalyst and with the group 6 metal carbonyl M(CO)6 (M = Cr, Mo, W) catalyst, producing the highly cross-linked isoluble polymer and the lowly cross-linked soluble polymer, respectively. An interrelationship between molecular weight and percent ceramic residue yield with metal within the respective group was not found. The polymers modified with the group 4 metallocene combination catalysts have higher molecular weight and lower percent ceramic residue yield than the polymers modified with the group 6 metal carbonyl catalysts do. The catalytic activity of group 4 metallocene combinations appears to be higher at ∼100 ℃, but to be lower at very high temperature than those of group 6 metal carbonyls. The pyrolysis of the modified 1 yielded SiC ceramic.