• 한국염색가공학회지
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• 제32권2호
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• pp.80-88
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• 2020

Supercritical fluid dyeing is a new alternative to the conventional aqueous process because of its environmental benefits. In this study, dyeing properties of Nylon 6 fabrics were investigated depending on dyeing temperature and pressure in supercritical CO₂ fluid dyeing system. In order to select the optimal condition for supercritical fluid dyeing of Nylon 6 fabrics, dyeing temperature and pressure were varied from 100, 110, 120℃, 200, 230, 260bar, respectively. The results of K/S values and levelling properties showed that the optimal dyeing condition for Nylon 6 fabrics was 110℃ and 230bar in the supercritical CO₂ fluid dyeing system. The washing fastness ratings of the dyed Nylon 6 fabrics under supercritical medium were good for both fading and staining except for staining on nylon.

• Advances in Energy Research
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• 제8권4호
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• pp.265-273
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• 2022

In this study, a product gas yield and carbon conversion were measured during the coal pyrolysis. The pyrolysis process occurred under two different atmospheres such as subcritical (45 bar, 10℃) and supercritical CO₂ condition (80 bar, 35℃). Under the same pressure (80 bar), the atmosphere temperature increased from 35℃ to 45℃ to further examine temperature effect on the pyrolysis at supercritical CO₂ condition. For all three cases, a power input supplied to heating wire placed below coal bed was controlled to make coal bed temperature constant. The phase change of CO₂ atmosphere and subsequent pyrolysis behaviors of coal bed were observed using high-resolution camcorder. The pressure and temperature in the reactor were controlled by a CO₂ pump and heater. Then, the coal bed was heated by wire heater to proceed the pyrolysis under supercritical CO₂ condition.

• 대한기계학회논문집A
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• 제33권9호
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• pp.913-921
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• 2009

In this study, supercritical nano plating was performed to observe its effect on materials. Using supercritical carbon dioxide as a solvent, we observed how different pressures and temperatures of the supercritical fluid affected the process and its outcome. The plating current increases as pressure increases from 8 MPa to 16 MPa, but it decreases after that. Similarly, the plating current increases as temperature is increased from $35^{\circ}C$ to $45^{\circ}C$, but the current decreases after that. Also, the thickness of the wet electrolyte plating is about $35\sim50{\mu}m$, while the thickness of the plating done using supercritical fluid is about $20\sim25{\mu}m$. At the results, It to it is considered that supercritical nano plating enable to form more thin and stable plating than wet electroplating methods. Also both of the electroplating methods could be affected plating quality by surface condition, and the supercritical nano plating has been confirmed to product more uniform plating surface than wet electroplating.

• Journal of Microbiology and Biotechnology
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• 제19권12호
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• pp.1596-1602
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• 2009

A lipase-catalyzed esterification reaction of (S)-naproxen ethyl ester by CALB (Candida antarctica lipase B) enzyme was performed in supercritical carbon dioxide. Experiments were performed in a high-pressure cell for 10 h at a stirring rate of 150 rpm over a temperature range of 313.15 to 333.15 K and a pressure range of 50 to 175 bar. The productivity of (S)-naproxen ethyl ester was compared with the result in ambient condition. The total reaction time and conversion yields of the catalyzed reaction in supercritical carbon dioxide were compared with those at ambient temperature and pressure. The experimental results show that the conversion and reaction rate were significantly improved at critical condition. The maximum conversion yield was 9.9% (216 h) at ambient condition and 68.9% (3 h) in supercritical state. The effects of varying amounts of enzyme and water were also examined and the optimum condition was found (7 g of enzyme and 2% water content).

• Macromolecular Research
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• 제17권12호
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• pp.950-955
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• 2009

The physical and rheological properties of thermoplasticized irradiation-crosslinked polyethylene foam using supercritical methanol treatment were investigated by GPC, FTIR, DSC, WAXS, DMTA and UDS. The polyethylene foam was selectively decrosslinked into thermoplasticized polyethylene in an appropriate supercritical methanol condition without any undesirable side reactions such as oxidation and disproportionation. The thermoplasticization was promoted with increasing reaction temperature to reach completion above $380^{\circ}C$. The supercritical reaction condition affected the crystallization behavior, and mechanical and rheological properties of the decrosslinked polyethylene foam, but not its crystallographic structure or crystallinity.

• 한국연초학회지
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• 제18권1호
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• pp.92-99
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• 1996

A mathematical model of the pressure gradient of supercritical CO2 in a vertical tobacco bed was developed in this study. In particular, the compaction of the tobacco as a function of temperature and CO2 flow is included in the model. Downflow of CO2 (low condition is described. At velocities in excess of 0.6 cm/sec at 7$0^{\circ}C$, there is a large increase in pressure gradient for beds deeper than about 0.5 m. The proposed model offers a better understanding of operating the process using supercritical CO2.

• 청정기술
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• 제18권2호
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• pp.155-161
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• 2012

본 연구의 목적은 분말 사출성형 공정에서 초임계유체를 이용하여 사출성형체로부터 결합제를 효율적으로 제거하는 것이다. 두께 1~2 mm 정도의 얇은 성형체의 경우는 기존의 초임계 추출공정을 이용하여 초기부터 온도, 압력이 높은 조건에서도 아무런 결함 없이 단시간 내에 결합제를 제거할 수 있지만, 시편이 두꺼워질수록 초기에 균열이 발생하기 때문에 일정 공정조건에서는 한계가 있다. 따라서 초기에는 낮은 공정조건에서 시작하여 단계별로 온도와 압력을 상승시키는 초임계 가변 조건 탈지공정을 연구하였다. 두께 1~4 mm의 세라믹 사출성형체 시편을 사용하여 여러 가지 초임계 조건에서 탈지실험을 수행하여 두꺼운 세라믹 사출성형체에 균열이 생기지 않으면서 가장 추출수율이 높은 가변조건 공정의 초기조건을 설정하였다. 이렇게 설정한 초기조건을 시작으로 직경 10 mm, 두께 4 mm의 두꺼운 세라믹 사출성형체 시편을 온도 333.15~343.15 K, 압력 12~27 MPa, $CO_2$ 유량 0.5~1.0 L/min 범위에서 단계별로 상승시켜 최종적으로는 5시간동안 95% 이상의 파라핀 왁스 결합제를 제거할 수 있었다.

• 한국분말재료학회지
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• 제10권1호
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• pp.6-14
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• 2003

The purpose of the present study is to investigate the method decreasing debinding time as well as lowering operation condition than pure supercritical $CO_2$ debinding by using cosolvent or binary mixture of propane + $CO_2$. First method is to add cosolvent, such as n-hexane, DCM, methanol, 1-butanol, in supercritical $CO_2$. In case of adding cosolvent, we were found the addition of non-polar cosolvent (n-hexane) improves dramatically the binder removal rate (more than 2 times) compared with pure supercritical $CO_2$ debinding, second method is to use mixture of supercritical propane + $CO_2$, as solvent. In case of using mixture of supercritical propane + $CO_2$, the rate of debinding speeded up with increasing of pressure and concentration of propane at 348.15 K. It was found that addition of cosolvent (e.g., n-hexane, DCM) and binary mixture propane + $CO_2$ for supercritical solvent remarkably improved binder removal rate for the paraffin wax-based binder system, in comparison with using pure supercritical $CO_2$.

• Korean Chemical Engineering Research
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• 제47권3호
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• pp.281-286
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• 2009

아임계 및 초임계 조건의 물을 이용하여 캐나다산 Athabasca 오일샌드로부터 역청 추출 및 황 제거 실험을 수행하였다. 0~120 min의 반응시간, 360, $380^{\circ}C$의 온도, 15~30 MPa의 압력 및 $0.074{\sim}0.61g/cm^3$의 물 밀도를 변화시키면서 micro reactor에서 역청 수율을 조사하였다. 역청 수율은 온도에 상관없이 압력이 증가할수록 증가하였으며, 특히 초임계 영역에서 수증기 개질반응에 의해 생성된 수소에 의해 역청의 수율이 급격히 증가하였다. 전체 기상 생성량은 압력 증가에 따라 감소하였으나 $380^{\circ}C$에서 황과 수소의 생성분율은 25 및 30 MPa로 압력 증가에 따라 소량 증가하였다. 이상의 결과는 초임계 조건이 수소의 생성과 황의 제거에 유리하다는 것을 보여준다. 초임계 조건$380^{\circ}C$, 25와 30 MPa)에서 역청 수율은 최대 약 22%였으며, 오일샌드에 함유된 황 제거율도 최대값 40%에 도달하였다.

• Composites Research
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• 제34권5호
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• pp.277-282
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• 2021

초임계유체 조건은 별도의 환원제와 높은 열처리 공정조건 없이 산화그래핀으로부터 그래핀을 제조할 수 있다. 본 연구에서는 메탄올과 에탄올 용매의 초임계유체 조건에서 산화그래핀을 그래핀으로 변환시키는 공정을 연구하였다. 제조된 그래핀의 구조를 FE-SEM과 XRD를 사용하여 분석하였을 때, 초임계 조건에서 산화그래핀의 환원반응은 다른 변수(농도, 반응시간)보다는 용매의 변화에 더 크게 영향을 받았다. 에탄올 용매의 사용이 메탄올을 사용했을 때보다 환원반응에 더욱 좋은 결과를 보여주었다. 본 연구에서 준비된 그래핀을 20 wt%까지 에폭시수지와 혼합하여 복합수지 조성물을 제조하여, 이 조성물의 열전도특성을 분석하였다. 복합수지조성물의 열전도도는 그래핀의 함량에 비례하여 상승하였고, 에탄올 초임계 용액조건에서 제조된 그래핀이 복합수지조성물의 열전도도에 더 효과적이었다.