• Title/Summary/Keyword: 초임계 조건

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초임계 난류연소 모델링

  • Park, Tae-Seon
    • Journal of the KSME
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    • v.56 no.9
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    • pp.32-37
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    • 2016
  • 초임계 유체의 고유한 물리적 특성변화와 난류유동을 결합하여 성능을 높이는 데 활용하고 있는 가장 대표적인 시스템 중의 하나는 연소기이다. 이때 연료와 산화제의 연소반응은 저압조건과 다른 고유한 특성을 가지고 있어 기존의 연소모델에 의해서는 정확한 분석이 어렵게 된다. 따라서 초임계 압력조건에 대한 연소과정을 분석할 수 있는 연소모델이 필요하고 이러한 연소과정이 난류유동조건에서 발생하기 때문에 최근 많은 연구가 초임계 난류연소모델 개발에 집중되어 왔다. 이 글에서는 특히 액체로켓엔진 관련 초임계 연소모델 개발 분야의 연구동향을 살펴보고자 한다.

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Micronization of Triclosan Using Supercritical Fluids (초임계 유체를 이용한 트리클로산의 미세입자 제조)

  • Shin, Moon-Sam
    • Proceedings of the KAIS Fall Conference
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    • 2012.05a
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    • pp.360-362
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    • 2012
  • 본 논문에서는 의약품, 화장품, 생활용품에서 널리 사용되는 약물인 트리클로산에 대해 초임계 유체를 이용하여 미세화공정이 연구되었다. 낮은 임계온도와 임계압력의 조건을 고려하여 초임계 이산화탄소를 선정하였고, 초임계 이산화탄소와의 용해도를 고려하여 초임계 용액 급속팽창공정이 선정되었다. 본 연구에서 입자크기에 영향을 미치는 온도와 압력효과가 검토되었고 상평형자료에 의해 해석되었다.

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Micronization of Salicylic Acid Using Supercritical Fluids (초임계 유체를 이용한 살리실산의 미세입자 제조)

  • Shin, Moon-Sam
    • Proceedings of the KAIS Fall Conference
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    • 2011.05a
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    • pp.482-484
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    • 2011
  • 본 논문에서는 화장품과 생활용품에서 널리 사용되는 약물인 살리실산에 대해 초임계 유체를 이용하여 미세화공정이 연구되었다. 낮은 임계온도와 임계압력의 조건을 고려하여 초임계 이산화탄소를 선정하였고, 초임계 이산화탄소와의 용해도를 고려하여 초임계 용액 급속팽창공정이 선정되었다. 본 연구에서 입자크기에 영향을 미치는 온도와 압력효과가 검토되었고 상평형자료에 의해 해석되었다.

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Micronization of Cosmeceutical Biocide Using Supercritical Fluids (초임계 유체를 이용한 약용화장품 항균제의 미세입자 제조)

  • Shin, Moon-Sam
    • Proceedings of the KAIS Fall Conference
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    • 2011.12a
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    • pp.361-363
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    • 2011
  • 본 논문에서는 의약품, 화장품, 생활용품에서 널리 사용되는 약물인 히토키치올에 대해 초임계 유체를 이용하여 미세화공정이 연구되었다. 낮은 임계온도와 임계압력의 조건을 고려하여 초임계 이산화탄소를 선정하였고, 초임계 이산화탄소와의 용해도를 고려하여 초임계 용액 급속팽창공정이 선정되었다. 본 연구에서 입자크기에 영향을 미치는 온도와 압력효과가 검토되었고 상평형자료에 의해 해석되었다.

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Numerical analysis of turbulent combustion in Supercritical combustor with multi-injector (다중 분사기가 장착된 초임계 연소기 난류연소해석)

  • Jeon, Tae Jun;Park, Tae Seon
    • Proceedings of the Korean Society of Propulsion Engineers Conference
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    • 2017.05a
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    • pp.803-810
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    • 2017
  • the liquid oxygen transitions to a supercritical state, causing rapid changes in properties and pseudo boiling in supercritical combustion. the combustion reaction operating in a supercritical state depends on the turbulence diffusion caused by difference of density, therefore, a study of the diffusion flow and pseudo boiling is required. Many researchers have studied these phenomena in the supercritical combustion, but A case study by various variables is inadequate. In this study, the flow field and flame structure were investigated numerically by changing the recirculation flow and liquid oxygen core length through oxygen-fuel ratio(O/F), combustor diameter and recess ratio at supercritical pressure condition.

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Cryogenic Jet Injection Test Using Liquid Nitrogen (액체 질소를 이용한 극저온 단일 제트 분사 시험)

  • Cho, Seong-Ho;Khil, Tae-Ock;Park, Gu-Jeong;Yoon, Young-Bin
    • Proceedings of the Korean Society of Propulsion Engineers Conference
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    • 2010.11a
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    • pp.597-600
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    • 2010
  • Cold flow injection test was conducted to investigate the characteristics of cryogenic liquid nitrogen jet at sub to supercritical condition. Single jet injector element was installed in high pressure chamber to investigate the effect of ambient pressure around the jet, injector geometry and flow conditions. Experimental results showed obvious differences between jet characteristics under subcritical and supercritical condition. Effect of injector inlet shape also was investigated.

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A Study on the Variable Condition Debinding Process in Supercritical CO2 for Removing Binder from Thick Ceramic Injection Molded Parts (두꺼운 세라믹 사출성형체로부터 효율적인 결합제 제거를 위한 초임계 CO2 가변조건 탈지공정 연구)

  • Kim, Hyung-Kun;Yim, Joon-Hyuk;Kim, Hyung-Soo;Lim, Jong-Sung
    • Clean Technology
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    • v.18 no.2
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    • pp.155-161
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    • 2012
  • The purpose of this study is to remove paraffin wax binder effectively from powder injection molded part using supercritical fluids in powder injection molding process. For a thin powder injection molded part about 1-2 mm thickness, paraffin wax binder can be removed rapidly without any defect by traditional supercritical extraction process which has fixed high temperature and pressure condition. But, for a thick powder injection molded part, there are limitations in removing paraffin wax binder by the fixed high process condition because crack occurs at the beginning step. Therefore, here we studied variable condition debinding process that starts with mild process condition at the beginning step and then increase the process conditions simultaneously at each step. To find out the initial process condition that has the highest extraction yield without any defect for each sample thickness, we investigated various supercritical debinding conditions using 1-4 mm thickness ceramic injection molded sample. By using the variable condition debinding process that starts with the initial process condition at the first step and then increasing process conditions simultaneously at each step (temperature from 333.15 to 343.15 K, pressure from 12 to 27 MPa, and $CO_2$ flow rate from 1.5 to 10 L/min), over 95% of paraffin wax binder was removed from the 4 mm thick (10 mm diameter) ceramic injection molded disk samples within 5 hours.

Analysis of Supercritical Shear Coaxial Jet Using Density Gradient Magnitude (밀도구배강도를 이용한 초임계 전단동축 제트 분석)

  • Lee, Keonwoong;Kim, Dohun;Son, Min;Han, Choyoung;Koo, Jaye
    • Journal of the Korean Society of Propulsion Engineers
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    • v.17 no.6
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    • pp.59-66
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    • 2013
  • Spray characteristics of single round jet with liquid nitrogen and coaxial spray with liquid nitrogen and gaseous argon were observed. Shadowgraph method was used for spray visualization, and density gradient magnitude image was used to analyse the result. In subcritical condition, irregularity of the jet surface was harder in the coaxial spray. In supercritical condition, diffusion of nitrogen injected from shear coaxial injector was faster than single jet. Jet diameter was induced by averaging images, in supercritical condition, difference of diameter of coaxial jet was rapidly decreased than that of single jet.

막냉각 및 재생냉각 난류유동

  • Park, Tae-Seon
    • Journal of the KSME
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    • v.56 no.9
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    • pp.49-53
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    • 2016
  • 액체로켓엔진은 연소실의 온도가 약 3,600K로서 냉각시스템은 필수적이다. 지금까지 대표적으로 사용되어온 냉각방법은 재생냉각과 막냉각으로 아임계압력에서 다양한 실험연구에 의해서 설계가 진행되어 왔다. 아임계압력에서 얻어진 유동구조 이해 및 설계경험식은 초임계 압력에서는 물성치가 급격히 변하기 때문에 재정립될 필요가 있다. 특히 열전달 성능을 좌우하는 난류유동구조가 크게 바뀌기 때문에 초임계 유체에 대한 난류유동 및 열전달연구가 진행될 필요가 있다. 이 글에서는 초임계 압력조건에서 난류열전달 연구동향을 소개하고자 한다.

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Phase Behavior of Simvastatin Drug in Mixtures of Dichloromethane and Supercritical Carbon Dioxide and Microparticle Formation of Simvastatin Drug Usins Supercritical Anti-Solvent Process (디클로로메탄과 초임계 이산화탄소의 혼합용매에서 Simvastatin 약물의 상거동과 초임계 역용매 공정을 이용한 Simvastatin 약물 미세입자의 제조)

  • Oh, Dong-Joon;Lee, Byung-Chul
    • Clean Technology
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    • v.13 no.1 s.36
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    • pp.34-45
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    • 2007
  • Phase behavior of the ternary systems of water-insoluble simvastatin drug, which is well known to be effective drugs for hypercholesterolemia therapy, in solvent mixtures of dichloromethane and supercritical carbon dioxide was investigated to present a guideline of establishing operating conditions in the particle formation of the drugs by a supercritical anti-solvent recrystallization process utilizing dichloromethane as a solvent and carbon dioxide as an anti-solvent. The solubilities of simvastatin in the mixtures of dichloromethane and carbon dioxide were determined as functions of temperature, pressure and solvent composition by measuring the cloud points of the ternary mixtures at various conditions using a high-pressure phase equilibrium apparatus equipped with a variable-volume view cell. The solubility of the drug increased as the dichloromethane composition in solution and the system pressure increases at a fixed temperature. A lower solubility of the drug was obtained at a higher temperature. The second half of this work is focused on the particle formation of the simvastatin drug by a supercritical anti-solvent recrystallization process in a cylindrical high-pressure vessel equipped with an impeller. Microparticles of the simvastatin drug were prepared as functions of pressure (8 MPa to 12 MPa), temperature (303.15 K, 313,15 K), feed flow rate of carbon dioxide, and stirring speed (up to 3000 rpm), in order to observe the effect of those process parameters on the size and shape of the drug microparticles recrystallized.

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