• 제목/요약/키워드: 압력 강하 계수

검색결과 178건 처리시간 0.023초

Effects of Chamfered Perforated Plate on Pressure Loss Characteristics (챔퍼가 적용된 타공판의 압력 강하 특성에 대한 연구)

  • You, Kyeongsik;Lee, Hyungyu;Cho, Jinsoo
    • Journal of the Korean Society for Aeronautical & Space Sciences
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    • 제47권11호
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    • pp.779-786
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    • 2019
  • Effects of chamfered perforated plate on pressure loss characteristics were studied with CFD analysis. Both inlet chamfer angle and outlet chamfer angle were considered. Perforated patterns were compared by pressure loss coefficient in certain porosity and Reynolds number. Reynolds number effects were studied for several chamfer angles and plate thickness. As the inlet chamfer angle was increased, the pressure loss coefficient was decreased until the certain angle and reversed to increase. In the outlet chamfered shape cases, the pressure loss coefficient was increased with chamfer angle. Effects of pattern shapes and Reynolds number on pressure loss characteristics were negligible with different chamfer angles and thickness studied in this paper.

Effect of the lubrication oil on heat transfer and pressure drop characteristics of supercritical carbon dioxide in a microfin tube (마이크로핀관내 냉동기유가 초임계 이산화탄소의 열전달과 압력강하에 미치는 영향)

  • Ku, Hak-Keun
    • Journal of the Korea Academia-Industrial cooperation Society
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    • 제13권4호
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    • pp.1440-1446
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    • 2012
  • This paper presents an experimental study of heat transfer and pressure drop characteristics of supercritical carbon dioxide with PAG inside a horizontal microfin tube. Heat transfer coefficient and pressure drop gradients were measured at 10 MPa in pressure and 520 kg/$m^2s$ in mass flux with variation of PAG mass concentration from 0.06% to 2.26%. The tendencies of both heat transfer and frictional pressure drop characteristics show the same as those of pure $CO_2$ up to 0.3% in PAG mass concentration. In case of 2.26% in PAG mass concentration, measured heat transfer coefficients showed 50% lower than those of pure $CO_2$ near the pseudocritical temperature and measured frictional pressure drop gradients show 1.6 times higher in comparison with those of pure $CO_2$ at $60^{\circ}C$ in $CO_2$ bulk temperature.

A Study on Characteristics of SiC Ceramic Candle Filters Applicable to Hot Gas Filtration (고온 집진용 탄화규소 세라믹 캔들 필터의 특성 연구)

  • 홍민선;문수호;김순태;이동태
    • Journal of Energy Engineering
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    • 제10권2호
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    • pp.120-131
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    • 2001
  • 최근 세라믹 필터에 대한 연구는 열악한 환경 및 산성가스에 대한 저항성으로 인해 고온 가스 여과에서 가장 전망 있는 기술로 부각되는 시점에 있다. 본 연구의 목적은 탄화규소(SiC) 세라믹 캔들 필터를 사용하여 IGCC와 PFBC의 새로운 전력생산 공정에서 배출되는 먼지를 제거하기 위한 필터성능을 조사하기 위함이다. 필터의 성능 평가는 고온.고압.고온.상압 조건에서 이루어졌으며 필터의 압력강하, 먼지 제거효율, 저항 계수, 그리고 열적.기계적 저항성 등을 파악하였다. 길이 30cm, 60cm 필터에 2종류의 먼지(코크스와 물유리 공정)를 이용하여 나타난 먼지 제거효율은 99.9% 이상을 보였으며 필터의 평균 기공 크기가 감소함에 따라 압력강하가 증가함을 확인하였다. 또한 탄화규소 세라믹 필터의 성능은 내부압력이 증가할수록 압력강하가 감소하고 유량이 증가할수록 압력강하가 증가함과 특히 유체에 대한 압력강하 변화는 온도의 영향보다는 상대적으로 내부압력에 더 많은 영향을 받음을 확인하였다.

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Characteristics of Cryogenic Cascade Refrigeration Cycle for Liquefaction of Natural Gas with the Pressure Drop of Heat Exchanger (LNG 열교환기의 압력강하에 따른 천연가스 액화용 초저온 캐스케이드 냉동사이클 특성)

  • Yoon, Jung-In;Choi, Kwang-Hwan;Son, Chang-Hyo;Kwag, Jin-Woo;Baek, Seung-Moon
    • Journal of Advanced Marine Engineering and Technology
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    • 제36권6호
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    • pp.756-761
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    • 2012
  • Natural gas is converted in to LNG by chilling and liquefying the gas to the temperature of $-162^{\circ}C$, when liquefied, the volume of natural gas is reduced to 1/600 of its standard volume. This gives LNG the advantage in transportation. In this study, the effects of the pressure drop of refrigerant and natural gas in the LNG heat exchanger of cryogenic cascade refrigeration cycle were investigated and then the design criteria for the pressure drop of refrigerant and natural gas of the LNG heat exchanger were proposed. The pressure drop of the cascade liquefaction cycle was investigated and simulated using HYSYS software. The simulation results showed that the pressure drop in the LNG heat exchanger is set to 50 kPa considering the increase in the compressor work and COP of cryogenic cascade liquefaction cycle.

Asymptotic Approach to Pressure Drop and Heat Transfer in a Rectangular Pipe with Shear-thickening Fluids (사각형 단면 파이프 내에서의 Shear-thickening 유체를 이용한 압력강하 및 열전달 예측에 대한 점근적 해석)

  • Lee, Dong-Ryul
    • Journal of the Korean Society of Mechanical Technology
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    • 제13권4호
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    • pp.23-30
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    • 2011
  • 본 연구는 산업용 열교환기 및 상용 파이프의 최적 설계를 위하여 열교환기 내의 사각형 단면 파이프의 shear-thickening 비뉴톤 유체의 압력강하 및 대류 열전달률을 수치해석적으로 수행하였다. shear-thickening 유체의 구성 방정식은 기존의 비뉴톤 유체 멱법칙을 보완한 확장 멱법칙 모델을 채택하였다. 파이프 내의 압력강하를 의미하는 마찰계수와 확장 레이놀즈 수의 곱은 기존 연구의 비교자료와 비교할 때 뉴톤 유체 영역과 멱법칙 영역에서 각각 0.018% 및 0.06% 내에서 일치함을 보였고, 대류 열전달률을 의미하는 뉴셀트 수는 문헌치와 비교할 때 뉴톤 유체 영역과 멱법칙 영역에서 각각 0.025% 및 0.14% 내에서 일치함을 보였다. 비뉴톤 확장 멱법칙 유체 모델의 형태를 띠는 shear-thickening 유체를 열교환기 또는 상용파이프 내의 사각형 단면 파이프 내에서 사용하면 유동지수(n)에 따라서 뉴톤 유체보다 최대 160%의 압력강하를 증가시켰고 최대 14%의 대류 열전달 감소를 발생시킬 수 있었다.

Study on Design Factor and Design-code Development for Plate Type Heat Exchangers (판형 열교환기의 주요 설계인자와 설계프로그램 개발에 관한 고찰)

  • Ko, Jea-Hyun;Park, Kweon-Ha;Song, Young-Ho
    • Journal of Advanced Marine Engineering and Technology
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    • 제36권8호
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    • pp.1003-1009
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    • 2012
  • Heat exchanger has been widely used in the industry which needs energy transport, and the application of the plate type heat exchanger having high efficiency has been greatly increased. In this study main design parameters are analyzed and new equations are induced. The induced formulation was compared with a commercial program in order to design an optimal heat exchanger. The equations of heat transfer coefficient and pressure drop for Chevron angles are introduced as functions of Reynolds number. The program implemented the equations is tested with Chevron angle variation. The results show that the convective heat transfer coefficients take errors within 8% and the pressure drops have errors within 5% in the analysis conditions.

Pressure Drop Reduction and Heat Transfer Increase with Rheological Fluid Flows in a Circular Conduit (원형 도관 내에서의 유변 유체에 대한 압력손실 감소 및 열전달 증가)

  • Lee, D.R.
    • Journal of Power System Engineering
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    • 제16권1호
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    • pp.51-57
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    • 2012
  • 본 연구는 컴팩트한 열교환기의 설계를 위하여 열교환기 내의 원형 단면 도관의 유변 유체의 압력 강하 및 대류 열전달률을 수치해석적으로 수행하였다. 유변 유체의 구성방정식은 기존의 비뉴톤 유체 멱법칙을 보완한 수정 멱법칙 모델을 채택하였다. 도관 내의 압력강하를 의미하는 마찰계수와 수정 레이놀즈 수의 곱은 기존 문헌치와 비교할 때 뉴톤 유체 영역과 유변 멱법칙 영역에서 각각 0.01% 및 0.004% 내에서 일치함을 보였고 유변 수정멱법칙 유체 모델의 형태를 띠는 유변 유체를 열교환기 내의 원형 단면 도관 내에서 사용하면 뉴톤 유체보다 최대 58%의 압력강하를 감소시켰고 최대 9%의 대류 열전달 증가을 발생시킬 수 있었다.

Analysis on condensation heat transfer and pressure drop to develop design program for plate heat exchangers (판형열교환기 설계프로그램 개발을 위한 응축열전달 및 압력강하 분석)

  • Ko, Jea-Hyun;Song, Young-Ho;Park, Kweon-Ha
    • Journal of Advanced Marine Engineering and Technology
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    • 제38권4호
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    • pp.376-382
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    • 2014
  • The purpose of this study is to get the formulas of condensation heat transfer coefficient and pressure drop about the water to develop design program for plate type heat exchangers. The single phase flow of cold side was calculated with the correlation of Ko. Condensation heat transfer coefficient model proposed by Annaiev was used and Lockhart model was used to analyze the pressure drop. The calculation algorithm was proposed to calculate heat transfer rate and pressure drop simultaneously. The prediction errors remained within 20% compared to the commercial code in the working range of the plate heat exchangers.

Study on the Effect of Total Pressure Loss by Bell Mouth Inlet Screen (벨 마우스 흡입구 보호망에 의한 전압력 손실영향 연구)

  • Lee, Changwook;Choi, Seong Man
    • Journal of the Korean Society of Propulsion Engineers
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    • 제25권6호
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    • pp.29-35
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    • 2021
  • Bell mouth inlet is applied in various industries due to the advantage of little pressure loss and accurate flow measurement. In this study, the configuration of the bell mouth intake is designed in a long radius shape, and a suitable grid size was selected to minimize the pressure drop and to prevent the engine damage by foreign objects at outdoor operating conditions. It was able to present a modified pressure drop coefficient equation from two data obtained from the computational simulation and experimental results for the total pressure loss by inlet screen installation.

An Experimental Study on Pressure Drop and Heat Transfer Coefficient of Laminar Ag Nanofluid Flow in Mini-Tubes (은 나노유체의 미세관내 층류 유동의 압력강하 및 열전달계수에 관한 실험적 연구)

  • Kwon, Jeong-Tae;Nahm, Taek-Hun;Kim, Tae-Wan;Kwon, Young-Chul
    • Journal of the Korea Academia-Industrial cooperation Society
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    • 제10권12호
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    • pp.3525-3532
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    • 2009
  • This study presents the heat transfer and pressure drop characteristics of Ag nanofluid in mini-tubes(outer diameters of 1/8inch, 3/16inch). Experiments were performed for Reynolds numbers ranged from 500 to 2,500 and nanofluid concentrations of 0.1 and 0.3vol.%. The pressure drop of nanofluid flow increased by max. 21% compared with that of distilled water. The heat transfer coefficients of the nanofluid of 0.1 vol.% enhanced 3~42% for 1/8inch tube, and 3~69% for 3/16inch tube. Also, the heat transfer coefficients of the nanofluid of 0.3 vol.% enhanced 35~65% for 1/8inch tube, and 62~125% for 3/16inch tube. From the results Ag nanofluid can be a better candidate as a coolant than distilled water when using in mechanical and/or electronic systems.