• 제목/요약/키워드: Internal-Mixing

검색결과 301건 처리시간 0.021초

공기보조 인젝터의 분무특성 연구 (Spray Characteristics of the Air-Shrouded Injectors)

  • 김기성
    • 한국마린엔지니어링학회:학술대회논문집
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    • 한국마린엔지니어링학회 2000년도 추계학술대회 논문집(Proceeding of the KOSME 2000 Autumn Annual Meeting)
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    • pp.82-90
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    • 2000
  • Improving the atomization characteristics by adopting the Air-Shrouded injector has been considered as one of the important methods for decreasing HC emissions in SI engines. Thus, in this study for the purpose of developing Air-Shrouded injector which has a finer spray, atomization characteristics of different types of commercial Air-Shrouded injectors were investigated through the spray imaging and the drop size measurements. As a result, it was found that the internal mixing type of Air-shrouded injector had a good atomization characteristics. But, a number of large droplets were found in the internal mixing type commercial injector, this phenomenon was improved by adopting the thread type nozzle passages.

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DCM 설계에서 주요 인자의 결정과 내.외적 안정해석 (The Analysis of Internal & External Stabilities and Factors for D.C.M Design)

  • 이충호;정승용;한상재
    • 한국지반공학회:학술대회논문집
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    • 한국지반공학회 2009년도 세계 도시지반공학 심포지엄
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    • pp.793-808
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    • 2009
  • This paper presents procedure and prediction method of internal and external stabilities when designing D.C.M, with main factors to be considered, such as chemical reaction of additive, physical properties of stabilized body and mixing strength. Results show that through case studies, a design unconfined compressive strength of stabilized body (hereafter referred to as 'compressive strength') directly depends on the quantity of cement, which is decided by laboratory test, and the compressive strength enormously affects internal and external stabilities. So laboratory mixing test to obtain the compressive strength for design allowable stress should be given careful considerations.

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탄소 섬유강화 복합소재의 고압 수지이송 성형공정에서 직선형 믹싱헤드의 성능 및 유용성 평가 (Performance and Feasibility Evaluation of Straight-Type Mixing Head in High-Pressure Resin Transfer Molding Process of Carbon Fiber Reinforced Composite Material)

  • 한범정;정용채;황기하;강명창
    • 한국기계가공학회지
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    • 제16권5호
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    • pp.157-165
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    • 2017
  • The high-pressure resin transfer molding (HP-RTM) technology has been commercialized for fast production of fiber reinforced composite materials. The high-pressure mixing head was one of the most core component of the HP-RTM process. In this study, a mixing head was systematically designed, manufactured and evaluated. This mixing head was composed of a nozzle, a mixing chamber, a cleaning piston part, and an internal mold release part. In actual, a straight-type structure was newly designed instead of the conventional L-type structure for improving the maximum mixing pressure and mixing ratio precision. The performance of mixing head was showed maximum mixing pressure of 15.22MPa and mixing ratio precision of 0.12%. CFRP molding experiments were successfully obtained a 6~11 laminating carbon sheet using HP-RTM presses and specimen molds.

내부혼합 동축 와류형 분사기를 장착한 액체로켓엔진용 축소형 연소기의 연소시험 (Combustion Tests of Sub-scale Combustor for a Liquid Rocket Engine with Internal Mixing Swirl Injector)

  • 한영민;이광진;임병직;최환석
    • 한국추진공학회지
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    • 제11권5호
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    • pp.72-77
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    • 2007
  • 액체로켓엔진용으로 내부혼합 동축 와류형 분사기를 장착한 축소형 연소기에 대한 설계 및 연소시험결과를 기술하였다. 추진제는 액체산소 및 케로신이며 연소기는 분사기 헤드, 삭마냉각방식의 연소실 그리고 물냉각 노즐부로 구성되어 있다. 분사기 헤드는 액체산소 매니폴드, 연료 매니폴드, 중앙 분사기 그리고 내부혼합 형태의 18개 분사기로 이루어졌다. 축소형 연소기 연소시험은 성공적으로 이루어졌으며, 분사기의 손상이 발생하지 않았고 연소특성속도는 설계점에서 1756 m/sec을 나타내었다. 고주파 연소불안정은 나타나지 않았지만 탈설계점에서 압력의 저주파 섭동이 기준치를 넘는 결과를 보여주었다.

Numerical analysis of internal flow and mixing performance in polymer extruder I: single screw element

  • Kim, Nak-Soo;Kim, Hong-Bum;Lee, Jae-Wook
    • Korea-Australia Rheology Journal
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    • 제18권3호
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    • pp.143-151
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    • 2006
  • We analyzed the non-Newtonian and non-isothermal flow in a single screw extruder system and investigated the mixing performance with respect to the screw speed and the screw pitch. The viscosity of polymer melt was described with Carreau-Yasuda model. The mixing performance was computed numerically by tracking the motions of particles in the screw element system. The extent of mixing was characterized in terms of the deformation rate, the residence time distribution, and the strain. The results revealed that the high screw speed reduces the residence time but increases the deformation rate while the small screw pitch increases the residence time. It is concluded that the high screw speed increases the dispersive mixing performance and the small screw pitch increases the distributive mixing performance.

Production of Ultra-fine Metal Powder with Gas Atomization Processes

  • Wang, M. R.
    • 한국분무공학회지
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    • 제11권2호
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    • pp.59-68
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    • 2006
  • Experimental results of the metal powder production with internal mixing, internal impinging and the atomizer coupled with substrate design are presented in this paper. In a test with internal mixing atomizer, mean powder size was decreased from $37{\mu}m\;to\;23{\mu}m$ for Pb65Sn35 alloy as the gas-to-melt mass ratio was increased from 0.04 to 0.17. The particle size further reduces to $16.01{\mu}m$ as the orifice area is increased to $24mm^2$. The micrograph of the metal powder indicates that very fine and spherical metal powder has been produced by this process. In a test program using the internal impinging atomizers, the mean particle size of the metal powder was decreased from $22{\mu}m\;to\;12{\mu}m$ as the gas-to-melt-mass ratio increased from 0.05 to 0.22. The test results of an atomizer coupled with a substrate indicates that the deposition rate of the molten spray on the substrate is controlled by the diameter of the substrate, the height of the substrate ring and the distance of the substrate from the outlet of the atomizer. This in rum determines the powder production rate of the spraying processes. Experimental results indicate that the deposition rate of the spray forming material decreases as the distance between the substrate and the atomizer increases. For example, the deposition rate decreases from 48% to 19% as the substrate is placed at a distance from 20cm to 40cm. On the other hand, the metal powder production rate and its particle size increases as the subsrate is placed far away from the atomizer. The production of metal powder with mean particle size as low as $3.13{\mu}m$ has been achieved, a level which is not achievable by the conventional gas atomization processes.

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CRITICAL HEAT FLUX ENHANCEMENT

  • Chang, Soon-Heung;Jeong, Yong-Hoon;Shin, Byung-Soo
    • Nuclear Engineering and Technology
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    • 제38권8호
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    • pp.753-762
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    • 2006
  • In this paper, works related to enhancement of the CHF are reviewed in terms of fundamental mechanisms and practical applications. Studies on CHF enhancement in forced convection are divided into two categories, CHF enhancement of internal flow in tubes and enhancement of CHF in the nuclear fuel bundle. Methods of enhancing the CHF of internal flows in tubes include enhancement of the swirl flow using twisted tapes, a helical coil, and a grooved surface; promotion of flow mixing using a hypervapotron; altering the characteristics of the heated surface using porous coatings and nano-fluids; and changing the surface tension of the fluid using additives such as surfactants. In the fuel bundle, mixing vanes or wire wrapped rods can be employed to enhance the CHF by changing the flow distributions. These methods can be applied to practical heat exchange systems such as nuclear reactors, fossil boilers, fusion reactors, etc.

내부혼합형 2유체 분사노즐의 형상에 따른 분무특성 (Spray Characteristics on Shape of Twin Fluid atomizer by Internal Mixing Chamber Type)

  • 윤수환;정대인;하종률
    • Journal of Advanced Marine Engineering and Technology
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    • 제18권4호
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    • pp.43-52
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    • 1994
  • I investigated experomentally the spray characteristics to the operating conditions and the shapes of internal mixing twin fluid atomizer. The wide variations of air per liquid ratio are conducted to predit the influences of the Sauter mean diameter(SMD), spray angle, distribution of drop size, the flowing condition of gas and length, flowing, area of gas and liquid, and diameter, number and place of the orifice. In this experiment, air per liquid raio, mixing chamber length per diameter, orifice diameter, and the flowing area ratio of gas and fluid influences greatly on SMD, spray angle, distribution of drop size and intermittent fluctuation region.

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Effect of Rice Straw Steaming Time and Mixing Ratio between Acacia mangium Willd Wood and Steamed Rice Straw on the Properties of the Mixed Particleboard

  • Tran, Van Chu;Le, Xuan Phuong
    • Journal of Forest and Environmental Science
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    • 제31권2호
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    • pp.119-125
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    • 2015
  • This study examined the effects of rice straw steaming time and mixing ratio between rice straw and wood particle on the properties of mixed particle board from Acacia mangium Willd wood and rice straw. Rice straw and Acacia mangium Willd wood were collected in Hanoi, Vietnam. The particle board was three-layer particle board with the structural ratio of 1:3:1. The thickness, density and board size of the particle board were 18 mm, $0.7g/cm^3$, and $800{\times}800{\times}18$ (mm, including trimming), respectively. A resin mixture between commercial Urea-formaldehyde (U-F) adhesive and methylene diphenyl isocyanate (MDI) adhesive was used with a dosage of 12% for the core layer and 14% for the surface layer. In this experimental design, the steaming time for rice straw was 15, 30, 45, 60, and 75 minutes at $100^{\circ}C$. The rice straw-wood mixing ratio was 10, 20, 30, 40, and 50%. The results showed that both mixing ratio and steaming time affect the properties of the particleboard, but the mixing ratio has a stronger impact. A higher mixing ratio and a longer steaming time resulted in a better quality of particleboard. The optimal steaming time for rice straw was 46.12 minutes with the straw-wood mixing ratio of 29.85% with the following characteristics of the particle board: the modulus of rupture (MOR) of 14.64 MPa, internal bond strength (IB) of 0.382 MPa, thickness swelling (TS) of 8.83%, and board density of $0.7-0.7g/cm^3$.