• Title/Summary/Keyword: Tube Length

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Prediction of Service Life of a Respirator Cartridge by the Occupational Environment -Simulation of Breakthrough Curve for Respirator Cartridge and Sampling Tube- (작업현장의 환경조건에 따른 방독마스크 정화통의 수명예측 -모사에 의한 정화통과 샘플관의 파과시간-)

  • 김덕기;신창섭
    • Journal of the Korean Society of Safety
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    • v.11 no.2
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    • pp.89-95
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    • 1996
  • To predict the service life of an organic vapor respirator cartridge, the breakthrough curve of respirator was simulated using a fixed-bed adsorption model and compared with that of sampling tube. And the effects of bed porosity, length to diameter ratio and flow rate of the sampling tube were studied. The life time of respirator cartridge was increased with the decrease of particle size and bed porosity. And the breakthrough time of sampling tube was affected by the flow rate, however not by the length to diameter ratio. The 10% breakthrough time of the sampling tube was corresponded with that of cartridge.

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Flow and Heat Transfer Characteristics of a Multi-Tube Inserted Impinging Jet (노즐출구에 삽입된 다중관에 의한 충돌제트의 유동 및 열전달 특성)

  • Hwang, Sang-Dong;Cho, Hyung-Hee
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.28 no.2
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    • pp.135-145
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    • 2004
  • An experimental study is conducted to investigate the flow and heat transfer characteristics of a multi-tube inserted impinging jet. Four different multi-tube devices are tested for various nozzle-to-plate distance. Flow visualization by smoke-wire method and velocity measurements using a hot-wire anemometer are applied to analyze the flow characteristics of the multi-tube insert impinging jet. The local heat transfer coefficients of the multi-tube inserted impinging jet on the impingement surface are measured and the results are compared to those of the conventional jet. In multi-tube inserted system the multi-tube length plays an important role in the flow and heat transfer characteristics of the jet flow. With multi-tube insert of I3d4 and I6d4 which has relatively longer tube length than the multi-tube-exit of I3d1 and I6d1, the flow maintains its increased velocity far downstream due to interaction between adjacent flows. For the small H/D of 4, the local heat transfer coefficients of multi-tube inserted impinging jet are much higher than those of the conventional jet because the flow has higher velocity and turbulent intensity by the use of the multi-tube device. At large gap distance of H/D=12, also higher heat transfer rates are obtained by installing multi-tube insert except multi-tube insert of I3d1.

Breakup Characteristics in Plain Jet Air Blast Atomizer(I)-Jet Breakup and Internal Flow- (2유체 분무노즐의 분열특성(I)-액주분열 및 내부유동-)

  • Kim, Hyeok-Ju;Lee, Chung-Won
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.21 no.8
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    • pp.1009-1023
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    • 1997
  • The breakup length of a liquid jet with flowrate, formed by releasing through a nozzle of circular cross-section into the atmosphere, was experimented and studied for 3 liquid nozzles of varying diameters. The experimental result was analyzed using the existing theoretical equation for predicting the breakup length. It was found that the breakup length of liquid jet depends on the velocity, and the breakup length increases with increasing of the liquid nozzle diameter. Also, the variation range of the breakup length for the same flowrate of liquid increased rapidly as velocity was increased for laminar flow, but in the turbulent flow region, it leveled off in the range of approximately 0.55-0.7 of the mean breakup length. Furthermore, when the longest smooth liquid jet was applied to the co-axial flow air blast atomizer, the effect of air flow on the flow pattern and breakup length was studied for 6 glass nozzles of different lengths and diameters. It was found that depending on the diameter of the mixing tube and liquid jet, it was possible to observe a wide range of flow patterns, such as liquid jet through flow, partial annular flow and annular flow. The liquid jet breakup length was more sensitive to the change in the length rather than the diameter of the mixing tube. As the length of the mixing tube shortens, the breakup length also shortens rapidly.

Ice-formation phenomena for laminar water flow in a stenotic tube (협착관내 층류유동에서 물의 결빙현상)

  • 서정세;김무근;노승탁;임장순
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.10 no.1
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    • pp.11-21
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    • 1998
  • A numerical study is made on the ice-formation for water flow inside a stenotic tube. The study takes into account the interaction existing between the laminar flow and the stenotic port in the circular tube. In the solution strategy, the present study is substantially distinguished from the existing works In that the complete set of governing equations in both the solid and liquid regions are resolved. In a channel flow between parallel plates, the agreement of predictions and available experimental data is very good. Numerical results are mainly obtained by varying the height and length of a stenotic shape and additionally for several temperatures of the wall and inlet of tube. The results show that the shape of stenotic port has the great effect on the thickness of the solidification layer in the tube. As the height of a stenosis grows and the length of a stenosis decreases, the ice layer thickness near the stenotic port is thinner due to backward flow caused by the sudden expansion of water tunnel. It is also found that the ice layer becomes more fat In accordance with Reynolds number and the temperature of the wall and inlet of tube decreased.

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Selection of Capillary Tubes for HCFC-22 Alternative Fluids (HCFC-22 대체냉매의 모세관 선정)

  • Jung, D.S.;Kim, C.B.
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.7 no.3
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    • pp.435-449
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    • 1995
  • In this paper, pressure drop through a capillary tube is modeled to determine the length of a capillary tube for a given set of conditions. HCFC-22 and its alternatives, HFC-134a, R407B, and R410A are used as working fluids. The conditions on which the model is tested are as follows : condensing temperature; 40.0, 45.0, 50.0, $55.0^{\circ}C$, degree of subcooling;0.0, 2.5, $5.0^{\circ}C$, capillary tube exit condition;choked flow, capillary tube diameter;1.2~2.4mm, mass flow rate;5.0~50.0g/sec. The results justify the use of Stoecker's model which yields the results very close to the values in ASHRAE handbook. While McAdams' method yields much better results than Duckler's in calculating the viscosity of the fluid in 2-phase, the friction factor suggested by Stoecker seems to be the best for capillary tubes of large diameter used in residential air conditioners. For each refrigerant, 372 data with various variables are calculated by the model. The results show that capillary tube length varies very uniformly with changes in condensing temperature and degree of subcooling. Based on this fact, regression analysis is performed to determine the dependence of mass flow rate on the length and diameter of a capillary tube, condensing temperature, and degree of subcooling. Thus determined correlation yields a mean deviation of 2.36% for 1,488 data, showing an excellent agreement.

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Some Aspects of Experimental in-Tube Evaporation

  • Ha, Sam-Chul
    • Journal of Mechanical Science and Technology
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    • v.14 no.5
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    • pp.537-546
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    • 2000
  • The heat transfer characteristics of refrigerant-oil mixture for horizontal in-tube evaporator have been investigated experimentally. A smooth copper tube and a micro-fin tube with nominal 9.5 mm outer diameter and 1500 mm length were tested. For the pure refrigerant flow, the dependence of the axial heat transfer coefficient on quality was weak in the smooth tube, but in the micro-fin tube, the coefficients were 3 to 10 times greater as quality increases. Oil addition to pure refrigerant in the smooth tube altered the flow pattern dramatically at low mass fluxes, with a resultant enhancement of the wetting area by vigorous foaming. The heat transfer coefficients of the mixture for low and medium qualities were increased at low mass fluxes. In the micro-fin tube, however, the addition of oil deteriorates the local heat transfer performance for most of the quality range, except for low quality. The micro-fin tube consequently loses its advantage of high heat transfer performance for an oil fraction of 5%. Results are presented as plots of local heat transfer coefficient versus quality.

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A Study on the Go-go-kwan(姑姑冠) -With a Special Reference to "Jip-sa(集史)"- (고고관(姑姑冠)에 관한 연구 - "집사(集史)"를 중심으로 -)

  • Kim, Mi-Ja
    • Journal of the Korean Society of Costume
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    • v.58 no.3
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    • pp.105-115
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    • 2008
  • A Go-go-kwan is a particular hat which has worn by married woman in Mongol and Yuan dynasty in China. It is also widely called as a Boktak in Mongol. The Go-go-kwan, recorded in jip-sa and in the miniature painting of 14th century is the early type of go-go-kwan. Later type can be seen from the relic collections of Gyeonggi Provincial Museum in Korea. The Go-go-kwan is composed with three parts ; feather part, tube part and hat part. Among the feathers, the largest one is as long as four times of the length of the tube and the shortest one is half the length of the tube. The tube is made of light weight wood such as white birch or bamboo, and covered with silk. Some of the hats were made exactly to fit on the head whereas others were designed to wear on the head as like jobawi.

Optimization of Nd:YAG laser welding parameters for sealing the small Ti tube ends (소형 티타늄 튜브 끝의 밀봉용접을 위한 Nd:YAG 레이저 용접조건의 최적화)

  • Lee Hyeong Geun;Han Hyeon Su;Son Gwang Jae;Hong Sun Bok
    • Proceedings of the KWS Conference
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    • v.43
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    • pp.73-75
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    • 2004
  • The purpose of this study is to optimize Nd:YAG laser welding parameters to seaz a Rf source into a Ti micro capsule. Ti tube ends can be sealed as some length of ぉbe end is melted and coalesced. The exact control of the melted length is the most important to get sound sealing. The Nozzle type, tube rotating speed, tilt angle, focal position, pumping voltage, pulse frequency and pulse width were selected as the Nd:YAG laser welding Parameters. These Parameters were optimized by the Taguchi experimental method using 115 orthogonal array. Appearance and cross section of the seated tube ends were examined by SEM.

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Investigation on the selection of capillary tube for the alternative refrigerant R-407C (대체냉매 R-407C의 모세관 선정에 관한 연구)

  • 김용환;김창년;박영무
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.10 no.1
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    • pp.56-65
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    • 1998
  • In this paper, experimental investigation of capillary tube performance for R-407C is performed. The experimental setup is made of real vapor-compression refrigerating system. In this study, mass flow rate is measured for capillary tubes of various diameter and length as inlet pressure and degree of subcooling are changed. These data are compared with the results of a numerical model. The mass flow rates of the numerical model are less than by 14% compared with the measured mass flow rates. It is found that mass flow rate and length for R-407c are less than those of R-22 under the same condition. Also based on this experimental study and the numerical model, a set of capillary tube selection charts for R-407C is constructed.

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An Experimental Study that depend on the Resonance Tube Length for a Thermoacoustic Refrigerator of 1/2 wave (1/2파장 열음향 냉동기의 공명관 길이 의존 특성 연구)

  • Song, Kyu-Joe;Park, Jong-Ho;Koh, Deuk-Yong;Kim, Hyo-Bong
    • Proceedings of the KSME Conference
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    • 2001.11b
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    • pp.217-222
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    • 2001
  • The thermoacoustic refrigerator has not only considerable possibility but also commercial usability, because it has high reliability, lower vibration, no moving part, and can easily be constructed. In this study, the resonance characteristics of the thermoacoustic refrigerator were investigated for better performance, varying the length of Resonant Tube to 400mm $\sim850mm$. In order to determine the optimum position of stack in the resonance tube and the frequency, the simple $\lambda/2$ thermoacoustic refrigerator was constructed. It was used air as a coolant. in the fifth harmonic, it was taken the highest ${\Delta}t$ that was $52.6^{\circ}C$ at 827Hz in 400mm tube with 40mm stack.

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