• Title/Summary/Keyword: Drop pattern

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Comparative study of CP(center of pressure) Pattern on pitching sort in Softball (소프트볼 투구 구질에 따른 압력중심 이동패턴의 차이점 분석)

  • Moon, Young-Jin;Kim, Jin-Gyong
    • Korean Journal of Applied Biomechanics
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    • v.16 no.3
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    • pp.183-188
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    • 2006
  • This research is to know differentiation of CP(center of pressure) pattern among four pitching sort(straight ball, raise ball, change up ball, drop ball). Subject are three national or junior athletes. We use the one camera, Novel Win pressure measurement system. Conclusions are as follows : 1. When we throw the straight ball, CP of left foot is effective to end movement at middle of foot in body balance on arm angular motion and enhanced speed. 2. When we throw the raise ball, to change CP from middle to post is more effective in order to raise the ball. 3.In drop ball pitching, in order to fall down the ball in front of hitter, CP of left foot move from post foot to interior part of forefoot 4. In change up ball pitching, if CP of left foot move into forefoot, it is a cause of high ball and hitter can recognize the change up ball because of late arm rotation motion.

Flow Characteristics of Vertical Upward Gas-Liquid Two-Phase Flow (수직상향 기액이상류의 유동특성)

  • Choi Bu-Hong
    • Journal of Advanced Marine Engineering and Technology
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    • v.29 no.4
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    • pp.377-383
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    • 2005
  • This paper deals with the flow characteristics of air-water two-phase flow in a vertical tube of 10mm I.D. and 600mm in length at an adiabatic condition. The obtained experimental data were covered with the liquid superficial velocity ranging from 0.095m/s to 2.56m/s. and the gas superficial velocity ranging from 0.032m/s to 21.08m/s. The effects of the gas and liquid superficial velocity on the flow pattern transitions, frictional pressure drop, and film thickness and gas-liquid interface roughness were also examined. It was found that the film thickness increased and the liquid film wave length was more longer with the liquid superficial velocity $j_L$ increasing at $j_G$ constant. It was also showed that the frictional pressure drops were experienced in three regions. namely increasing region(bubbly flow), decreasing region (Taylor bubble and slug flows) and re-increasing region (annular flow).

Characteristics of Flow Regime Transitions in Horizontal Gas-Liquid Two-Phase Flow (수평 기액2상유동에서 유동양식의 천이특성)

  • Lee, S.C.;Lee, J.P.;Kim, J.Y.
    • The Magazine of the Society of Air-Conditioning and Refrigerating Engineers of Korea
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    • v.17 no.4
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    • pp.342-349
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    • 1988
  • The characteristics of flow pattern transitions in a horizontal cocurrent gas-liquid flow have been investigated by means of a statistical analysis of instantaneous pressure drop curves at an orifice. The dimensionless intensity of pressure drop fluctuation shows a sudden change during the course of flow transitions, indicating that it may be a good measure to identify the flow regime transitions. The probability density function of the curves feature a unique pattern depending upon the flow regimes and the statistical properties of the PDF also have particular ranges for each flow regime. In conclusion, the statistical analysis of instantaneous pressure drops may be a powerful tool for predicting the flow regime transitions.

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Numerical investigations on the effect of tortuosity on friction factor in superconducting CICC configuration

  • Vaghela, Hitensinh;Lakhera, Vikas;Bhatt, Kunal;Sarkar, Biswanath
    • Progress in Superconductivity and Cryogenics
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    • v.23 no.4
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    • pp.49-55
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    • 2021
  • The Cable in Conduit Conductor (CICC) configurations are designed, tested and realized to make high field superconducting (SC) magnets. The evolution of CICC design makes it challenging to forecast thermo-hydraulic behavior. A common objective of thermo-hydraulic studies is to obtain the most reliable predictive correlation for friction factor in CICC geometries and to reduce the dependency on the experiment. So far, only the void fraction and Reynolds number have been considered in the predictive correlations in an explicit way. In the present paper, the CICC twisting pattern dependency, called tortuosity (τ), on the pressure drop prediction, has been assessed through a numerical simulation approach. The CICC twisting pattern with 6+1 petals (solid conductor in the present study) with different twisting pitches is mimicked in the numerical simulation for the range 100 ≤ Re ≤10000 and 1 < τ < 1.08 and a correlation for friction factor, f, has been proposed as a function of Re and τ.

Cycling Packet Dropping Mechanism for Assured Forwarding Packets in Internet (인터넷에서 Assured Forwarding 패킷을 위한 사이클링 패킷 폐기 메커니즘)

  • Kim, Su-Yeon;Gang, Hyeon-Guk
    • The KIPS Transactions:PartC
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    • v.9C no.2
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    • pp.221-226
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    • 2002
  • Cycling Packet Dropping mechanism we proposed in this paper adaptively drops packets, as predicting traffic pattern between each cycle. Therfore the proposed mechanism makes up for the drawback of RIO mechanism and minimizes errors being capable of predicting in Dynamic and Strict Packet Dropping mechanism. And we executed a simulation and analyzed the throughput and packet drop rate based on the Sending Drop Precedence changing dynamically depending on the network traffic. The results show that the proposed mechanism provides better performance on drop precedence levels and stricter drop precedence policy for AF class.

The analysis of lower extremities injury on depth jump (Depth Jump 시 하지 관절 상해에 관한 운동역학적 분석)

  • So, Jae-Moo;Kim, Yoon-Ji;Lee, Jong-Hee;Seo, Jin-Hee;Chung, Yeon-Ok;Kim, Koang-Ki
    • Korean Journal of Applied Biomechanics
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    • v.15 no.1
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    • pp.127-142
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    • 2005
  • The purpose of this study was to analysis biomechanics of the lower extremities injury the heights(40cm, 60cm, 80cm) of jump box as performed depth jump motion by 6 females aerobic athletes and 6 non-experience females students. The event of depth jump were set to be drop, landing and jump. The depth jump motions on the force plate were filmed using a digital video cameras, and data were collected through the cinematography and force plate. On the basis of the results analyzed, the conclusions were drawn as follows: 1. The landing time of skill group was shorter than unskill group at 40cm, 60cm drop height during drop-landing-jump phase especially. The landing time of 60cm drop height was significant between two group(p<.05). 2. The peak GRF of sagittal and frontaI direction following drop height improve was variety pattern and the peak vertical force of 40cm drop height was significantly(p<.05). 3. The magnitude of peak passive force was not increase to change the drop height. 4. The peak passive forces was significant at 40cm drop height between two groups(p<.05)

EFFECT OF THE CHANNEL STRUCTURE ON THE COOLING PERFORMANCE OF RADIATOR FOR TRANSFORMER OF NATURAL CONVECTION TYPE (자연대류를 이용한 변압기용 방열기의 채널 구조가 방열성능에 미치는 영향)

  • Kim, D.E.;Kang, S.;Suh, Y.K.
    • Journal of computational fluids engineering
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    • v.19 no.4
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    • pp.86-93
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    • 2014
  • Increased demand of power-transformer's capacity inevitably results in an excessive temperature rise of transformer components, which in turn requires improved radiator design. In this paper, numerical simulation of the cooling performance of an ONAN-type (Oil Natural Air Natural) radiator surrounded by air was performed by using CFX. The natural convection of the air was treated with the full-model. The present parametric study considers variation of important variables that are expected to affect the cooling performance. We changed the pattern and cross-sectional area of flow passages, the fin interval, the flow rate of oil and shape of flow passages. Results show that the area of flow passage, the fin interval, the flow rate of oil and shape of flow passages considerably affect the cooling performance whereas the pattern of flow passages is not so much influential. We also found that for the case of the fin interval smaller than the basic design, the temperature drop decreases while a larger interval gives almost unchanged temperature drop, indicating that the basic design is optimal. Further, as the flow rate of oil increases, the temperature drop slowly decreases as expected. On the other hand, when the shape of flow passages are changed, temperature drop is increased, indicating that the cooling performance is enhanced thereupon.

Experimental measurements of R-22 two-phase friction factor in plate heat exchangers (판형열교환기에서 R-22 냉매의 이상 압력 손실계수 평가)

  • Yoo, Sang-Roon;Jeong, Ji-Rwan
    • Proceedings of the KSME Conference
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    • 2007.05b
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    • pp.2273-2278
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    • 2007
  • Brazed Plate Heat Exchanger (BPHE) is a type of compact plate heat exchanger with parallel corrugated plates which are brazed together in series. Each plate hascorrugation called herringbone pattern. Inside a BPHE, hot fluid and cold fluid alternate its flow direction to establish counter current flow configuration. Two-phase flow heat transfer and pressure drop of R-22 in BPHE were experimentally measured in this study. In the present experiments, single-phase region and two-phase region coexist in a BPHE. Therefore, the inside of a BPHE have to be divided into single phase region and two phase region and analyzed accordingly. The results from the single phase flow analysis are then extended to the two phase flow analysis to correlate the condensation and evaporation heat transfer and pressure drop for the refrigerant R-22 in the BPHEs. Previous models for two- phase friction factor have been compared with the present experimental results.

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A Study on Performance Characteristics of R134a Variation with a Capillary Tube Diameter and Length in a Domestic Small multi Refrigerator [Kim_Chi Refrigerator] (모세관 내경 축소에 따른 소형멀티 냉동시스템의 성능특성변화)

  • Lee, Moo-Yeon;Choi, Seok-Jae;Kim, Sang-Ok
    • Proceedings of the KSME Conference
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    • 2004.11a
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    • pp.1598-1603
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    • 2004
  • This paper is an experimental study on the performance characteristic with a variation of capillary diameter and length. The performance characteristic of a refrigeration system is predicted that it is occurring changes of flow pattern and pressure drop in a capillary tube because of reduction of capillary diameter 0.74 to 0.6 mm. The difference between experimental results and analytical results is mainly caused by values of friction factor for using to calculate pressure drop through a small diameter capillary tube under 0.74mm. The experimental equation is derived from capillary tube test data using curve fitting method.

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