• 제목/요약/키워드: slurry pressure

검색결과 247건 처리시간 0.023초

전방 차수층이 쉴드터널 초과 이수압에 미치는 영향 (Effect of a Frontal Impermeable Layer on the Excess Slurry Pressure during the Shield Tunnelling)

  • 이용준;이상덕
    • 한국철도학회:학술대회논문집
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    • 한국철도학회 2011년도 정기총회 및 추계학술대회 논문집
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    • pp.1199-1213
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    • 2011
  • 이수가압식 쉴드공법은 사질토에서 적용성이 우수하지만, 이수압이 낮으면 이수 유출 및 지반변형이 발생하기도 한다. 따라서 이수가압식 쉴드에서는 초기 막장압보다 큰 초과 이수압을 가하여 막장 안정을 유지한다. 그러나 이수압이 너무 높으면 전방 지반의 수동 파괴를 유발하므로 수동 파괴 위험성을 줄이고 이수압을 증가시키는 방법으로 막장 전방에 수평 차수층을 설치하는 방안이 있으나 위치와 규모, 효과가 잘 알려져 있지 않다. 따라서 본 연구에서는 포화 사질토에서 막장전방에 차수 그라우팅 적용시 발생하는 효과를 규명하기 위하여 모형실험을 수행하였다. 실험 결과, 차수층이 있는 경우가 없는 경우보다 이수압을 크게 가할 수 있어서 전방 차수층이 막장 안정성을 증대시킬 수 있다는 것을 확인하였다. 막장 안정성 증대에 가장 큰 영향을 주는 적정 차수층은 길이 1.0~1.5D, 설치높이 1.0D로 나타났다. 초기 막장압 대비 최대 이수압의 비로 막장의 자립 안전율(F)을 제안할 수 있으며, 전방 차수층을 적정 위치에 설치할 경우 초기 막장압보다 3.5~4.0배 크게 이수압을 가할 수 있는 것으로 나타났다.

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포화 사질토에서 전방 차수층이 쉴드터널 초과 이수압에 미치는영향 (Effect of a frontal impermeable layer on the excess slurry pressure during the shield tunnelling in the saturated sand)

  • 이용준;이상덕
    • 한국터널지하공간학회 논문집
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    • 제13권4호
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    • pp.347-370
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    • 2011
  • 이수가압식 쉴드공법은 이수압을 적정 수준으로 관리하면 특히 사질토에서 적용성이 우수하지만, 이수압이 낮으면 이수 유출 및 지반변형이 발생하기도 한다. 따라서 이수가압식 쉴드공법에서는 초기 막장압보다 큰 초과 이수압을 가하여 막장의 안정을 유지한다. 그러나 이수압이 너무 높으면 전방 지반의 수동 파괴를 유발하므로 전방 지반의 수동 파괴 위험성을 배제하고 이수압을 증가시키는 방법으로 막장 전방에 수평 차수층을 설치하는 방안이 있으나 그 위치와 규모 및 효과가 잘 알려져 있지 않다. 따라서 본 연구에서는 포화된 사질토에서 막장 전방에 차수 그라우팅을 적용할 경우에 발생하는 효과를 규명하기 위하여 모형실험을 수행하였다. 실험에서는 차수층의 위치와 길이를 변화시거면서 이수의 유출이나 지반 파괴 이전까지 이수압을 가하여 최대 이수압과 지반 변위 및 이수의 유출로 인한 파괴 형상을 측정하여 분석하였다. 실험 결과, 전방 차수층이 없는 경우에 최대 이수압과 초과 이수압은 토피고에 선형비례 하였으며, 차수층이 존재하는 경우에는 차수층이 없는 경우보다 이수압을 크게 가할 수 있어서 전방 차수층이 막장 안정성을 증대시킬 수 있다는 것을 확인할 수 있었다. 막장 안정성 증대에 가장 큰 영향을 주는 적정 차수층의 규격은 길이 1.0 ~ 1.5D, 설치높이 1.0D로 나타났다. 초기 막장압 대비 최대 이수압의 비로 막장의 자립 안전율(F)을 제안할 수 있으며, 전방 차수층을 적정 위치에 설치할 경우 초기 막장압보다 3.5~4.0배 크게 이수압을 가할 수 있는 것으로 나타났다.

소구경 배관내 아이스슬러리의 유동형상 및 압력강하 특성에 관한 실험적 연구(2) (Experimental Study on Flow Patterns and Pressure Drop Characteristics of Ice Slurry in Small Size Pipe (2))

  • 이동원;윤찬일;주문창
    • 설비공학논문집
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    • 제14권5호
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    • pp.391-397
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    • 2002
  • Pressure drop were experimentally investigated for ice slurry flowing in the acrylic pipes with inner diameter of 24 mm. Ice slurry was made from 6.5% ethylene glycol-water solution, and the pipes is consisted of horizontal, vertical (upward and downward) and $90^{\circ}$ elbow pipe. The ice Packing factor (IPF) and the flow rate of the experiments were varied from 0 to 30% and from 5 to 70kg/min respectively The measured pressure drop in various pipe positions were compared with those for the solution flow (IPF=0). The pressure drop was larder than that for solution flows as the IPF increased when the flow rate was low or very high. Sharp increases in pressure drop were observed for the cases when IPF is more than 70% in horizontal and vertical pipes, whereas the pressure drop increased with the IPF simultaneously in an elbow pipe.

자기장이 페라이트 슬러리의 주입시간에 미치는 영향 (Influences of Magnetic Field on Injection Time of Ferrite Slurry)

  • 임종인;육영진;이영진
    • 한국세라믹학회지
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    • 제43권12호
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    • pp.829-832
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    • 2006
  • In this study, the influence of the magnetic field on ferrite slurry's injection time during the slurry forming process was investigated. The evaluation system of the slurry's injection time under the strong magnetic field was designed with FEM and manufactured. Studied parameters were the applied magnetic field, the input pressure of the slurry, and the supplying tube materials. As the results, the injection time was increased with the external magnetic field strength and rapidly decreased with increasing the input pressure of the slurry. Also the injection time was decreased when the supplying tube was manufactured with the magnetic material having the higher magnetic permeability than the ferrite.

Analysis of $Si_3N_4$ Ultra Fine Powder Using High-pressure Acid Digestion and Slurry Injection in Inductively Coupled Plasma Atomic Emission Spectrometry

  • 김K.H.;김H.Y.;임H.B.
    • Bulletin of the Korean Chemical Society
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    • 제22권2호
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    • pp.159-163
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    • 2001
  • Si3N4 powder has been analyzed by inductively coupled plasma atomic emission spectrometry (ICP-AES). The sample was dissolved by high-pressure acid digestion with HF, H2SO4 (1+1), and HNO3 mix ture. This technique is well suited for the impurity analysis of Si3N4 because the matrix interference is eliminated. A round-robin samples trace elements, such as Ca, W, Co, Al, Fe, Mg, and Na, were determined. For the direct analysis, slurry nebulization of 0.96 mm Si3N4 powder also has been studied by ICP-AES. Emission intensities of Fe were measured as ICP operational conditions were changed. Significant signal difference between slurry particles and aqueous solution was observed in the present experiment. Analytical results of slurry injection and high-pressure acid digestion were compared. For the use of aqueous standard solution for calibration, k-factor was determined to be 1.71 for further application.

배연탈황설비 흡수탑 내 연소가스 및 슬러리의 거동에 관한 수치해석적 연구 (Numerical Analysis on the Flue Gas Flow and Slurry Behavior in the Absorber of a Flue Gas Desulphurization (FGD) System)

  • 최청렬
    • 한국대기환경학회지
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    • 제23권4호
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    • pp.478-486
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    • 2007
  • Numerical analysis had been performed to understand flow characteristics of the flue gas and slurry in the absorber of a flue gas desulphurization (FGD) system using computational fluid dynamics (CFD) technique. Two-fluid(Euler-Lagrangian) model had been employed to simulate physical phenomenon, which slurry particles injected through slurry spray nozzles fall down and bump into the flue gas inflowing through inlet duct. It was not necessary to adopt pre-defined pressure drop inside the absorber because interaction between flue gas and slurry particles was considered. Hundreds of slurry spray nozzles were considered with the spray velocity at the nozzles, swirl velocity and spreading angle. The results note that the flow disturbance of flue gas is found at the bottom of the absorber, and the current rising with high speed stream is observed in the opposite region of the inflow duct. The high speed stream is reduced as the flue gas goes up, because the high speed stream of flue gas dumps falling slurry particles due to momentum exchange between flue gas and slurry particles. In spite of some disproportion in slurry distribution inside the absorber, escape of slurry particles from the absorber facility is not observed. The pressure drop inside the absorber is mainly occurred at the bottom section.

슬러리 가압함침에 의한 3D Mullite 섬유 Preform의 알루미나 입자 충전 (Packing of Alumina Particles in 3D Preform of Mullite Fiber by Slurry Pressure-Infiltration)

  • 심수만
    • 한국세라믹학회지
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    • 제50권6호
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    • pp.528-532
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    • 2013
  • Well-dispersed slurries of submicron-sized alumina powders were pressure-infiltrated in 3D preforms of mullite fibers and the effects of the particle size and infiltration pressure on the particle packing characteristics were investigated. Infiltration without pressure showed that the packing density increased as the particle size decreased due to the reduction of the friction between the particles and the fibers. The infiltrated preforms contained large pores in the large voids between the fiber tows and small pores in the narrow voids between the individual fibers. Pressure infiltration resulted in a packing density of 77% regardless of the particle size or the infiltration pressure(210 ~ 620 kPa). Pressure infiltration shortened the infiltration time and eliminated the large pores in preforms infiltrated with the slurries of smaller particles. The slurry pressure-infiltration process is thus an efficient method for the packing of matrix materials in various preforms.

아이스슬러리의 분기관내 압력손실과 IPF 변화에 관한 실험적 연구 (Experimental Study on Transformation of IPF and Pressure Drop in Branches with Ice Slurry)

  • 박기원;최현웅;노건상;정재천
    • Journal of Advanced Marine Engineering and Technology
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    • 제27권2호
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    • pp.272-279
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    • 2003
  • This study aimed to understand the effects of transporting ice slurry Particles through Pipes with branches. The experimental apparatus was constructed as ice slurry mixing tank. vortex pump, manometers for differential pressure measuring. IPF(ice packing factor) measuring instruments and branches as test sections. The experiments were carried out under various conditions. with concentration of water solution ranging between 0∼20wt% and velocity of water solution at the entry ranging between 1.5∼2.5m/s. The differential Pressure and IPF between the pipe entry and exit were measured. and flowing form was checked throughout the experiment. The pressure loss in 3d branches appeared compared with 6d branches so that it was very high. In the pressure loss of the inside and outside of branches. 6d branches was showed the difference. but was agreed in 3d branches The pressure loss according to concentration of water solution, low value appeared at 10wt% in 6d branches, at 20wt% in 3d branches. The pressure loss according to velocity, did not show large difference. The change of IPF at outlet, appeared +15∼-25% in 6d branches and 0∼-20% in 3d branches. The difference of IPF at the inside and outside of branches. appeared 10∼15% in 6d branches and maximum 5% in 3d branches.

연약지반에서의 쉴드 TBM 굴착시 막장면 안정성 평가를 위한 실험적 연구 (An Experimental Study on Shield TBM Tunnel Face Stability in Soft Ground)

  • 김용만;이상덕;추석연;고성일
    • 한국철도학회논문집
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    • 제16권1호
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    • pp.47-51
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    • 2013
  • 본 논문은 연약지반 쉴드 TBM 축소 모형실험을 통하여 슬러리에 의해 가해지는 막장 지보압의 변화에 따른 터널 막장면 안정성 변화 양상을 파악하고자 토피고에 따라 0.5D, 0.75D, 1.0D, 1.25D, 1.5D의 총 5개 Case에 대하여 모형실험을 수행하였으며, 이론적인 터널 막장면 지보압 및 모형실험으로 선정된 적정 지보압 값을 상호 비교하였다. 암반 쉴드 TBM과 달리 연약지반 쉴드 TBM의 경우 균질한 지반조건임에 따라 모형실험으로부터 산정된 적정 지보압이 터널 심도에 따른 막장면 토압 및 수압으로부터 이론적으로 산정된 막장압 범위($P_{min}{\leq}P_{slurry\;pressure}{\leq}P_{max}$)와 잘 일치하고 있음을 확인하였다.

수직관내 고-액 슬러리 유동 계측 실험연구 (Experimental Study of Solid-water Slurry Flow in Vertical Pipe)

  • 최종수;홍섭;양찬규
    • 한국해양공학회:학술대회논문집
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    • 한국해양공학회 2001년도 추계학술대회 논문집
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    • pp.160-163
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    • 2001
  • In order to develop a nodule conveying system through a flexible pipe out of the deep-seabed manganese nodule miner, an experimental study of the solid-water slurry flow in vertical pipe is performed as the first stage of total experiments. Hydraulic characteristics of the pipe slurry flow such as slip velocity, transport concentration and pressure gradient are investigated for the size of particle, load ratio, and flow rate of water. The higher the load ratio is, the larger the transport concentration and pressure gradient become. The bigger the size of particles is, the larger the pressure gradient becomes. The effectiveness of the flow rate to hydraulic performance is also investigated. This results are to be used for designing crusher and pump, and operating the conveying device.

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