• Title/Summary/Keyword: Sub-bench

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Temperature Dependence of Cr Impurity in La0.6Sr0.4Ti0.3Fe0.7O3-δ Coated Ba0.5Sr0.5Co0.8Fe0.2O3-δ Ion Conducting Membrane for oxygen Separation (산소 분리를 위한 La0.6Sr0.4Ti0.3Fe0.7O3-δ가 코팅된 Ba0.5Sr0.5Co0.8Fe0.2O3-δ 이온전도성 분리막에서 Cr 불순물의 온도 의존성)

  • Park, Yu Gang;Park, Jung Hoon
    • Korean Chemical Engineering Research
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    • v.57 no.1
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    • pp.11-16
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    • 2019
  • $La_{0.6}Sr_{0.4}Ti_{0.3}Fe_{0.7}O_{3-{\delta}}$(LSTF) coated $Ba_{0.5}Sr_{0.5}Co_{0.8}Fe_{0.2}O_{3-{\delta}}$(BSCF) membranes which has properties of high oxygen permeability and stability to $CO_2$ were applied to a bench scale apparatus to conduct oxygen permeation experiments. Also, the membranes of the laboratory and the bench scale device were divided into three regions according to the temperature gradient in the membrane reactor for comparative analysis. While oxygen permeation experiment were conducted up to $900^{\circ}C$, temperature dependence of Cr deposition was investigated. As a result, it was confirmed that the oxygen permeability was $2.37ml/min{\cdot}cm^2$, which was significantly lower than $3.79ml/min{\cdot}cm^2$ measured in the laboratory apparatus. It was found through XRD and SEM/EDS analysis that the decrease in oxygen permeability was originated from the deposition of gaseous Cr on the membrane surface released from the alloy material of the housing. In particular, a large amount of Cr was found in the medium temperature region.

Study on the Effect of Bolt and Sub-bench on the Stabilization of Tunnel Face through FEM Analysis (FEM해석에 의한 막장볼트 및 보조벤치의 막장안정성 효과에 관한 연구)

  • Kim, Sung-Ryul;Yoon, Ji-Sun
    • Tunnel and Underground Space
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    • v.18 no.6
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    • pp.427-435
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    • 2008
  • In this paper, review was made for the excavation method and optimum bench length for unstable tunnel face in case of rock classification type V in order to make the best use of in-situ bearing capacity. 3D FEM analyses were performed to investigate the influences on the tunnel face and adjacent area with regard to the pattern and number of bolts when face bolts were used as a supplementary measure. As a result of this study, full section excavation method with sub-bench is effective in reducing the displacement greatly due to early section closure. Displacement-resistant effects in accordance with the bolting patterns are grid type, zig-zag type and then circular type in order of their effect. And horizontal extrusion displacement of tunnel face reduces as the number of bolts increase. A grid type face bolt covering $1.5m^2$ of tunnel face could secure the face stability in case of full section excavation method with sub-bench.

Experimental Investigation on the Reduction Characteristics of Nitric Dioxide(NO2) over Platinum-based Oxidation Catalyst (백금산화촉매를 통한 이산화질소(NO2)의 저감 특성에 관한 실험적 연구)

  • Kim, Young-Deuk;Cho, Ja-Yun;Lee, Jung-Gil;Kim, Woo-Seung
    • Transactions of the Korean Society of Automotive Engineers
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    • v.20 no.4
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    • pp.142-149
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    • 2012
  • The reduction characteristics of $NO_2$ to NO are experimentally studied over a platinum-based catalyst, especially at lower temperatures below about $200^{\circ}C$. In the present work, two types of steady-state experiments, engine bench and synthetic gas bench tests, are carried out in sequence. Steady-state engine bench tests with the DOC mounted on a light duty 4-cylinder 2.0 liter turbocharged diesel engine are performed and prove that CO plays a major role in $NO_2$ abatement at temperatures below the light-off temperature of CO oxidation, about $200^{\circ}C$. Synthetic gas bench tests are then performed using synthetic gas mixtures with CO, $C_3H_6$, NO, $NO_2$, $O_2$, $H_2O$ and $N_2$ in the $140{\sim}450^{\circ}C$ T-range and show that both CO and $C_3H_6$ are capable of reducing $NO_2$. It is noted that the reaction rate of $NO_2$ with $C_3H_6$ is much higher than that with CO. At temperatures below about $200^{\circ}C$, the reduction of $NO_2$ to NO is promoted with increasing CO concentration and $NO_2$/$NO_X$ ratio and with decreasing $O_2$ concentration, as well as with the presence of $H_2O$.

Modeling and CAE Simulation of Chassis Driveline Test Bench for Vehicle NVH Improvement (차량 NVH개선 설계를 위한 샤시 구동계의 Driveline Test Bench 구성 및 CAE 해석)

  • Kim, Kee-Joo;Ju, Hyung-Jun;Lee, Yong-Heon;Bae, Dae-Sung;Sung, Chang-Won;Baik, Young-Nam;Sohn, Il-Seon
    • Transactions of the Korean Society of Automotive Engineers
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    • v.17 no.1
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    • pp.114-119
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    • 2009
  • The authors have investigated the NVH problems of drive system in full vehicle test. However it is difficult to define the NVH problems of driveline system. Since it is hard to measure the rotating part and it is vague that only the drive system induces the NVH problem. Vibration in a driveline is presented in this paper. In the experiment, the rear sub-frame and propeller shafts and axle were composed and mounted with rubber each other. For applying the vibration input instead of the torsional vibration effect of an engine, the shaker was taken. In particular, torsional vibration due to fluctuating forced vibration excitation across the joint between driveline and rear sub-frame was carefully examined. Accordingly, the joint response was checked from experiments and the FE-simulation using FRF (frequency response function) analysis was performed. All test results were signal processed and validated against numerical simulations. In present study, the new test bench for measuring the vibration signal and simulating the vehicle chassis system was proposed. The modal value and the mode shape of components were analyzed using the CAE model to identify the important components affecting driveline noise and vibration. It could be reached that the simplified test bench could be well established and be used for design guide and development of the vehicle chassis components.

Characteristics of Agricultural Paddy Soil Contaminated by Lead after Bench-scale In-situ Washing with FeCl3 (납 오염 논토양의 원위치 세척을 위한 FeCl3의 Bench-scale 적용성 평가: 세척전후 토양 특성변화)

  • Koh, Il-Ha;Kim, Gi Suk;Chang, Yoon-Young;Yang, Jae-Kyu;Moon, Deok Hyun;Choi, Yulim;Ko, Myoung-Soo;Ji, Won Hyun
    • Journal of Soil and Groundwater Environment
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    • v.22 no.1
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    • pp.18-26
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    • 2017
  • In a previous study, we assessed the feasibility of ferric chloride ($FeCl_3$) as a washing agent in bench-scale in-situ soil washing to remove Pb from agricultural paddy soil. Herein is a subsequent study to evaluate variations in soil properties after $FeCl_3$ soil washing in terms of fractionation and bioavailability of Pb and chemical properties of the soil. After soil washing, the soil pH decreased from 4.8 to 2.6 and the exchangeable fractions of Pb in the soil increased from 12 mg/kg to 15 mg/kg. Variations in the Pb fractionation of the soil increased Pb bioavailability by almost three-fold; however,the base saturation decreased by 75%. The concentrations of total nitrogen and available phosphate were similar before and after soil washing. The available silicate concentration significantly increased after soil washing but was two times lower than that of soil washed with HCl, which is widely used as a washing agent. This indicates that $FeCl_3$ can be an acceptable washing agent that protects the soil clay structure. The results suggest that soil amendment, such as liming, is needed to recover soil pH, reduce mobility of Pb, and provide exchangeable bases of Ca, Mg, and K as essential elements for the healthy growth of rice plants in reused soil that has been washed.

Performance Analysis of an ORC System for Two Different Working Fluids (두 종류의 다른 작동유체가 ORC 시스템의 성능에 미치는 영향)

  • Chang, Hong-Soon;Song, Yeong-Kil;Han, Young-Sub
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.25 no.7
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    • pp.413-417
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    • 2013
  • The organic Rankine Cycle (ORC) uses a kind of refrigerant as a working fluid that evaporates at relatively low temperature, as the Rankine Cycle uses superheated steam as the working fluid. A small scale ORC test bench was installed, and two different working fluids (R245fa and R134a) were injected into the test bench. The test bench was in operation with the two different working fluids under the same conditions. The effects against the system performance from the different working fluids were analysed, and root causes were identified. Other factors reflecting the power generation efficiency were also found. A conclusion was drawn, that R245fa makes the system perform better, than R134a.

Experimental Evaluation of Developed Ultra-low NOx Coal Burner Using Gas in a Bench-scale Single Burner Furnace (Bench-scale 연소로에서 가스 혼소를 통한 초 저 NOx 석탄 버너 개발 연구)

  • Chae, Taeyoung;Lee, Jaewook;Lee, Youngjae;Yang, Won
    • Clean Technology
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    • v.28 no.2
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    • pp.117-122
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    • 2022
  • This study developed and tested an ultra-low NOx burner in an 80 kW combustion furnace. The experiment was conducted in an 80 kW single burner combustion furnace with changing the swirl numbers, total equivalence ratios, and primary/secondary oxidizer ratios. In this study, liquefied natural gas (LNG) was used as an auxiliary fuel to significantly reduce NOx production. In a thermal power plant, the amount of NOx generated during coal combustion is about 300 ppm. However, using the burner tested in this study, it was possible to reduce the amount of NOx generated via LNG co-firing to 40 ppm. If the input amount of the primary oxidizer is enough for the gas to be completely combusted and the gas and coal are added simultaneously, the combusted gas forms a high-temperature region at the burner outlet and volatilizes the coal. As a result, the N contained in the devolatilized coal is discharged. Therefore, when the coal is subsequently burned, the amount of NOx produced decreases because there is almost no N remaining in the coal. If a thermal power plant burner is developed based on the results of this study, it is expected that the NOx generation will be significantly lower in the early stage of combustion.

Steam reforming of biomass tar over Ni/Ru-x/Al2O3 catalysts (Ni/Ru-x/Al2O3 촉매를 이용한 바이오매스 타르 개질)

  • Yoon, Sang Jun;Oh, Kun Woong;Park, Seo Yoon;Kim, Yong Gu;Seo, Myung Won;Ra, Ho Won;Lee, Jae-Goo
    • 한국연소학회:학술대회논문집
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    • 2014.11a
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    • pp.355-356
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    • 2014
  • Catalytic steam reforming of tar produced from biomass gasification was conducted using several Ni-based catalysts. K and Mn were used as a promoter over $Ni/Ru/Al_2O_3$ catalyst. The pellet and monolith type catalysts were prepared and applied to lab and bench-scale biomass gasification system. The $Ni/Ru-K/Al_2O_3$ catalyst shown higher performance than $Ni/Ru-Mn/Al_2O_3$ catalyst at low temperature range.

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Polystyrene Supported Al(OTf)3: a Stable, Efficient, Selective, and Reusable Catalyst for Sulfonylation of Arenes with Sulfonic Acids

  • Boroujeni, Kaveh Parvanak
    • Bulletin of the Korean Chemical Society
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    • v.31 no.7
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    • pp.1887-1890
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    • 2010
  • Cross-linked polystyrene supported aluminium triflate (Ps-Al(OTf)$_3$) was found to be an efficient and chemoselective heterogeneous Lewis acid catalyst for the direct conversion of arenes to sulfones using sulfonic acids as sulfonylating agents. The solid acid catalyst is stable (as a bench top catalyst) and can be easily recovered and reused without appreciable change in its efficiency.

Preparation of PVDF Hollow Fiber Membrane and Absorption of SO2 from Flue Gas Using Bench Scale Gas-Liquid Contactor (PVDF 중공사막 제조 및 벤치규모 기-액 접촉기를 이용한 SO2 흡수특성)

  • Park, Hyun-Hee;Jo, Hang-Dae;Kim, In-Won;Lee, Hyung-Keun
    • Korean Chemical Engineering Research
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    • v.46 no.3
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    • pp.521-528
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    • 2008
  • The micro-porous asymmetric PVDF hollow fiber membranes for gas-liquid contactor were prepared by the dry-jet wet phase inversion process and the characteristics of hollow fiber membranes were evaluated by the gas permeation method and scanning electron microscope. The chemical absorbent for removal of $SO_2$ gas was sodium hydroxide at bench scale hollow fiber membrane contactor. The experiments were performed in a counter-current mode of operation with gas in the shell side and liquid in the fiber lumen of the module to examine the effect of various operating variables such as concentration of absorbent, gas flow rate, L/G ratio and concentration of inlet $SO_2$ gas on the $SO_2$ removal efficiency using PVDF hollow fiber membrane contactor. Membrane mass transfer coefficient($k_m$) was calculated by mathematical modeling. The volumetric overall mass transfer coefficient increased with increasing the concentration of absorbent and L/G ratio. The increase of the absorbent concentration and L/G ratio not only provides more sufficient alkalinity but also decreases liquid phase resistance. The volumetric overall mass transfer coefficient increased with increasing gas flow rate due to decreasing the gas phase resistance.