• Title/Summary/Keyword: Variable Guide Vanes

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Development of Variable Guide Vane Actuator System for Testing of Aircraft Gas Turbine Engine (항공용 가스터빈 리그시험용 가변정익 구동시스템 개발)

  • Kim, Sun Je;Jeong, Chi Hoon;Ki, Taeseok
    • Journal of the Korean Society of Propulsion Engineers
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    • v.23 no.3
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    • pp.9-17
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    • 2019
  • Variable guide vanes(VGVs) that consist of link mechanisms and an actuator system are required for an aircraft gas turbine engine to adjust the incidence angle of stator vanes. In this study, we developed a VGV actuator system for three-stage VGVs with two hydraulic actuators. The requirements for the actuator system were derived by analyzing the link mechanisms and air loads, and a hydraulic power-pack was developed based on these requirements. Through a load test using the actuator test-rig and the application of synchronizing control logic with proper control gains, the actuator system could be developed and verified.

Active Surge Control with Variable Inlet Guide Vane

  • Choi, Wook-Jin;Kim, Sang-Un;Won, Sang-Chul
    • 제어로봇시스템학회:학술대회논문집
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    • 2004.08a
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    • pp.1211-1214
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    • 2004
  • In this paper, we propose to use variable inlet guide vane as a means of active surge control to solve above problems. There is some advantage. For example, since the inlet guide vanes are already present in POSCO, no additional actuation device is required. We can collect all data easily which is related to the test and can simulate new model using our compressors. We can obtain the result that blow-off valve is opened less 5% and can operate air compressor automatically and more efficiently. Through a simulation example, the effectiveness of the proposed schemes is illustrated.

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Effective Performance Prediction of Axial Flow Compressors Using a Modified Stage-Stacking Method (단축적법의 개선에 의한 축류압축기의 효과적인 성능예측)

  • Song, Tae-Won;Kim, Jae-Hwan;Kim, Tong-Seop;Ro, Sung-Tack
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.24 no.8
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    • pp.1077-1084
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    • 2000
  • In this work, a modified stage-stacking method for the performance prediction of multi-stage axial flow compressors is proposed. The method is based on a simultaneous calculation of all interstage variables (temperature, pressure, flow velocity) instead of the conventional sequential stage-by-stage scheme. The method is also very useful in simulating the effect of changing angles of the inlet guide vane and stator vanes on the compressor operating characteristics. Generalized stage performance curves are used in presenting the performance characteristics of each stage. General assumptions enable determination of flow path data and stage design performance. Performance of various real compressors is predicted and comparison between prediction and field data validates the usefulness of the present method.

Design and Performance Test of SCR Pilot Plant($1,000Nm^{3}/hr$) ($1,000Nm^{3}/hr$급 SCR Pilot Plant의 설계 및 성능실험)

  • Kim, J.I.;Chang, I.G.;Seon, C.Y.;Kim, J.S.;Chon, M.H.
    • Proceedings of the KSME Conference
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    • 2001.06d
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    • pp.979-984
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    • 2001
  • As a preceding process for developing design technology and establishing operation technology, the design procedure of the SCR(Selective Catalytic Reduction) pilot plant that can handle $1,000Nm^{3}/hr$ of flue gas was reported in this paper. And we also considered several factors that might cause abnormality of the plant in the designing process. The plant was designed and fabricated to test the $DeNO_{x}$ performances in variable operating conditions in the range of $3,000{\sim}36,000hr^{-1}/hr$ in space velocities, $1.67{\sim}6\;m/s$ in linear velocities, $200{\sim}500^{\circ}C$ temperatures, $300{\sim}1,000Nm^{3}/hr$ flow rates, and $0{\sim}1.4:1\;NH_{3}/NO$ ratios. In order to maintain the flow uniformity, the guide vanes and flow straightener were designed and constructed in the plant. The SCR pilot plant can be operated by the automatic control system, which enable to obtain performance data in real time and to set up the operating technology. The catalyst reactor consists of 4 catalyst layers and surface area of each layer can be adjusted to be of small size. Arrangement of catalysts per layer is $3{\times}6$ with the catalyst dimensions of $150{\times}150{\times}500mm(L{\times}W{\times}H)$.

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