• 제목/요약/키워드: 다층 다단 다공성 플레이트

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임팩션 효과에 편극전하 방식을 부가한 다층 다단 다공성 플레이트 시스템의 집진특성 (Dust Collection Characteristics of Multi-layer Multi-stage Porous Plate System with Polarization Charge to Impaction Effect)

  • 김보배;김일규;여석준
    • 대한환경공학회지
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    • 제33권8호
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    • pp.598-605
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    • 2011
  • 본 연구의 주 목적은 다층 다단 다공성 시스템에 편극전하 방식을 부가하여 본 시스템의 집진특성을 실험적으로 해석하는데 있다. 본 시스템의 압력손실 및 집진효율 특성 해석을 위해 실험은 인가전압, 시스템 유입유속, 유입농도 및 stage 수 등의 실험적 변수들에 의해 수행된다. 실험결과, 기류유입 시 유입유속 $v_{in}$ = 3.11 m/s에서 단(stage) 수 변화($1{\rightarrow}5$단)에 따라 압력손실은 $18{\sim}134mmH_2O$를 나타낸다. 인가전압 0 kV 및 기류유입이 없을 때, 시스템 유입유속 $v_{in}$ = 2.58 m/s인 경우 5 stage에서 집진효율은 92.5% 인 데 비해, 동일 유속에서 플레이트 별 편극전하(alternating polarization charge-applied voltage 2.5 kV) 및 기류유입 시스템인 경우 5 stage 효율은 98.5%로 전자에 비해 6% 정도 매우 높은 효율 상승을 보인다.

다층 다단 다공성 플레이트 시스템의 집진 특성 (Collection Characteristics of Multi-layer Multi-stage Porous Plate System)

  • 김일규;여석준
    • 동력기계공학회지
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    • 제14권5호
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    • pp.10-16
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    • 2010
  • The main object of this study is to investigate the collection characteristics of multi-layer multi-stage porous plate system experimentally. The experiment is carried out to analyze the characteristics of pressure drop and collection efficiency for the present system with the experimental parameters such as inlet velocity, tube diameter, inlet concentration, and stage number, etc. In results, the pressure drop becomes 22 to $115mmH_2O$ with increment of stage number (1 to 5) of porous plate system at tube velocity 15 m/s and tube diameter ${\Phi}8$. In case of fly ash and 5 stage, the collection efficiency becomes 90.5 to 95.7% increasing the tube velocity 12 to 15 m/s at inlet concentration $3g/m^3$ and tube diameter ${\Phi}8$. Additionally, it is estimated that the collection efficiencies of 5 stage are 94.3, 95.6 and 99.1% for fly ash, steel dust and based power, respectively (${\Phi}8$ tube, $V_t$ = 12m/s, inlet concentration $3g/m^3$).

이오나이저 및 유전체 방식을 도입한 다층 다단 다공성 플레이트 시스템의 집진특성 (Dust Collection Characteristics of Multi-layer Multi-stage Porous Plate System with Ionizer and Dielectric-substance)

  • 여석준
    • 동력기계공학회지
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    • 제17권6호
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    • pp.63-72
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    • 2013
  • The main purpose of this study is to analyze the collection characteristics of multi-layer multi-stage porous plate system with ionizer and dielectric-substance experimentally. The experiment is carried out to analyze the characteristics of pressure drop and collection efficiency for the present system with experimental parameters such as applied voltage, inlet velocity, stage number and inlet particle concentration, etc. In results, for multi-layer multi-stage porous plate system of inflow type, at 5 stage and $v_{in}$=2.58 m/s, the pressure drop becomes lower 15 $mmH_2O$ as 95 $mmH_2O$ than that of non-inflow type system. It is estimated that for the present system with ionizer and dielectric-substance, the collection efficiency represents 98.5% showing higher 5.2% comparing to that of multi-layer multi-stage porous plate system without ionizer and dielectric-substance at 5 stage, $v_{in}$=2.58 m/s and inlet concentration $3g/m^3$(fly ash).

습식 다층 다단 다공성 플레이트 시스템의 집진특성 (Collection Characteristics of Wet-type Multi-layered and Multi-staged Porous Plate System)

  • 여석준;김주연
    • 동력기계공학회지
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    • 제18권3호
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    • pp.42-50
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    • 2014
  • The main object of this study is to investigate the collection characteristics of wet-type multi-layered and multi-staged porous plate system experimentally. The experiment is carried out to analyze the characteristics of pressure drop and collection efficiency for the present system with the experimental parameters such as water spray, inlet velocity, stage number and inlet particle concentration, etc. In results, for the present system of wet-type, the pressure drop represents 158 $mmH_2O$ higher 3% than that in dry-type at 5 stage and $v_{in}$=3.53 m/s. In case of 5 stage, $v_{in}$=3.53 m/s and water spray 250 ml/min, the collection efficiency of the present system becomes significantly higher as 99.7% comparing to that of the conventional wet-type scrubber. Additionally, for 5 stage and 250 ml/min, $SO_2$ removal efficiencies decrease with the increment of inlet velocity representing 75.0, 62.5, 50.0%, at $v_{in}$=2.12, 2.82, 3.53 m/s, respectively.