• 대한기계학회논문집
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• 제11권6호
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• pp.982-990
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• 1987

본 연구에서는 참고문헌(12)에서 배제된 머플러와 플래퍼밸브의 운동을 추가 시킴으로써 앞의 모델보다 실제장치에 근접시켜 보다 정확한 열적 및 동적거동을 예측 하고, 또한 컴퓨터 시뮬레이션의 수행시 계산시간을 줄여 정상운전상태의 결과를 얻고 자 한다.

• 한국가스학회지
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• 제23권6호
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• pp.8-16
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• 2019

저공해 연소를 위한 방법 중 하나인 배기가스 재순환(flue gas recirculation, 이하 FGR)은 질소산화물 저감에 효과적인 연소 기법이다. 이를 메탄/공기 대향류 예혼합화염에 적용하여 화염의 특성변화와 NOx 생성 기구를 파악하기 위한 수치해석을 진행하였다. 신장률에 따라 배출되는 생성물들의 몰분율이 달라진다는 점을 고려하여 재순환율은 생성물을 기준으로 정의되었으며, 실제 연소 시스템을 반영하기 위해 주요 생성물인 CO₂, H₂O, O₂ 그리고 N₂를 희석제로써 재순환하였다. FGR 기법이 적용됨에 따라 특정한 신장률 조건에서 최대화염 온도의 전환점이 발견되었다. 또한, 재순환율이 증가함에 따라 온도와 NO의 경향이 달리 나타났으며, 이를 파악하고자 NO 반응을 열적 NO와 Fenimore NO로 구분하여 분석하였다.

• 대한기계학회논문집B
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• 제34권8호
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• pp.775-782
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• 2010

본 연구는 대형 석탄 화력 발전소 탈황설비 내 흡수탑의 성능향상을 위하여 Tray 설치 가능성을 검토하기 위한 연구로 전산 유체역학(CFD) 기법을 이용하여 탈황설비 내 흡수탑의 내부유동을 전산해석 하였다. 흡수탑 내의 Gas와 Slurry의 거동에 대한 사실적 묘사를 위해 Euler-Lagrangian 기법을 이용한 전산해석을 수행하였다. 기존 흡수탑 내에 Tray를 설치함에 따라 탈황설비 내에서 Slurry의 체공시간 증가로 인한 펌프동력 절감과 압력강하 증가로 인한 Fan의 소요동력 증가에 대하여 중점적으로 비교 및 고찰하였다. 그 결과 Tray를 설치함에 따라 흡수탑 내에 Slurry의 체공시간과 배기가스의 압력강하가 증가되는 것을 확인할 수 있었다. 체공시간 증가로 인하여 절약된 동력이 압력강하에 의한 동력 소모량 증가보다 더 큰 것으로 확인되었다.

• 한국가스학회지
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• 제24권4호
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• pp.39-47
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• 2020

배기가스 재순환(flue gas recirculation, 이하 FGR)은 질소산화물 저감에 효과적인 연소 기법으로 저공해 연소 분야에 다양하게 응용되고 있다. 이전 연구에 이어서 메탄/공기 대향류 예혼합화염에 FGR 기법 적용 시 나타나는 화염의 특성 변화 및 NOx 생성기구를 파악하기 위한 수치해석이 진행되었다. 배출되는 질소산화물(NOx)은 4가지 주요 반응경로(열적 NO, prompt NO, N₂H 및 N₂O)로 구분하여 배기가스 재순환율에 따른 각 NO 생성률을 상대적으로 나타내었다. 그 결과 열적 NO가 전체 NO 형성에 가장 크게 차지한 반면 N₂H의 영향은 미미하였다. 또한, 열적 NO의 기여를 검토하기 위하여 본 연구에 사용된 반응기구(UC San Diego mechanism)를 수정하여 재순환율 증가에 따른 NO 배출지수(EINO)를 비교하였다.

• 한국연소학회지
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• 제10권1호
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• pp.1-6
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• 2005

This paper presents the combustion characteristics of hydrocarbon fuel from a conventional pressure-swirl nozzle of a small-scale burner. The nozzle has orifice diameters of 0.256 mm and liquid flow rates ranging from 50 to 64 mL/min were selected for the experiments. The furnace temperature distribution along the axial distance, the gas emission such as CO, $CO_2$, NOx, $SO_2$, flue gas temperature, and combustion efficiency were studied. The local furnace and flue gas temperatures decreased with an increase in air velocity. At injection pressures of 1.1 and 1.3 MPa the maximum furnace temperatures occurred closer to the burner exit, at an axial distance of 242 mm from the diffuser tip. The CO and $CO_2$concentrations decreased with an increase in air velocity, but they increased with an increase in injection pressure. The effect of air velocity on NOx was not clearly seen at low injection pressures, but at injection pressure of 1.3 MPa it decreased with an increase in air velocity. The effect of air velocity on $SO_2$ concentration level is not well understood. The combustion efficiency decreased with an increase in air velocity but it increased with an increase in injection pressure. It is recommended that injection pressure less than 0.9 MPa with air velocity not above 8.0 m/s would be suitable for this burner.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 2005년도 동계 학술대회 논문집
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• pp.76-82
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• 2005

This paper presents the combustion characteristics of hydrocarbon fuel from a conventional pressureswirl nozzle of a small-scale burner. The nozzle has orifice diameters of 0.256 mm and liquid flow rates raging from 50 to 64 mL/min were selected for the experiments. The furnace temperature distribution along the axial distance, the gas emission such as CO, $CO_2,\;NOx,\;S0_2,$ flue gas temperature, and combustion efficiency were studied. The local furnace and flue gas temperatures decreased with an increase in air velocity. At injection pressures of 1.1 and 1.3 MPa the maximum furnace temperatures occurred closer to the burner exit, at an axial distance of 242 mm from the diffuser tip. The CO and $CO_2$ concentrations decreased with an increase in air velocity, but they increased with an increase in injection pressure. The effect of air velocity on NOx was not clearly seen at low injection pressures, but at injection pressure of 1.3 MPa it decreased with an increase in air velocity. The effect of air velocity $SO_2$ concentration level is not well understood. The combustion efficiency decreased with an increase in air velocity but it increased with an increase in injection pressure. It is recommended that injection pressure less than 0.9 MPa with air velocity not above 8.0 m/s would be suitable for this burner.

• Carbon letters
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• 제3권4호
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• pp.187-191
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• 2002

In the present research, we prepared the activated carbon (AC) sorbents to remove gas-phase mercury. The mercury adsorption of virgin AC, chemically treated AC and fly ash was performed. Sulfur impregnated and sulfuric acid impregnated ACs were used as the chemically treated ACs. A simulated flue gas was made of SOx, NOx and mercury vapor in nitrogen balance. A reduced mercury adsorption capacity was obtained with the simulated gas as compared with that containing only mercury vapor in nitrogen. With the simulated gas, the sulfuric acid treated AC showed the highest performance, but it might have the problem of corrosion due to the emission of sulfuric acid. It was also found that the high sulfur impregnated AC also released a portion of sulfur at $140^{\circ}C$. Thus, it was concluded that the low sulfur impregnated AC was suitable for the treatment of flue gas in terms of stability and efficiency.

• 설비공학논문집
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• 제16권3호
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• pp.273-279
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• 2004

A lab-scale fluidized bed heat exchanger for waste gas heat recovery is devised and tested. Compared to our previous works on fluidized bed type system with a single riser, the present heat exchanger system is featured by its multiple (four) risers to handle increased amount of exhaust gas. Particles are introduced to the main hot gas stream alongside the pipe circumference near riser inlets. The heat exchanger performance and pressure drop are evaluated through experiments for the present gas-to-water heat exchanger system.

• 해양환경안전학회:학술대회논문집
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• 해양환경안전학회 2018년도 공동국제학술발표회
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• pp.198-198
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• 2018

• 한국환경보건학회지
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• 제29권1호
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• pp.34-42
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• 2003

The objective of this study is to investigate the waste recycling possibility, practicability, economic efficiency and acid gas sorbent use of the hard-shelled mussel. This study is to investigate the hydration/calcination reaction and fixed bed reactor. The physical-chemical characteristics of the hard-shelled mussel were analyzed by ICP SEM-EDX, BET and pore volume. Thus, the results could be summarized as follows; Hard-shelled mussel can be used as iron-manufacture and chemical sorbents considering more than 53.7% of the mussel is lime content. The SO$_2$removal efficiency of the hard-shelled mussel after calcined hydration increased thirty times as a result of the higher pore size, specific surface area and pore volume. Also, the CaO content, pore volume, pore size distribution and specific surface area greatly influenced the SO$_2$ and NOx removal reactivity. The optimum particle diameter average of hard-shelled mussel was $\pm$100 mesh, which was applied to the sorbent on the medium/small scale waste incinerator and flue gas desulfurization processes.