• 제목/요약/키워드: Bed Temperature

검색결과 1,044건 처리시간 0.023초

Sludge Pellet의 NOx제거특성에 미치는 온도의 영향 (Effect of heating temperature to remove NOx by sludge pellet)

  • 김영주;박재윤;박홍재;송원섭;박상현;배명환
    • 한국전기전자재료학회:학술대회논문집
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    • 한국전기전자재료학회 2002년도 하계학술대회 논문집 Vol.3 No.2
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    • pp.922-926
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    • 2002
  • In this paper, in order to investigate the catalytic effect of the sludge exhausted from waterworks as heating temperature for NOx removal, we measure NO, $NO_2$ concentration as increasing temperature of sludge pellets and applying high voltage to sludge pellets in a quartz-glass reactor at the same time. NO initial concentration is 100ppm balanced with air gas in a mixing chamber. The gas flow is 5[l/min] and the heating temperature of sludge pellets in a quartz-glass reactor is adjusted from $200[^{\circ}C]$ $400[^{\circ}C]$ to investigate the effect of sludge pellets for removal NOx$(NO+NO_2)$ as increasing temperature. $BaTiO_3$ pellets is filled in a packed-bed reactor for corona discharge to measure how much NOx$(NO+NO_2)$ is removed after generating $NO_2$ from the packed-bed reactor. AC[60Hz] voltage is supplied to the reactor for discharge. In the result, $NO_2$ concentration is decreased by sludge pellets without heating temperature for sludge pellets in case of sludge pellets done heat treatment, however NO concentration is almost the same to be compared NO initial concentration. As increasing heating temperature for sludge pellets, $NO_2$ adsorbed on the sludge surface done heat treatment is converted to NO by the thermal energy, so NO concentration is extremely increased by reduction decomposition of $NO_2$. Finally, We think the sludge is possible to use for reduction catalysts, however we need to study more about the possibility and endurance of sludge as catalysts for NOx removal.

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초저이온 농도범위에서 혼합층 이온교환능과 온도의 영향 - 2. 온도의 영향 - (The Mixed-Bed Ion Exchange Performance and Temperature Effects at Ultra-Low Concentrations - 2.Temperature Effects -)

  • 윤태경;노병일;이창원;문병현;이강춘;조명찬
    • 공업화학
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    • 제10권2호
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    • pp.206-211
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    • 1999
  • 본 연구에서는 NaCl수용액의 초저이온 농도범위 ($1.0{\times}10^{-4}M$ 이하)에서 양이온 교환수지 대 음이온 교환수지의 비, 수지량, 계의 온도를 함수로 한 혼합층 이온교환의 거동을 실험적으로 연구하였다. 실험실 크기의 연속흐름 칼럼을 통하여 양이온 교환수지와 음이온 교환수지의 교환능이 소모될 때까지의 유출농도를 처리된 유량의 함수로 측정하여 파과곡선을 구하였다. 초기누출은 수지량이 적은 경우 양이온과 음이온의 파과곡선에 나타났으나, 선택도계수가 낮은 양이온의 파과곡선에 현격하게 크게 나타났다. 선택도계수는 파과곡선의 기울기에 영향을 미쳤으며, 계수값이 큰 음이온의 파과곡선의 기울기가 급격하였다. 온도변화는 파과곡선의 기울기에 영향을 미쳤으며, 온도가 증가할수록 이온교환속도가 증가하였다. 이 온도효과는 수지비에 관계없이 수지총량이 증가할수록 또는 이온교환수지의 교환능이 감소하여 파과곡선이 평형에 가까워질수록 감소하였다.

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촉매연소기에서 2단 공급공기와 연료가 NOx 저감에 미치는 연구 (NOx Reduction with Secondary Air and Fuel in a Catalytic Combustor)

  • 정진도;이보영
    • 한국대기환경학회지
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    • 제19권5호
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    • pp.541-549
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    • 2003
  • A basic experimental study was conducted in order to find the optimum combustion control technology to decrease the thermal NO$_{x}$, by applying the catalytic combustion method with natural gas. NO$_{x}$ emission increased with increasing space velocity due to temperature rising in the furnace. In order to overcome the low resistance to high temperature, secondary air was supplied to the CST combustor. The following secondary fuel formed combustible mixture in part, which resulted in steep increase of the exiting temperature of the 2nd catalyst bed. It led to the more generator of NO$_{x}$, 30∼60% of the 1 st catalyst bed. It might be due to the potential increase of thermal NO$_{x}$.

유동층 열분해로에 의하여 생산된 상수리나무 바이오오일의 특성 (Characteristics of Bio-oil derived from Quercus Acutissima in a Fluidized Bed Pyrolyser)

  • 이선훈;엄민섭;유경선;이영수;김남찬;이시훈;이재구;김재선
    • 자원리싸이클링
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    • 제15권1호
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    • pp.3-11
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    • 2006
  • 유동층 열분해로에서 상수리나무의 급속열분해를 수행하고 생성된 바이오오일의 물리화학적 특성을 GC/MS를 이용하여 분석하였다. 유동층 열분해로에서 얻어진 상수리나무와 낙엽송의 바이오오일 수율은 각각 $350^{\circ}C,\;400^{\circ}C$에서 최대치를 보였으며 이는 두 수종간의 셀룰로오스 함량차이에 기인하는 것으로 추정된다. 최적온도 이상에서는 반응온도가 증가할수록 프리보드에서의 2차 열분해에 의하여 촤와 오일의 수율이 감소하였고 가스상 성분과 수분의 함량이 증가하였다. 유등층 열분해로에서 시료의 투입량은 생성물의 수율과 조성에는 큰 영향을 주지 않았으며 이는 충분한 혼합이 이루어지기 때문으로 판단되었다.

금속산화물을 이용한 유동층반응기에서 배연탈황특성 (The Characteristics of Desulfurization using Metal Oxides in a Fluidized Bed Reactor)

  • 박태성;홍성창
    • 공업화학
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    • 제9권2호
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    • pp.278-285
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    • 1998
  • 배출가스중의 $SO_2$ 제거를 위하여 다양한 금속산화물로 구성된 천연망간광석, 철광석, $CuO/{\gamma}-A1_2O_3$ 등을 흡착제로 사용하여 고정층반응기에서 흡착용량실험을 하였다. 또한 흡착제중 흡착용량이 떨어지는 철광석을 제외한 두 가지 흡착제를 이용하여 유동층반응기에서 유속, 온도, 입자크기 등의 조업조건에 따른 $SO_2$ 흡착실험을 수행하였다. 모든 흡착제에서 온도가 증가할수록 흡착량이 증가하는 화학흡착반응을 보였고 유동층반응기에서 $U_o/U_{mf}$$U_o-U_{mf}$와 같은 유속조건에 따라 입자 크기에 따른 흡착량의 변화가 다르게 나타났으며 유동층반응기 성능식으로부터 반응속도상수를 얻었다. 이 실험을 통하여 천연망간광석이 유동층반응기에서 $SO_2$ 흡착제로의 사용가능성을 확인할 수 있었다.

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기본간호학 실습교육현황과 실습내용 개선을 위한 조사 연구 (A Study on the Contents of Fundamental Nursing Practice)

  • 이영휘;서화숙
    • 대한간호학회지
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    • 제28권3호
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    • pp.650-661
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    • 1998
  • The purpose of this study was to provide fundamental data for determining contents of Fundamental Nursing Practice and developing desirable bedside nursing techniques for clinical nursing areas. Subjects for this study were 86 nurses who were employees of two university hospitals located in Seoul and a district area. Data were collected by questionnaires. Items of Fundamental Nursing Practice were classified into 72 items according to the result from content analysis of 9 textbooks of Fundamental Nursing. The results are as follows : 1) Items which above 80% of respondents practiced during the school inside practice or clinical nursing practice course were axillary temperature measurement, radial pulse measurement, respiratory rate measurement, application of oral hygiene, hand-washing technique, application of hot and cold bags, intramuscular injection technique, open bed-making, soap enema method, application of nelaton catheterization and oral and nasal suction methods. 2) Above 90% of respondents replied that all items except temperature measurement and bed-making were requisite contents for Fundamental Nursing Practice. Above 10% of respondents replied oral and rectal temperature measurement and bed-making were unnecessary content. 3) Above 90% of respondents replied that operating methods of all items except isolation technique, admission and discharge procedures, and retention enema in the Fundamental Nursing Practice course and clinical situation were consistent. The main reasons that respondents did not apply methods which they learned in the Fundamental Nursing Practice course to the clinical situation were 'insufficient time', 'colleagues were using different methods', 'insufficient supply of instuments' or 'inappropriate appliances'.

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고온수소 전환 반응기에 관한 수치해석적 연구 (Numerical Study on High Temperature CO-Shift Reactor in IGFC)

  • 서동균;이진향;지준화;홍진표;오석인
    • 한국수소및신에너지학회논문집
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    • 제29권4호
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    • pp.324-330
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    • 2018
  • In this study a numerical study was conducted to show flow, temperature and gas distributions in a high temperature CO shift reactor which was designed specially for energy saving and then evaluated with the related experiment. Mole fractions of syngas at the end of the catalyst bed were predicted with various assumed pre-exponential factors, were compared with the corresponding experimental results and $10^8$ was finally selected as the value. With the selection, a base case was examined. It was calculated that the inlet duct attached asymmetrically to the CO shift reactor affects on the distribution of the upward momentum (+z directional). In addition, CO conversion ratio is achieved up to 90% in the catalyst bed and especially it reached up to 70% at the initial part of catalyst bed.

가압 유동층 반응기에서 산소공여입자의 메탄 연소 특성에 미치는 온도, 압력 및 기체체류시간의 영향 (Effects of Temperature, Pressure, and Gas Residence Time on Methane Combustion Characteristics of Oxygen Carrier Particle in a Pressurized Fluidized Bed Reactor)

  • 류호정;박상수;문종호;최원길;이영우
    • 한국수소및신에너지학회논문집
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    • 제23권2호
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    • pp.173-182
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    • 2012
  • Effects of temperature, pressure, and gas residence time on methane combustion characteristics of mass produced oxygen carrier particle (OCN706-1100) were investigated in a pressurized fluidized bed reactor using methane and air as reactants for reduction and oxidation, respectively. The oxygen carrier showed high fuel conversion, high $CO_2$ selectivity, and low CO concentration at reduction condition and very low NO emission at oxidation condition. Moreover OCN706-1100 particle showed good regeneration ability during successive reduction-oxidation cyclic tests up to the 10th cycle. Fuel conversion and $CO_2$ selectivity decreased and CO emission increased as temperature increased. These results can be explained by trend of calculated equilibrium CO concentration. However, $CO_2$ selectivity increased as pressure increased and fuel conversion increased as gas residence time increased.

국내 무연탄의 순환류동층 보일러에서 탈황 특성 연구 (A Study of Desulfation Characteristics of Circulating Fluidized Bed Combustion for Domestic Anthracite)

  • 정진도;김장우;하준호
    • 한국대기환경학회지
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    • 제20권4호
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    • pp.429-436
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    • 2004
  • Circulating fluidized bed combustion (hereafter CFBC) technology enables an efficient combustion for the materials with low heating values such as high ash coal and sludges. It also has desulfation function by adding limestone directly to combustor. The CFBC has been considered as one of the best processes for low grade coal containing with large contents of ash and sulfur. In this paper, in order to various tests were performed to find the optimum desulfation condition for CFBC using Korean Anthracite. We surveyed possible parameters and conducted desulfation efficiency test in D Thermal Power Plant. In addition, the result of some fundamental theoretical consideration was discussed with CFBC. Optimum limestone size could be considered to be 0.1-0.3mm irrespective of combustion temperature and Ca/S molar ratio variation. Desulfation efficiency increased as the molar ratio increased. Because desulfation process occurs at the surface at higher temperature, inner side of limestone can't be utilized. When surface area is not appropriate, some SO$_2$ emit without reaction. Optimum molar ratio should be decided after considering chemical and physical properties of limestone and coal thoroughly such as particle size, pore size and HGI. Commercial CFBC is operated at Ca/S 1.6. Combustor temperature 840-87$0^{\circ}C$ shows good desulfation efficiency.

고온건식탈황을 위한 유동층반응기 특성연구 (The Characteristics of Desulfurization for Dry-Type High Temperature in a Fluidized Bed Reactor)

  • 장현태
    • 한국안전학회지
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    • 제14권1호
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    • pp.78-85
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    • 1999
  • The removal characteristics of H$_2$S from IGCC process over the natural manganese ore(NMO) containing several metal oxides($MnO_x$ : 51.85%, $FeO_y$ : 3.86%, CaO : 0.11%) were carried out in a batch type fluidized bed reactor(I.D.=40mm, height=0.8m). The $H_2S$ breakthrough curves were obtained as a function of temperature, initial gas velocity, initial gas concentration, and aspect ratio. The effect of particle size ratio and particle mixing fraction on $H_2S$ removal were investigated with binary system of different particle size. From this study, the adsorption capacity of $H_2S$ increased with temperature but decreased with excess gas velocity. The breakthrough time for $H_2S$ is reduced as the gas velocity is increased which leaded to gas by-passing and gas-solid contacting in a fluidized bed reactor. The results of the binary particle system with different size in batch experimental could predict to improve the behavior of continuous process of $H_2S$ removal efficiency. The natural manganese ore could be considered as potential sorbent in $H_2S$ removal.

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