• 제목/요약/키워드: Packed Tower

검색결과 28건 처리시간 0.025초

흡수탑에서 VOCs 제거 기술개발을 위한 세정수의 특성연구

  • 김혜진;최상기;박문기;박상원;최성우
    • 한국환경과학회:학술대회논문집
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    • 한국환경과학회 2001년도 가을 학술발표회 발표논문집
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    • pp.44-45
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    • 2001
  • VOCs의 일종인 benzene을 흡수하기 위한 최적의 세정액으로 열매체유를 선정하여, 충진탑(Packed Tower), 흡수칼럼에 세정액만 채워 bubble 시킨 기포탑(Aeration Tower)와 충진물과 세정액을 채워 bubble 시킨 Combined Packed & Aeration Tower의 3가지 시스템을 비교한 결과 Combined Packed 쇼 Aeration Tower 시스템에서 benzene 흡수효율이 가장 좋았다.

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Experimental Study on Heat and Mass transfer Coefficient Comparison Between Counterflow Types and Parallel in Packed Tower of Dehumidification System

  • Sukmaji, I.C.;Choi, K.H.;Yohana, Eflita;Hengki R, R.;Kim, J.R.
    • 한국태양에너지학회:학술대회논문집
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    • 한국태양에너지학회 2009년도 춘계학술발표대회 논문집
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    • pp.162-169
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    • 2009
  • In summer electrical energy is consumed in very high rate. It is used to operate conventional air conditioning system. Hot and humid air can germinate mould spores, encourage ill health, and create physiological stress (discomfort). Dehumidifier solar cooling effect is the one alternative solution saving electrical energy. We use surplus heat energy in the summer, to get cooling effect and then to get human reach to comfort condition. These devices have two system, dehumidifier and regeneration system. This paper will be focus in dehumidifier system. Dehumidifier system use for absorbing moisture in the air and decreasing air temperature. When the liquid desiccant as strong solution contact with the vapor air in the packed tower, it works. The heat and mass transfer performances of flow pattern in the packed tower of dehumidifier are analyzed and compared in detail. In this experiment was introduced, the flow patterns are parallel flow and counter flow. The performance of these flow patterns will calculate from air side. Which is the best flow pattern that gave huge mass transfer rate? The proposed dehumidifier flow pattern will be helpful in the design and optimization of the dehumidifier solar cooling system.

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Study on the Performances of Air Flow Fate Effect on a Structured Packed Tower at Adiabatic Condition in a Liquid Lithium Chloride Cooling System

  • Bakhtiar, Agung;Choi, K.H.;Kim, J.R.
    • 한국태양에너지학회:학술대회논문집
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    • 한국태양에너지학회 2009년도 추계학술발표대회 논문집
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    • pp.404-408
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    • 2009
  • The liquid desiccant air-conditioning system has been proposed as an alternative to the conventional vapor compression cooling systems to control air humidity. The complete system of liquid desiccant air-conditioning system is consisted two main components those are humidifier (regeneration) and dehumidifier. Humidifier part is connected to the load when summer season which is the air condition is hot and humid have to be turned into comfort condition on human. This paper purpose is performances study of air flow rate effect on a structured packed tower on cooling and dehumidifier system using liquid lithium chloride as the desiccant. Experimental apparatus used in this present study is consisted of three components those are load chamber, packed tower and chiller. Load chamber’s volume is $40m^3$, and packed tower dimension is cubic with length 0.4m occupied with packed column. Totally, 15 experimental has done using 5 times repeat on each variable of air velocity that varying on 2m/s, 3m/s and 4m/s with other conditions are controlled. Air inlet initial temperature and relative humidity are set respectively on $30^{\circ}C$ and 52%, desiccant flow rate is 0.63 kg/s, desiccant temperature is $10^{\circ}C$ and desiccant concentration is 0.4. The result of this study shows that averagely, the moisture removal rate and the heat transfer rate are influenced by the air velocity. Higher air velocity will increase the heat transfer and decreasing the moisture removal rate. At adiabatic condition the air velocity of 2 m/s respectively is having the higher moisture removal rate acceleration then the air velocity of 3m/s and 4 m/s until the steady state condition.

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GaAs Scrap으로부터 熱分解法에 의한 갈륨 回收 (Recovery of Gallium from GaAs Scraps by Thermal Decomposition)

  • 최영윤;남철우;유연태;김완영
    • 자원리싸이클링
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    • 제14권2호
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    • pp.28-32
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    • 2005
  • 화합물반도체 제조 공정에서 발생하는 GaAs scrap으로부터 열분해법을 이용하여 갈륨을 회수하기 위한 기초 실험으로 200 g/batch 규모의 진공 열분해 실험을 수행하였고, 이 결과를 이용하여 30 kg/batch 용량의 Packed Tower가 부착된 열분해 장치를 제작하였다. 기초실험 결과 GaAs의 열분해속도는 온도가 높아짐에 따라 커지지만, 특히 1000$^{\circ}C 이상에서는 갈륨의 증기압 또는 증가하므로 갈륨의 회수율이 낮아지는 것을 알 수 있었다. 노 내 압력이 2~2.5${\times}10^{-2} mmHg일 때 1000~1050$^{\circ}C에서 가장 좋은 결과를 보였고, 이때 89% 정도의 갈륨 회수율을 나타내었다. GaAs의 열분해 시 비소의 분압은 온도가 높아짐에 따라 증가하고 융점인 1237$^{\circ}C를 전환점으로 온도는 낮아져도 증기압은 높은 이력현상(Hysteresis)을 보이는데, 이와 같은 특성을 이용하여 산업 생산에 적용한 열분해장치 제작에서는 반응기 위에 충진탑을 설치하였다. 그 결과, 열분해 반응기 내의 온도가 융점 이상의 고온에서도 99% 정도의 높은 회수율을 얻을 수 있었다.

Study Characteristics in Packed Tower of Liquid Desiccant Solar Cooling System Using Counter Flow Configuration

  • Rahmanto, R. Hengki;Choi, K.H.;Agung, B.;Sukmaji, I.C.
    • 한국태양에너지학회:학술대회논문집
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    • 한국태양에너지학회 2009년도 추계학술발표대회 논문집
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    • pp.168-174
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    • 2009
  • High water vapour content in air can cause a number of problems as for human or surrounding materials. For human a high water vapour can create physiological stress, discomfort, and also can encourage ill health. While, the cause for the environment is can accelerate the corrosion of metals, accelerate the growth of spores and mould, can reduce the electrical resistance of insulators and etc. Desiccant systems have been proposed as energy saving alternatives to vapor compression air conditioning for handling especially the latent load and also sensible load. Use of liquid desiccants offers several design and performance advantages over solid desiccants, especially when solar energy is used for regeneration. The liquid desiccants contact the gas inside the packed tower of liquid desiccant solar cooling system and the heat transfer and mass transfer will occur. This thesis is trying to study the characteristics inside the packed tower of dehumidifier systems. This characteristics consist of mass transfer rate, heat transfers rate, human comfort and energy that consume by the system. Those characteristics were affected by air flow rates, air temperature and humidity, and desiccant temperature and all that variation will influence the performance of the systems. The results of this thesis later on can be used to determine the best performance of the systems.

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유류오염토양으로부터 발생하는 VOC가스처리를 위한 바이오스크러버 개발 (Development of a Bioscrubber for Treatment of VOC Emissions from Contaminated Soil with Hydrocarbons)

  • 장윤영;황경엽;곽재호;최대기
    • 한국토양환경학회지
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    • 제2권1호
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    • pp.83-90
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    • 1997
  • 저농도의 난 수용성 VOC가스가 포함되어 있는 다량의 오염가스를 처리하기 위하여 흡수탑과 생물반응기의 결합체인 새로운 처리시스템을 제시하였다. 바이오스크러버의 스크러버에서는 세정액으로 기상중의 처리대상오염물질의 흡수가 일어나며 세정액은 생물반응기로 이송되어 호기성 미생물이 오염물을 분해시킨다. 본 연구에서는 폐가스중의 VOC분리를 위하여 재순환가능한 고비점용매를 사용하였다. 고비점용매를 포함한 세정액은 기/액 향류접촉이 이루어지는 흡수탑의 충전층에서 폐가스중의 오염물을 분리한다. 흡수탑은 Pall ring충전제로 채워 실제공정을 모사 하고자 하였다. 흡수처리후 생물반응기로 이송된 흡수액은 재생 후 다시 흡수탑으로 재 순환하였다. 실험에 사용된 대상가스는 농도가 400 mg/$\textrm{m}^3$ 인 톨루엔으로, 세정액이 가스흐름과 향류로 약 10~15L/min의 유량으로 충전층을 적시며 내려오는 충전탑내부로 약 100 L/min의 유량으로 도입하였다. VOC처리를 위해 제작된 본 바이오스크러버에서 고비점용매를 이용한 연속실험결과 최적운전 조건에서 약 80%의 처리율을 얻을 수 있었다.

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탑형 발효기에 의한 에탄올 연속 생산 (Continuous Ethanol Production by Tower Fermentor)

  • 서근학;송승구김재형
    • KSBB Journal
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    • 제9권2호
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    • pp.104-107
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    • 1994
  • Cone 형태 탑형발효기에서 연속발효실험을 수행 결과 발효조 최대 효모 농도는 37.5-39.5g/l이었고 최대 에탄올 생산성은 희석율 0.32 $hr^{-1}$에서 16.3gEtOH/L.hr 이었다. 평균 에탄올 수율은 0.48 g/EtOH/g glucose로서 이는 이론적 수율의 94%였다. Cone형태 탑형발효기는 에탄올 연속생신시 효과적인 발효기로 생각되었다.

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지하수중의 질산성질소 제거를 위한 영가철 충진 복극전해조의 현장적용에 관한 연구 (Removal of Nitrate in Groundwater by Bipolar ZVI Packed Bed Electrolytic Cell at Field Pilot)

  • 나소정;정주영;김한기;박주양
    • 상하수도학회지
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    • 제25권6호
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    • pp.989-994
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    • 2011
  • Nitrate contamination of groundwater is a common problem throughout intensive agriculture areas (non-point source pollution). Current processes (e.g. ion exchange and membrane separation) for nitrate removal have various disadvantages. The objective of this study was to evaluate electrochemical method such as electroreduction using bipolar ZVI packed bed electrolytic cell to remove nitrate from groundwater at field pilot. In addition ammonia stripping tower continuously removed up to 77.0% of ammonia. Bipolar ZVI packed bed electrolytic cell also removed E.coli. In the field pilot experiment for groundwater in 'I' city (average nitrate 30~35 mg N/L, pH 6.4), maximum 99.9% removal of nitrate was achieved in the applied 600 V.

영가철 충진 복극전해조를 이용한 질산성질소 및 대장균의 연속식 제거 (Continuous Removal of Nitrate and Coliform using Bipolar ZVI Packed Bed Electrolytic Cell)

  • 정주영;박정호;최원호;박주양
    • 상하수도학회지
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    • 제25권5호
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    • pp.651-658
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    • 2011
  • Nitrate is a common contaminant in industrial wastewater and ground water. The maximum contaminant level set by EPA for nitrate of 10 mg/L as N. In this study, nitrate was removed using bipolar ZVI packed bed electrolytic cell that maximized the contact area between each electrode and contaminants under 600 V. Also this study investigates the simultaneously deals with removal of ammonia by operating air stripping tower. In addition to the air stripping also helped to precipitate iron ions to the form of iron oxides. Bipolar ZVI packed bed electrolytic cell was also effective in removing coliform by electrical power. In the continuous experiments for the simulated wastewater (initial nitrate for 25 mg/L as N), maximum 96.3% removal of nitrate was achieved in the applied 600 V at the flow rate of 6 mL/min.

역류식 충전탑에서 이산화탄소 탈착과 수력학절 거동에 관한 연구 (A Study on Hydraulic Behavior and Desorption of $CO_2$ Gas in the Counter-current Packing Tower)

  • 김석택
    • 환경위생공학
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    • 제15권3호
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    • pp.94-100
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    • 2000
  • This study was carried out to interpret hydraulic behavior and CO2 gas desorption in counter-current packing tower which packed 50mm plastic Hiflow-ring. The results are as follow : To compare with conventional packing, 50mm Hiflow-ring could save energy because of low pressure drop under high load. As relative error between calculated value and investigated value was less than 6% in the loading point and flooding point we found that we are predict results mathematically which occur in packing tower. The unique magnitude of packing which was used are as follows. $C_L=2.1{\times}10^{-4}$, n=0.787 so we can predict efficiency which occur

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