• 제목/요약/키워드: Packed Bed

검색결과 357건 처리시간 0.022초

충전층을 이용한 암반공동 열에너지저장시스템의 열에너지 수지 분석 (Thermal Energy Balance Analysis of a Packed Bed for Rock Cavern Thermal Energy Storage)

  • 박정욱;류동우;박도현;최병희;신중호;선우춘
    • 터널과지하공간
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    • 제23권3호
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    • pp.241-259
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    • 2013
  • 충전층을 이용한 열에너지저장 시스템은 자갈이나 콘크리트와 같은 열저장매질과 공기나 오일과 같은 열전달유체를 이용하여 현열에너지를 저장하는 방식으로서, 저장매질의 경제성과 화학적 안정성, 시스템 구축의 용이성 등 많은 장점이 갖는다. 본 연구에서는 충전층을 이용한 열에너지저장 기술에 대하여 개략적으로 소개하고, 이러한 열에너지저장소의 에너지 수지와 성능 효율을 분석하기 위한 수치 모델을 제시하였다. 유한차분법을 이용하여 저장소 내 1차원 비정상 열전달 해석을 수행하였으며, 반복적인 주입과 토출에 따른 충전층의 온도분포와 외부로의 손실 에너지를 계산하였다. 해석모델은 AA-CAES(advanced adiabatic compressed air energy storage)와 연계된 고온의 열에너지저장시스템으로 저장소가 지하암반 내에 위치하는 경우와 지상에 위치하는 경우를 모사하고, 성능효율 및 열손실률을 비교 분석하였다.

상자포장 청과물의 송풍저항 특성 (Resistance to Air Flow through Packed Fruits and Vegetables in Vented Box)

  • 윤홍선;조영길;박경규
    • Journal of Biosystems Engineering
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    • 제20권4호
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    • pp.351-359
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    • 1995
  • In pressure cooling system, produce were packed in vented box and cooled rapidly by producing a difference in air pressure on opposite faces of stacks of vented box. So, energy requirements and performance of pressure cooling system depended upon the air flow rate and the static pressure drop through packed produce in vented box. The static pressure drop across packed produce in vented box normally depended upon air flow rate, vent area of box and conditions of produce bed (depth, porosity, stacking patterns, size and shape of products) in box. The objectives of this study were to investigate the effect of vent area and air flow rate on airflow resistance of empty box and packed produce in vented box, and to investigate the relationship between the air flow resistance of packed products in vented box and sum of air flow resistance of empty box only and products in bulk only. Mandarins and tomatoes were used in the experiment. The airflow rate were in the range of 0.02~1.0$m^3$/s.$m^2$, the opening ratio of vent hole were in the range of 2.5~20% of the side area. The results were summerized as follows. 1. The pressure drops across vented box increased in proportion to superficial air velocity and decreased in proportion to opening ratio of vent hole. A regression equation to calculate airflow resistance of vented box was derived as a function of superficial air velocity and opening ratio of vent hole. 2. The pressure drops across packed produce in vented box increased in proportion to superficial air velocity and decreased in proportion to opening ratio of vent hole. 3. Because of the air velocity increase in the vicinity of vent hole in box, the airflow resistances of packed products in vented box were always higher than sum of air flow resistance of empty box only and products in bulk only. 4. Based on the airflow resistance of empty box and products in bulk, a regression equation to calculate airflow resistance of packed products in vented box was derived.

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흡착탑에서 벤젠과 톨루엔의 파괴거동 (Breakthrough Behavior of Benzene and Toluene in Adsorption Bed)

  • 강성원;민병훈;서성섭
    • 한국응용과학기술학회지
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    • 제17권2호
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    • pp.83-88
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    • 2000
  • The VOCs(Volatile Organic Compounds) is one of the major cause for the atmosphere pollution. Breakthrough behavior of benzene and toluene in adsorption bed packed with activated carbon was experimentally studied. Composition and temperature of the gas flowing in the bed was measured and breakthrough curves for each component was obtained. Breakthrough time of benzene was earlier than that of toluene due to relatively weak adsorptivity. The relationship between breakthrough time and flow rate was obtained. The shape of temperature change with time was dependent on the position in the bed. Temperature changed faster and sharper in the inlet than in the outlet. It was noted that breakthrough behavior could be affected by the heat transfer properties.

Column Removal of Trichloroethylene and Dichloromethane using Low Cost Activated Carbon

  • Radhika, M.;Lee, Young-Seak;Palanivelu, K.
    • Carbon letters
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    • 제11권1호
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    • pp.13-21
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    • 2010
  • Coconut shell activated carbon (CSAC) was investigated for its ability in the removal of two neutral chlorinated organic compounds, namely trichloroethylene (TCE) and dichloromethane (DCM) from aqueous solution using a packed bed column. The efficiency of the prepared activated carbon was also compared with a commercial activated carbon (CAC). The important design parameters such as flow rate and bed height were studied. In all the cases the lowest flow rate (5 mL/min) and the highest bed height (25 cm) resulted in maximum uptake and per cent removal. The experimental data were analysed using bed depth service time model (BDST) and Thomas model. The regeneration experiments including about five adsorption-desorption cycles were conducted. The suitable elutant selected from batch regeneration experiments (25% isopropyl alcohol) was used to desorb the loaded activated carbon in each cycle.

Plasma/Adsorption 공정의 특성연구 (Plasma/Adsorption Process with Packed Bed Reactor)

  • 김관태;한소영;신완호;이재옥;송영훈
    • 한국대기환경학회:학술대회논문집
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    • 한국대기환경학회 1999년도 추계학술대회 논문집
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    • pp.471-472
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    • 1999
  • 각종 산업분야에서 발생되는 NO$_{x}$ 및 VOC$_{s}$ 는 발생원에 따라 농도, 조성 및 가스량, 온도등의 조건이 크게 달라, 이를 경제적이고 효율적으로 제어하기 위해서는 각각의 조건 및 처리목적에 따른 적절한 방지기술의 선정이 필요하다.(중략)

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활성탄을 충전한 고정층에서 페놀 흡착에 따른 파과곡선과 물질전달저항 해석 (Analysis of Breakthrough Curves and Mass Transfer Resistance for Phenol Adsorption in a Fixed-bed Process Packed with Activated Carbon)

  • 유해나;감상규;이민규
    • 한국환경과학회지
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    • 제23권1호
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    • pp.53-60
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    • 2014
  • Adsorption of phenol on activated carbon in a fixed bed was studied. The effects of fixed-bed length, superficial velocity (flow rate) and particle size of adsorbent on fixed-bed performance were investigated. Some characteristic parameters such as the breakthrough time ($t_{0.05}$), saturation time ($t_{0.95}$), length of mass transfer zone ($L_{MTZ}$), adsorptive capacity (W), and adsorption rate constant ($K_a$) were derived from the breakthrough curves. Adsorbent particle sizes significantly affected the shape of the breakthrough curve. Larger particle sizes resulted in an earlier breakthrough, a longer $L_{MTZ}$ and a lower adsorption rate. Superficial velocity was a critical factor for the external mass transfer during fixed-bed adsorption process. The external mass transfer resistance was dominant as increasing superficial velocity.

$BaTiO_3$-슬러지 Packed-bed형 반응기에서 $NO_x$제거에 미치는 슬러지의 영향 (Effect of Sludge Pellets on $NO_x$ REmoval in $BaTiO_3$-sludge Packed-bed Reactor)

  • 박재윤;송원섭;고희석;박상현
    • 한국전기전자재료학회논문지
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    • 제14권10호
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    • pp.861-867
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    • 2001
  • In this paper, in order to investigate the catalytic effect of the sludge exhausted from waterworks on NO$_{x}$ removal, we measure NO removal characteristics with and without sludge pellets in BaTiO$_3$-sludge packed-bed reactor of plate-plate geometry. NO initial concentration is 50 ppm balanced with air and a gas flow rate is 5ι/min. Gas temperature is changed from 25 to 10$0^{\circ}C$ to investigate the role of sludge pellet on removing active oxygen species and NO$_2$. BaTiO$_3$pellets is filled for coronal discharge at upstream of reactor and sludge pellets is filled for catalytic effect at downstream of reactor. The volume percent of sludge pellets to BaTiO$_3$pellets is changed from 0% to 100% and AC voltage is supplied to the reactor for discharging simulated gases. In the results, when sludge pellets is put at the downstream of plasma reactor, NO removal rate is slightly increased. However, NO$_2$and $O_3$ as by-products during NO removal is significantly decreased from 51ppm without sludge pellets to 5 ppm with sludge pellets and from 50 ppm without sludge pellets to 0.004ppm with sludge pellets, respectively. Therefore, NO$_{x}$(NO+NO$_2$) removal rate is increased up to 93%. It is thought that sludge pellet maybe react with active oxygen species and NO$_2$ generated by corona discharge in surface of BaTiO$_3$pellets, the then NO$_2$O$_3$as by-products are considerably decreased. When we increase gas temperature from room temperature to 10$0^{\circ}C$, NO removal rate is decreased, while NO$_2$ concentration is independent on gas temperature. These result suggest that the removal mechanism of active oxygen species and NO$_2$in sludge pellet is not absorption, but chemical reaction. Therefore we expect that sludge pellets exhausted for waterworks could be used as catalyst for NO$_{x}$ removal with high removal rate and low by-product.oduct.

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Effect of Various Factors on the Operational Stability of Immobilized Cells for Acrylamide Production in a Packed Bed Reactor

  • Lee, Cheo-Young;Choi, Sang-Kyo;Chang, Ho-Nam
    • Journal of Microbiology and Biotechnology
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    • 제3권1호
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    • pp.39-45
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    • 1993
  • The effect of concentrations of phosphate buffer and acrylonitrile, pH, and various salts on the operational stability of the immobilized cells of Brevibacterium CH2 in a packed bed reactor were investigated. The effects of salts and carriers on the swelling of the immobilized beads during hydrolysis in a columnreactor were also investigated. Immobilization of the cells in Ba-alginate was more desirable than those in polyacrylamide and Ca-alinate for the swelling of the immobilized beads and the desired quality of the acrylamide produced. High quality acrylamide was produced using the Ba-alginate beads in a recycle fed-batch reactor without using an isotonic substrate. The conversion yield was nearly 100%, including a trace amount of acrylic acid produced as a by-product.

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Production of Salicylic Acid from Naphthalene by Immobilized Pseudomonas sp. Strain NGK1

  • Shinde, Manohar;Kim, Chi-Kyung;Karegoudar, Timmanagouda-Baramanagouda
    • Journal of Microbiology and Biotechnology
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    • 제9권4호
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    • pp.482-487
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    • 1999
  • The Pseudomonas sp. strain NGK1 (NCIM 5120) was immobilized in calcium alginate, agar, and polyacrylamide gel matrices. The salicylic acid-producing capacity of freely suspended cells was compared with immobilized cells in batches with a shake culture and continuous culture system in a packed bed reactor. Freely suspended cells ($4\times10^{10}cfu/ml$) produced 12 mM of salicylic acid, whereas cells immobilized in calcium alginate ($1.8\times10^{11}$cfu/g beads), agar ($1.8\times10^{11}$cfu/g beads), and polyacrylamide ($1.6\times10^{11}$cfu/g beads) produced 15, 11, and 16mM of salicylic acid, respectively, from naphthalene at an initial concentration of 25 mM. The continuous production of salicylic acid from naphthalene was investigated in a continuous packed bed reactor with two different cell populations. The longevity of the salicylic acid-producing activity of the immobilized cells from naphthalene was also studied in semi continuous fermentations. The immobilized cells could be reused 18, 13, and more than 20 times without losing salicylic acid-producing activity in calcium alginate-,agar-, and polyacrylamide-entrapped cells, respectively. The study reveals a more efficient utilization of naphthalene and salicylic acid production by the immobilized Pseudomonas sp. strain NGK1 as compared to the free cells.

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대기오염 물질 저감을 위한 저온 플라즈마 반응공정의 특성 (Characteristics of Non-Thermal Plasma Process for Air Pollution Control)

  • 송영훈;신동남;신완호;김관태;최연석;최영석;이원남;김석준
    • 한국대기환경학회지
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    • 제16권3호
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    • pp.247-256
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    • 2000
  • Basic characteristics of non-thermal plasma process to remove C2H4 and NO have been experimentally investigated with a packed-bed type reactor and an ac power supply. The performance of the non-thermal plasma generated by ac power supply was compared with that of a wire-plate type reactor equipped with a pulsed power supply. The result shows that the non-thermal plasma can be effectively generated with an AC power supply that can be easily fabricated with conventional techniques. In order to understand the basic reaction mechanisms of the non-thermal plasma process, parametric tests for different carrier gases(air and nitrogen) and for different reaction pathways have been performed. The test results show that O3 generated by non-thermal plasma plays an dominant role to oxidize C2H4 and NO over N and O radicals when these pollutant gases are carried by dry air under room temperature condition. Experimental observations, however, indicate that N and O radicals can significantly affect on the removal process of the pollutant gases under certain conditions.

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