• 제목/요약/키워드: Liquid Waste Treatment

검색결과 158건 처리시간 0.024초

확장표면을 적용한 액체식 제습기에서 제습액 분배 특성에 관한 실험적 연구 (Experimental Study on Liquid Desiccant Distribution Characteristics at a Dehumidifier with Extended Surface)

  • 이민수;장영수;이대영
    • 대한설비공학회:학술대회논문집
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    • 대한설비공학회 2009년도 하계학술발표대회 논문집
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    • pp.645-649
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    • 2009
  • Liquid desiccant cooling technology can supply cooling by using waste heat and solar heat which are hard to use effectively. For compact and efficient design of a dehumidifier, it is important to sustain sufficient heat and mass transfer surface area for water vapor diffusion from air to liquid desiccant on heat exchanger. In this study, the plate type heat exchanger is adopted which has extended surface, and hydrophilic coating and porous layer coating are adopted to enhance surface wettedness. PP(polypropylene) plate is coated by porous layer and PET(polyethylene terephthalate) non-woven fabric is coated by hydrophilic polymer. These coated surfaces have porous structure, so that falling liquid film spreads widely on the coated surface foaming thin liquid film by capillary force. The temperature of liquid desiccant increases during dehumidification process by latent heat absorption, which leads to loss of dehumidification capacity. Liquid desiccant is cooled by cooling water flowing in plate heat exchanger. On the plate side, the liquid desiccant can be cooled by internal cooling. However the liquid desiccant on extended surface should be moved and cooled at heat exchanger surface. Optimal mixing and distribution of liquid desiccant between extended surface and plate heat exchanger surface is essential design parameter. The experiment has been conducted to verify effective surface treatment and distribution characteristics by measuring wall side flow rate and visualization test. It is observed that hydrophilic and porous layer coating have excellent wettedness, and the distribution can be regulated by adopting holes on extended surface.

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RF-LPP법을 이용한 고순도 마이크로 Ag 입자 합성 (The synthesis of high purity micro Ag particle using the rapid firing -liquid phase precursor method)

  • 임병석;송영현;이민지;맹성렬;윤대호
    • 한국결정성장학회지
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    • 제25권3호
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    • pp.93-97
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    • 2015
  • 본 연구에서는 고순도 균질 마이크로 Ag 입자를 얻기 위하여 용매추출법과 RF-LPP법을 이용하여 Air 분위기에서 $500^{\circ}C$에서 3시간 동안 열처리하여 Ag 입자를 합성하였다. 합성된 마이크로 Ag 입자를 XRD에 의해 비교 분석한 결과 주요 peak들이 JCPDS card(No. 87-0719)와 일치하는 것을 확인하였다. RF-LPP법을 이용함으로써, 핵 생성 싸이트 제어를 통해 균질 마이크로 Ag 입자를 합성하였으며, 환원처리 후 산소의 함유가 줄어드는 것을 확인하였다. 본 연구를 통하여 재활용 기술에 큰 기여를 할 것이라 기대한다.

폐 LCD (Liquid Crystal Display) 해체 후 분리된 CCFL (Cold Cathode Fluorescence Light) 내 수은의 건식 제거 공정 (Decontamination of Mercury Contained in CCFLs (Cold Cathode Fluorescence Light) Disassembled from Waste LCDs (Liquid Crystal Display))

  • 박재량;이성규;강이승;이찬기;조성수;홍명환;홍현선
    • 자원리싸이클링
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    • 제23권2호
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    • pp.61-70
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    • 2014
  • LCD TV와 컴퓨터 모니터에는 스크린을 밝게 할 목적으로 냉음극관이 장치되어 있는데 이러한 냉음극관 대부분에는 수은이 봉입되어 있으므로 폐 LCD의 재활용 시 적절히 취급되어야 한다. 아울러 이러한 폐 LCD내의 냉음극관의 처리는 2002년에 채택된 EU의 WEEE 와 RoHS 지침에 따라 취급되고 제거되어야만 한다. 본 연구에서는 폐 LCD의 몰드 프레임에 장착된 CCFL을 안전하고 효율적으로 제거한 다음 여기 함유된 수은과 형광체 화합물을 환경친화적으로 분리하여 무해화 처리할 수 있는 건식 공정을 개발하였다. 이를 통해서 실용적이고 경제성 있는 폐디스플레이 자원 재활용 통합공정 개발에 기여할 목적으로 CCFL 무해화 시스템의 설계 및 제작, 이를 운용한 수은/형광체 화합물의 환경친화적 무해화 처리 효율을 평가해 보았다. CCFL 무해화 시스템을 이용하여 처리된 CCFL내 잔류 수은의 양을 정량적으로 평가해 본 결과 무해화율 99% 이상을 달성하였다.

트리튬 처리기술 현황 (A Status of Tritium Processing Technologies)

  • 안도희;김광락;백승우;이민수;임성팔;정흥석
    • 한국방사성폐기물학회:학술대회논문집
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    • 한국방사성폐기물학회 2003년도 가을 학술논문집
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    • pp.172-179
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    • 2003
  • 핵확산 저항성 핵연료주기공정, 트리튬을 활용하는 첨단산업 시설과 중수로형 원전 등의 국내 원자력 산업에서 다양한 화합물 형태로 발생하는 트리튬 폐기물을 처리하는 기술을 개발하기 위하여 국내외 트리튬 처리기술의 현황을 조사하였음. 트리튬 폐기물을 크게 기체상, 유기상, 수용액상으로 분류하였고, 이들을 각각 처리할 수 있는 기술을 분석하였음. 이러한 트리튬 폐기물의 처리기술 개발은 원자력 산업의 지속적인 발전을 위한 기술력 기반조성 및 국민의 방사성 폐기물에 대한 긍정적 이미지를 심어 주는데 필수적임.

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다성분 염화물계 진공 증류의 잔류 액체 거동 계산 (Residual Liquid Behavior Calculation for Vacuum Distillation of Multi-component Chloride System)

  • 박병흥
    • 방사성폐기물학회지
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    • 제12권3호
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    • pp.179-189
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    • 2014
  • 파이로 공정은 사용후핵연료 관리 이슈 해결과 유용자원 재활용 제고의 목적으로 개발되고 있다. 파이로 공정 중 전해환원 공정은 LiCl을 전해질로 사용하여 산화물을 금속으로 전환시키는 공정으로 금속 전환체에 잔류염이 포함되므로 후속 공정이 요구된다. 진공 증류 공정은 다양한 용융염계에서 적용되어 왔으며 금속 전환체에서도 활용될 수 있다. 전해환원 금속 전환체 잔류염은 LiCl과 알카리 및 알카리토 금속 염화물을 포함한다. 본 연구에서는 이들 염화물들의 증기압을 추산하여 진공 증류 공정에서 잔류 액체의 조성변화를 계산하였다. 증류된 기체가 일정하게 제거되는 조건에서 물질수지와 기-액 평형식을 결합한 모델을 개발하였으며 증기압을 이용하여 무차원 시간에 대한 액체 조성 변화를 계산하였다. 공정 조건 변화 모사를 위해 온도와 용융염 조성을 변화시켜 거동을 비교하였다. 잔류염의 증류는 주성분인 LiCl에 의해 지배되었으며 LiCl 보다 증기압이 높은 CsCl은 쉽게 제거될 것이 예상되었다. 증기압이 유사한 RbCl은 LiCl과 일정한 조성이 유지되었다. 반면 증기압이 낮은 $SrCl_2$$BaCl_2$는 시간에 따라 농축되며 초기 조성이 높은 경우 증류 과정에서 석출될 가능성이 있는 것으로 예상되었다.

수직관내 유리알-물 유동의 압력손실 및 열전달 성능 (Pressure Loss and Heat Transfer Characteristics of the Glass Beads-Water Flow in a Vertical Tube)

  • 김내현;김정식;이윤표
    • 설비공학논문집
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    • 제8권4호
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    • pp.550-560
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    • 1996
  • Recently, fluidized bed heat exchangers with circulating liquid are widely used in a number of places-chemical, process, food concentration, waste water treatment facilities, etc. In a circulating heat exchanger, solid particles circulate with the liquid, thereby increase the heat transfer and reduce the fouling potential of the heat exchanger. In this study, glass beads were circulated through a vertical tube. The pressure loss and the heat transfer coefficient were measured. At low flow velocities, glass beads enhanced the heat transfer considerably. The enhancement increased as the volume fraction of the glass beads increased. The pressure loss showed a similar trend. From the observed particle behavior near tube wall, a possible explanation of the trend is provided.

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LDPE 반회분식 촉매열분해에서 조업조건이 반응 특성에 미치는 영향 (Effects of Reaction Conditions on the Performance of Catalytic Pyrolysis of LDPE in a Semi-Batch Reactor)

  • 나정걸;임철현;최휘경;정수현
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2006년도 추계학술대회
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    • pp.79-82
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    • 2006
  • Fueled by ballooning oil prices, waste plastics are now regarded as being cheap and abundant renewable sources, removing their stigma of dirty wastes Catalytic pryolysis of plastics in liquid phase allows recovery of light fuel oil as well as green treatment of polymerics wastes, and therefore significant efforts have been devoted to this research field. In this study, catalytic Pyrolysis of LDPE was carl ied out in semi-batch reactor which equipped a unit of separation and recirculation. The effect of react ion conditions were examined by analyzing liquid oil yield and carbon number distribution of products

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Axial and Radial Gas Holdup in Bubble Column Reactor

  • Wagh, Sameer M.;Ansari, Mohashin E. Alam;Kene, Pragati T.
    • Bulletin of the Korean Chemical Society
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    • 제35권6호
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    • pp.1703-1705
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    • 2014
  • Bubble column reactors are considered the reactor of choice for numerous applications including oxidation, hydrogenation, waste water treatment, and Fischer-Tropsch (FT) synthesis. They are widely used in a variety of industrial applications for carrying out gas-liquid and gas-liquid-solid reactions. In this paper, the computational fluid dynamics (CFD) model is used for predicting the gas holdup and its distribution along radial and axial direction are presented. Gas holdup increases linearly with increase in gas velocity. Gas bubbles tends to concentrate more towards the center of the column and follows a wavy path.

수직관내 유리알-물 유동의 압력손실 및 열전달 성능 (Pressure Loss and Heat Transfer Characteristics of the Glass Bead - Water Flow in a Vertical Tube)

  • 김내현;김정식;이윤표
    • 한국에너지공학회:학술대회논문집
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    • 한국에너지공학회 1996년도 춘계학술발표회 초록집
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    • pp.121-131
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    • 1996
  • Recently, circulating liquid fluidized bed heat exchangers are widely used in a number of places - chemical, process, food concentration, waste water treatment facilities, etc. In a circulating heat exchanger, solid particles circulate with the liquid, thereby increase the heat transfer and reduce the fouling potential of the heat exchanger. In this study, glass beads were circulated through a vertical tube. The pressure loss and the heat transfer coefficient were measured. At low flow velocities, glass beads enhanced the heat transfer considerably. The enhancement increased as the volume fraction of the glass beads increased. It also increased as the particle diameter increased. The pressure loss showed a similar trend. From the observed particle behavior near tube wall, a possible explanation of the trend is provided.

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열적방법을 활용한 유기염소계 폐농약의 분해 특성 평가 (Evaluation of Decomposition Characteristics of Organochlorine Pesticides Using Thermal Method)

  • 권은혜;윤영삼;배지수;전태완;이영기
    • 한국폐기물자원순환학회지
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    • 제35권8호
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    • pp.744-753
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    • 2018
  • The Stockholm Convention, which was adopted in Sweden in 2001 to protect human health and the environment, includes regulations for Persistent Organic Pollutant Rotors such as toxic and bioaccumulatives. Currently, there are 28 types of materials. This prohibits and limits the production, use, and manufacture of products. Korea is a member of the Convention, and it is necessary to prepare management and treatment plans to address the POP trends. Thus, we experimentally investigate whether the environmentally stable incineration is achieved when the sample is thermally treated using the Lab-scale (1 kg/hr). The target samples is pesticides in liquid phase and solid phase. In this study, organic chlorinated pesticides and their thermal characteristics were analyzed. We calculated the theoretical air volume based on the element analysis results. Because the interior of the reactor is small, more than 10 times of the air ratio was injected. The retention time was set to at least 4 seconds using a margin. The incineration temperature was $850^{\circ}C$ and $1100^{\circ}C$. Thus, we experimentally investigated whether the environmentally stable incineration was achieved when the sample was thermally treated using the Lab-scale (1 kg/hr). We analyzed five types of exhaust gas; the 02 concentration was high, but the CO amount decreased. Complete combustion is difficult because of the small size of the furnace due to the nature of Lab-scale. The organic chlorine-containing pesticide had an average decomposition rate of 99.9935%. Considering the decomposition rates of organic chlorine-containing pesticide in this study, the incineration treatment at over 2 ton/hour, which is typical for a conventional incinerator, is possible. Considering the occurrence of dioxins and unintentional persistent organic pollutants, it can operate at more than $1,100^{\circ}C$.