• Title/Summary/Keyword: 소화가스

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LFG를 이용한 350kW급 가스엔진 발전시스템 개발

  • Lee, Jang-Hui;Kim, Yeong-Min;Choe, Yeong-Ha;Sin, Dong-Seong;Choe, Myeong-Hak;Min, Gyun-Hong;Choe, Byeong-Cheol;Lee, Chun-Hui;Sin, Dong-Ho;Choe, Byeong-Cheol
    • 한국신재생에너지학회:학술대회논문집
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    • 2005.11a
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    • pp.276-285
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    • 2005
  • 본 과제에서는 참여기업인 두산인프라코어(구 대우종합기계)에서 양산중인 국산디젤엔진을 개조해 가스엔진을 제작하였으며, 두산인프라코어에서 500시간 내구시험을 2차례 실시하였고, 주관기관인 한국기계연구원에서 국산 ECU를 활용하여 도시가스를 연료로 실험을 수행한 후 김포매립지에서 현장 적용실험을 수행하였다. 메탄농도가 46$\sim$56%로 변하는 조건에서 350kW의 출력을 달성하였으며, 삼원촉매를 적용한 결과 2005년 배기규제를 만족하는 결과를 도출하였다. 위탁기관인 전남대에서는 촉매 특성에 관한 실험을 1차년도와 2차년도에 수행하였다. 본 과제에서 개발한 LFG(=매립지가스) 엔진은 국내에서 개발된 최초의 LFG 엔진으로서 쓰레기 매립지 뿐만 아니라 음식물 쓰레기 혐기소화 처리과정, 분뇨나 축분 등의 혐기소화 처리과정, 하수종말 처리장 등에서 발생하는 바이오가스를 이용한 발전 동력원으로 사용될 수 있을 것으로 기대된다.

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An Experimental Study on the Damage of the Data Process Equipment When $CO_2$ is Discharged ($CO_2$ 소화설비 방사시 정보저장장치의 저온손상에 관한 연구)

  • 이수경;김종훈;김영진;최종운
    • Fire Science and Engineering
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    • v.13 no.3
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    • pp.19-26
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    • 1999
  • $CO_2$ extinguishing system is the most $\phi$pular among the gas extinguishing system. $CO_2$ is usually stored with liquified state. But, it gasifies at the tip of nozzle when $CO_2$ was released through the pipe and head. A ro$\alpha$n temperature is very low when $CO_2$ was released. So electrical instrument, magnetic storage equipment and memory semiconductor are electrically or physically injured by cooling effect in a few minutes. So, we intend to find out temperature profile and electrical damage in compartment area, and supply basic d data for research and making standards and code through the full scale experiment. As result of experiment on the damage due to cooling effect from $CO_2$ extinguishing system, i instantaneous discharging temperature. was $-82.5^{\circ}C$ in average. An average temp. in the compartment after discharging $CO_2$ was $-40^{\circ}C$.

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Discharge and Fire Extinguishing Test of Inert Gas Clean Agent (불활성 가스계 청정 소화약제의 방출 및 소화)

  • Song Eun-Seok;Kim Jae-Duck;Park Yang-Won
    • Fire Science and Engineering
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    • v.19 no.2 s.58
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    • pp.29-36
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    • 2005
  • We carried out discharge and fire extinguishing tests of new inert gas clean agent, which consists of $92\%$ nitrogen and $8\%$ carbon dioxide, as an alternative of Halon that is banned by Montreal Protocol to protect the ozone layer of the earth. Discharge and fire extinguishing tests were performed in $27m^3$ and $190m^3$ rooms with piping which allows gaseous agent to transport from storage to test rooms. We confirmed that it took less than regulation time, 60 seconds for the discharge of over $95\%$ initial charged amounts. Discharge test variables were piping length and orifice size. Fire extinguishing tests verified that this new inert gas clean agent is suitable for both n-Heptane fire and deep seated fire of wood crib.

A Study on the Precautions Effects of the Enclosure Integrity Test for the Gaseous Extinguishing Systems: Focusing on the Power Plant (가스계 소화설비의 밀폐도 시험에 영향을 미치는 사전조치에 관한 연구: 발전소를 중심으로)

  • Kim, Young-Chul;Jo, Il-Hyun;Lee, Su-Kyung
    • Fire Science and Engineering
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    • v.29 no.1
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    • pp.60-66
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    • 2015
  • The present study was aimed to analyze enclosure integrity test, which is the performance experiment of soaking time, in a fire zone equipped with gaseous extinguishing system in an effort to find understand the effect of precaution factors upon the success of fire extinguishment. To achieve the goal of this study, it divided the fire zones of internal and external power plants into ones taking precaution measures and not taking them and then enclosure integrity test was given respectively. Therefore, this study examined the success rate if the test according to the presence and absence of the precaution measure and confirmed the failure factors, designed concentration soaking time and proportion of leakage area to total volume area by type of gaseous extinguishing system and rooms. Precaution measures were applied to the fire zones without them to confirm the increase of the success rate of enclosure integrity test. By doing so, it was found that reduced number of experiments caused by failure led to cost saving.

Effects of Aeration on Bio-hydrogen (Bio-H2) Production in the Anaerobic Digestion (혐기성 소화시 aeration이 수소생성에 미치는 영향)

  • Lee, Myoung Joo;Jang, Hyun Sup;Hwang, Sun Jin;Jeong, Yeon Koo
    • KSCE Journal of Civil and Environmental Engineering Research
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    • v.26 no.6B
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    • pp.683-687
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    • 2006
  • This research investigated the effect of aeration pretreatment for anaerobic seed sludge on hydrogen production. Aeration time for anaerobic sludge was maintained at 0, 1, 3, 6, 12, and 24 hours in batch tests. Two continuous anaerobic reactors (aerated and non-aerated) were also operated. All experiments were conducted at $35^{\circ}C$ using mineral salts-glucose (20 g/l) medium. Methane production decreased with the increase in aeration time. Aeration for 6 hours was determined as an optimum from the amount of hydrogen produced. Hydrogen was steadily produced in the continuous reactor seeded with aerated sludge while no methane production was observed. However, small amount of hydrogen was produced in the non-aerated reactor for short period of time from the start even though short HRT (2 days) and low pH (5.5) were maintained.

A Study on the Sludge Reduction and Biogas Production through a Two-phase Anaerobic Digestion Process (이상 혐기성 소화 공정을 통한 슬러지 발생량 저감과 바이오가스 생산에 관한 연구)

  • Woo, Mi-Hee;Han, Gee-Bong
    • Journal of Korean Society of Environmental Engineers
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    • v.32 no.9
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    • pp.894-899
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    • 2010
  • We coordinated the experiments with ozone pretreatment and two-phase anaerobic digestion using solid-liquid separation to raise the efficiency of sludge volume reduction and obtained the following results. The pre-treatment with ozone reduced the solid concentration in the average of TSS $8.3{\pm}2.0%$ TSS and $9.2{\pm}}2.8%$ VSS. Of the organic material, TCOD decreased $5.1{\pm}2.4%$, but SCOD showed $72{\pm}6.5%$ increased, which was due to destruction of the cell wall and dissolution of icell media by the powerful oxidative stress of ozone. During the two-phase anaerobic digestion process, we achieved the reduction of $21.5{\pm}3.4%$ TSS, $20.2{\pm}8.4%$ VSS, $32.1{\pm}7.9%$ TCOD and $22.1{\pm}7.2%$ SCOD in average. The maximum methane gas production were 177.6 mL per g TSS, 210.8 mL per g VSS, 127.0 mL per g TCOD and 1452.0 mL per g SCOD, respectively. Solid material reduction through the two-phase anaerobic digestion and MLE (Modified Ludzack-Ettinger) processes were 93.8% of TSS and 92.0% of VSS. We concluded that suggested two-phase anaerobic digestion and MLE process could achieve the reasonable production of biogas and a maximum reduction of the sludge volume.