• 한국환경과학회지
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• 제25권1호
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• pp.23-29
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• 2016

This study has conducted greenhouse gas emission reduction test as using Oyster-shells originated PCC paper filler compare to non-Oyster shells used PCC. This examination was estimated and calculated in accordance with both IPCC (Intergovernmental Panel on Climate Change) and World Business Council for Sustainable Development (WBSCD). The greenhouse gas emission reduction estimation result indicates that, when oyster shells are recycled and used as paper filler, it reduces $27.97tCO_2\;per\;100\;ton$ of oyster shells. It is greenhouse gas emission $44.27tCO_2$ from PCC production changed to carbon emission reduction when replaced with oyster shell. LNG greenhouse gas emission $16.3tCO_2$ in relation to the pre-treatment with oyster shell per 100 ton is also reflected. As a result, it is assumed that roughly $0.2797tCO_2/oyster\;shell{\cdot}ton$.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2008년도 추계학술대회B
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• pp.2940-2945
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• 2008

The scale of 2.4 MW MCFC was taken to construct a high-efficiency and economical power generation system without CO2 emission into the atmosphere for utilizing its exhaust gas. The conventional steam turbine power generation system (STGS) was evaluated and the net generated power (NGP) was estimated to be only 133 kW and the STGS is not economically feasible. A CO2-caputuring repowering system was proposed, where low temperature steam (LTS) produced at HRSG by using exhaust gas from MCFC is utilized as a main working fluid of a gas turbine, and the temperature of LTS was raised by combusting fuel in a combustor by using pure oxygen, not the air. It has been shown that NGP of the proposed system is 264 kW, and CO2 reduction amount is 608 t-CO2/y, compared to 306 t-CO2/y of STGS. The CO2 reduction cost was estimated to be negligible small, even when the costs of oxygen production and CO2 liquefaction facilities etc. were taken into account.

• 한국안전학회지
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• 제11권3호
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• pp.112-118
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• 1996

When fossil fuels are burned they produce CO gas because of incomplete combustion. If the CO gas reacts with the hemoglobin in the red blood cells, it may result in death or sequelae. Generally, the CO gas is eliminated in the form of the $$$CO_2$ gas by the oxidation reaction over the platinum catalyst. In this study, the electrochemical CO removal was investgated by using the solid electrolyte cell reactor, the type of which was represented as reactants$/Pt/Y_2O_3-ZrO_2/Pt/Air$. If the overpotential was applied to the platinum working electrode, the conversion could be changed with the overpotential applied. It was found that the oxidation rate could be increased 2.8 times higher than that of the normal condition, i. e. under open circuit conditions when $P_{co}/P_{O_2}$ was 0.5 and overpotential was 0.9V. From these results, it is concluded that the reactor used in this study is more efficient than conventional catalytic reactors.

• 센서학회지
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• 제18권1호
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• pp.54-62
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• 2009

${Co_3}{O_4}$ and ${Co_3}{O_4}$-based thick films with additives such as ${Co_3}{O_4}-{Fe_2}{O_3}$(5 wt.%), ${Co_3}{O_4}-{SnO_2}$ (5 wt.%), ${Co_3}{O_4}-{WO_3}$(5 wt.%) and ${Co_3}{O_4}$-ZnO(5 wt.%) were fabricated by screen printing method on alumina substrates. Their structural properties were examined by XRD and SEM. The sensitivities to iso-${C_4}H_{10}$, $CH_4$, CO, $NH_3$ and NO gases were investigated with the thick films heat treated at $400^{\circ}C$, $500^{\circ}C$ and $600^{\circ}C$. From the gas sensing properties of the films, the films showed p-type semiconductor behaviors. ${Co_3}{O_4}-{SnO_2}$(5 wt.%) thick film heat treated at $600^{\circ}C$ showed higher sensitivity to i-${C_4}H_{10}$ and CO gases than other thick-films. ${Co_3}{O_4}-{SnO_2}$(5 wt.%) thick film heat treated at $600^{\circ}C$ showed the sensitivity of 170 % to 3000 ppm iso-${C_4}H_{10}$ gas and 100 % to 100 ppm CO gas at the working temperature of $250^{\circ}C$. The response time to i-${C_4}H_{10}$ and CO gases showed rise time of about 10 seconds and fall time of about $3{\sim}4$ minutes. The selectivity to i-${C_4}H_{10}$ and CO gases was enhanced in the ${Co_3}{O_4}-{SnO_2}$(5 wt.%) thick film.

• 한국가스학회지
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• 제18권5호
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• pp.26-32
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• 2014

CCS(Carbon Capture and Storage)는 제철, 철강, 발전소 등에서 발생되는 $CO_2$를 포집 및 저장하는 기술로서, 지구 온난화의 주범인 $CO_2$를 감축시키는 효과적인 기술이다. CCS 포집 기술과 저장 기술은 집중적인 개발을 도모하고 있으며, 현재 실증단계에 있다. 그러나 상용화 단계에 이르기 위해서는 포집, 저장 기술을 비롯하여 수송기술까지도 구성 요소에 대한 안전성 확보가 필요하다. 특히, 수송기술은 CCS 특성상 파이프라인을 이용한 수송기술이 적합하지만, $CO_2$ 파이프라인 운용 사례가 부족하여, 파이프라인 또는 구성 요소(밸브 등)에 대한 적합한 재질을 선택해야 한다. 본 연구에서는 $CO_2$ 파이프라인에 사용 가능한 고무재질을 알아보고자 여러 분야에서 사용되는 고무 재질을 $CO_2$에 침지하여 압력 온도 변화에 따른 부피변화를 비교 분석 하였다.

• 대한금속재료학회지
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• 제47권2호
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• pp.107-113
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• 2009

Molten iron with 2 mass % carbon content was decarbonized at 1823 K~1923 K by bubbling $Ar+O_2$ gas through a submerged nozzle. The reaction rate was significantly influenced by the oxygen partial pressure and the gas flow rate. Little evolution of CO gas was observed in the initial 5 seconds of the oxidation; however, this was followed by a period of high evolution rate of CO gas. The partial pressure of CO gas decreased with further progress of the decarbonization. The overall reaction is decomposed to two elementary reactions: the decarbonization and the dissolution rate of oxygen. The assumptions were made that these reactions are at equilibrium and that the reaction rates are controlled by mass transfer rates within and around the gas bubble. The time variations of carbon and oxygen contents in the melt and the CO partial pressure in the off-gas under various bubbling conditions were well explained by the mathematical model. Based on the present model, it was explained that the decarbonization rate of molten iron was controlled by gas-phase mass transfer at the first stage of reaction, but the rate controlling step was transferred to liquid-phase mass transfer from one third of reaction time.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2009년도 하계학술발표대회 논문집
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• pp.821-826
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• 2009

Due to environmental concerns $CO_2$ has been reintroduced as a potential candidate to replace HFCs in refrigeration systems. Oils are always required in a vapor-compression cycle, and thus actual working fluid in the system is $CO_2$-oil mixtures even though the oil concentrations are low at the heat exchangers and the expansion device. The cooling heat transfer coefficients for $CO_2$-oil mixtures under supercritical condition are required to designing of the gas cooler in the $CO_2$ refrigeration system properly. In the present study, the gas cooling heat transfer coefficients for $CO_2$-PEC9 was estimated by using the Gnileinski correlation, and the Kim and Ghajar model through the previous prediction models for the thermo-physical properties of $CO_2$-oil mixture. The Gnileinski correlation was used when the oil wt.% in the mixture is less than 1.0, and for the higher oil concentration the Kim and Ghajar model was applied. The estimated results agree with the experimental results conducted by the Dang et al.

• 한국세라믹학회지
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• 제40권12호
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• pp.1177-1182
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• 2003

BaTiO$_3$ 분말에 흑연 분말을 첨가하여 BaTiO$_3$계 가스센서용 다공성 감지물을 제조하였으며, 이 감지물의 결정구조와 미세구조를 연구하였다. 이 감지물 소성체는 정방정 perovskite 결정구조를 가지고 있었다 흑연 분말의 첨가량이 증가함에 따라 소성체의 기공도가 증가하였다. 이것은 소성 시 흑연 분말과 산소가 발열반응하여 CO 및 $CO_2$ 가스를 생성하고, 이 가스가 휘발하였기 때문이라고 생각된다. 제조한 BaTiO$_3$계 소성체는 대기에서 측정한 저항과 CO 가스에서 측정한 저항이 고온( >∼20$0^{\circ}C$)에서 큰 차이를 나타내고 있으며 온도가 증가함에 따라 차이가 커짐을 관찰하였다. 소성체 기공도의 증가에 따른 반응 site의 증가로 인하여 소성체의 표면흡착기인 $O_2$$^{-}$와 CO 가스의 반응과, 소성체에 있는 $O^{-}$와 CO 가스의 반응이 활발하기 때문에 CO 가스의 민감도가 크게 증가하였다. 본 연구에서 제조된 다공성 BaTiO$_3$계 세라믹스는 CO 가스센서의 감지물 재료로써 유망하다고 생각된다.

• Korean Chemical Engineering Research
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• 제50권3호
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• pp.516-521
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• 2012

본 연구는 연소기체로부터 $CO_2$ 기체를 포집하는 기포 유동층 흡착 및 재생 반응기 공정의 주요 운전변수의 영향을 조사하기 위해서 단순화된 공정모델을 개발하였다. 반응속도와 반응기에서 고체입자의 평균체류시간을 이용하여 흡착탑과 재생탑에서 각 반응 전환율을 계산하였다. 실험실 규모 기포 유동층 공정에 적용하여 $CO_2$ 포집효율에 대한 온도, 기체유속, 고체순환속도, 연소기체 중 수분농도의 영향을 조사하였다. $CO_2$ 포집효율은 흡착탑의 온도 혹은 유속이 증가함에 따라서 감소하였다. 그러나 연소기체의 수분농도 혹은 재생탑의 온도가 증가함에 따라서 증가하였다. 계산된 $CO_2$ 포집효율은 측정값과 잘 일치하였다. 그러나 본 모델은 $CO_2$ 포집효율에 대한 고체순환속도의 영향과 잘 일치하지 않았다. 이의 해석을 위해서는 기체-고체 접촉효율에 대한 이해가 더 필요하였다.

• 한국토양환경학회지
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• 제2권1호
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• pp.63-72
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• 1997

본 연구는 여러 종류의 매립지에서 발생가스를 측정하여, 다음과 같은 결론을 얻었다. (1) $CH_4$가스는 대부분 수직가스포집관에서 유출되며, $CO_2$가스는 총유출량의 약 50% 정도가 수직가스포집관을 통하여 유출된다. (2) 매립지 표면에서는 $CH_4$가스 보다 $CO_2$가스가 많이 유출된다. (3) 사면 복토층은 면적비율이 작으나 가스 발생량이 많으며, 특히 $CO_2$가스의 발생율이 높다. (4) 새로 반입된 쓰레기층 표면에서의 $CH_4$가스 발생량은 미소이므로 무시하여도 되나, $CO_2$ 가스 유출량이 많다. (5) 쓰레기층 노출, 복토층 다짐정도등에 따라 가스 발생량의 변화를 보인다. (6) 가스포집관과 복토 표면에서의 가스 유출량은 $CH_4$가스 유출이 많으나, 매립지 전체에서는 $CO_2$가스 유출량이 많다.