• Title/Summary/Keyword: 이산화탄소 전환

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산업용 보일러 연료전환에 따른 효율 향상 적용사례

  • 유현석;이현찬;이중성
    • Environmental engineer
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    • s.175
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    • pp.70-75
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    • 2001
  • 산업용 보일러에 대해 오일버노에서 가스버너로 설비교체를 하면서 폐열회수, 저공기비 운전 등을 통해 열효율이 6$\~$8$\%$ 정도 향상되었으며 fuel NO의 제거로 질소산화물질은 1/3정도 배출되었다. 지구온난화 물질인 이산화탄소의 배출도 에너지 절감을 통해 6$\~$8$\%$ 정도 절감되었다. 이러한 결과는 국내 산업용 보일러의 효율향상 및 성능개선에 대한 분석적인 적용

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Patent Trend Analysis of Carbon Capture/Storage/Utilization Technology (이산화탄소 포집/저장/활용 기술 특허 동향 분석)

  • Bae, Junhee;Seo, Hangyeol;Ahn, Eunyoung;Lee, Jaewook
    • Economic and Environmental Geology
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    • v.50 no.5
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    • pp.389-400
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    • 2017
  • In December 2015, 195 nations agreed to cut green house gas emissions in the Paris Climate Convention, and all over the world showed their willingness to participate in greenhouse gas mitigation. Accordingly, various technologies related to greenhouse gas reduction are being considered, among which carbon dioxide capture, storage, utilization (CCUS) technologies are attracting attention as an unique technology capable of directly removing greenhouse gases. However, CCUS technologies are still costly and have low efficiency. It is still more important to analyze the level of CCUS technology before commercialization and to understand trends and to predict future direction of technology. Therefore, this study analyzes the patent trends of CCUS technology and derives implications for future directions. As a result of country analysis, the United States had the highest number of applications, and sectoral analysis shows that 64% of total patents are from capture sector. Companies such as Alstom technology, Toshiba Corp, and Mitsubishi Heavy are focusing on capturing carbon dioxide. In Korea, government research institutes have focused on storage and utilization technologies. In addition, since the late 2000s, patent applications have increased rapidly, and many countries have been interested in the development of the technology and have made efforts to reduce greenhouse gas.

Characterization of CO2 Biomineralization Microorganisms and Its Mineralization Capability in Solidified Sludge Cover Soil in Landfill (매립지 복토용 슬러지 고화물내 이산화탄소 생광물화 고정균 분석 및 생광물화능 평가)

  • Ahn, Chang-Min;Bae, Young-Shin;Ham, Jong-Heon;Chun, Seung-Kyu;Kim, Chang-Gyun
    • Journal of Korean Society of Environmental Engineers
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    • v.35 no.8
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    • pp.598-606
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    • 2013
  • This study was performed to determine whether biomineralization microbes were actively present underneath landfill cover soil producing biocalcification. From this, various types of microbes were observed. Among them, two species were dominantly found; Bacillus megaterium and Alkaliphilus metalliredigens that were known as biominerlization bacteria. With those microbes, $CO_2$ was more highly consumed than without bacteria. In response, the calcium carbonate mineral was produced at 30% (wt) greater than that of the control. At the same time, TG-DTA was successfully used for quantification of $CO_2$ consumed forming calcium carbonate minerals resulting from biocalcification. It was decided that the presence of solidified sewage sludge cake utilized as a cover soil in the landfill could efficiently contribute to possible media adaptably and naturally sequestering $CO_2$ producing from the landfill.

Enzymatic Biodiesel Synthesis from Canola Oil in Liquid Carbon Dioxide (액체 이산화탄소 조건에서의 캐놀라 오일 유래의 효소적 바이오디젤 생산)

  • Lee, Myung-Gu;Park, Chul-Hwan;Cho, Jae-Hoon;Lee, Jun-Hak;Lee, Do-Hoon;Kim, Sang-Yong
    • KSBB Journal
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    • v.25 no.4
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    • pp.337-343
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    • 2010
  • It has been well known that organic solvents like t-butanol and n-hexane can protect lipases from the inhibition by short-chain alcohols in the enzymatic transesterification. However, use of the organic solvents should be minimized considering their negative effects on environment and human health. Therefore, use of the greener solvents has been pursued in various are as including the enzymatic biotranformation. In this study, the liquid carbon dioxide ($LCO_2$) was employed as an alternative media for the enzymatic transesterification of canola oil. The conversion in the $LCO_2$ was comparable with those in organic solvents and the supercritical carbon dioxide, and under optimum conditions, the value reached 99.7%. It is expected that this method can provide a new type of biodiesel production process with higher energy efficiency and lower environmental impact.

A Study on reforming product characteristics by gas phase secondary pyrolysis (기상2차 열분해에 의한 개질 생성물 특성에 관한 연구)

  • Son, Young-Il;Yoon, Sang-Jun;Choi, Young-Chan;Ra, Ho-Won;Lee, Jae-Goo
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.05a
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    • pp.243-246
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    • 2008
  • 목질계 바이오매스 가스화 발전에 있어서는 가스화 가스중에 함유되어있는 타르를 가능한 한 가연성 가스로 전환하여 냉가스효율을 향상시키는 것 및 잔유하는 타르는 후단기기에 악영향을 초래할 우려가 있기 때문에 타르를 저감 제거하는 것이 바람직하다. 본 연구에서는 공기 수증기를 사용하여 타르개질 프로세스의 개선을 위해서 타르에서 가스성분으로의 전환에 관한 개질 실험을 실시하여 Wood chip 타르의 열분해 개질 생성물 거동에 대하여 검토하였다. Wood chip 열분해로 생성된 타르의 원소분석 및 $^1H$ NMR분석의 결과로 타르를 치환기를 가지지 않는 방향족, alkyl-기를 가지는 방향족, 산소 함유 방향족, 지방족의 4개로 분류하였다. 개질제에 의해 경질 타르, 중질 타르 모두 감소하였다. 개질 공기는 타르를 연소시키지만 그 속도는 가연성 가스와 경합하고 $900^{\circ}C$에서는 타르의 연소는 나타나지 않았다. alkyl-기를 가지는 방향족은 메탄과 치환기를 가지지 않는 방향족으로 전환되고, 치환기를 가지지 않는 방향족은 수소와 soot로 전환되고, 산소 함유 방향족은 일산화탄소와 치환기를 가지지 않는 방향족으로 전환되는 것을 알았다. 또한, 개질제에 의해alkyl-기를 가지는 방향족, 치환기를 가지지 않는 방향족, 산소 함유방향족 모두가 일산화탄소,이산화탄소로 전환되는 것을 알았다.

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Water Gas Shift reaction research of the synthesis gas for a hydrogen yield increase (수소 수율 증가를 위한 합성가스의 수성가스전환 반응 연구)

  • Kim, Min-Kyung;Kim, Jae-Ho;Kim, Woo-Hyun;Lee, See-Hoon
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.06a
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    • pp.840-843
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    • 2009
  • 폐자동차의 최종처분 과정에서 발생하는 자동차 파쇄 폐기물(Automobile Shredder Dust)은 대부분이 고분자 화합물로 높은 발열량을 가지고 있다. 또한 할로겐족 원소가 포함된 난연성 고분자류가 많아 다이옥신의 생성 우려가 높은 고분자류와 다이옥신 생성의 촉매 역할을 할 수 있는 금속성분이 많이 함유되어 있어 가스화용융시스템에 적용하여 처리하기에 매우 적합한 폐기물이다. 본 연구에서는 ASR의 가스화 용융 시설에서 고농도 CO를 함유한 합성가스를 수성가스전환반응(Water Gas Shift reaction, WGS)을 이용하여 수소의 수율을 높이는 기술을 제시하였다. 가스화 용융 설비에서 배출되는 합성가스 조성을 기준으로 적합한 고정층 WGS 반응기를 설계하고, 고온 촉매(KATALCO 71-5M)와 저온 촉매(KATALCO 83-3X)를 사용하여 실험하였다. 수성가스 반응 후의 가스 조성은 온도가 상승할수록 일산화탄소가 줄어들고 이에 따라 수소와 이산화탄소 발생량이 증가 되어 고온 촉매를 사용했을 경우 일산화탄소 전환율 ($1-CO_{out}/CO_{in}$)은 55.6에서 95.8%까지 상승하였다. 동일한 온도조건에서는 촉매에 관계없이 $CO/H_2$가 감소할수록 전환율도 감소하는 경향을 보였지만 동일한 합성가스 조성에서 일산화탄소 전환율을 비교하면 저온 촉매가 고온 촉매보다 매우 우수함을 알 수 있었다.

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Facile Separation of Zinc Oxalate to Oxalate and its Conversion to Glycolic Acid via Electrochemical Reduction (ZnC2O4의 Oxalate로의 효과적 분리 및 이의 전기화학적 환원을 통한 글리콜산으로의 전환)

  • Sunmi Im;Yiseul Park
    • Clean Technology
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    • v.29 no.1
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    • pp.46-52
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    • 2023
  • Oxalic acid has been traditionally obtained via the oxidation of carbohydrates using nitric acid and catalysts. However, this process produces a variety of nitrogen oxides during oxidation and requires a separation process due to its various intermediates. These products and additional steps increase the harmfulness and complexity of the process. Recently, the electrochemical reduction of carbon dioxide into oxalic acid has been suggested as an environmentally friendly and efficient technology for the production of oxalic acid. In this electrochemical conversion system, zinc oxalate (ZnC2O4) is obtained by the reaction of Zn2+ ions produced by Zn oxidation and oxalate ions produced by CO2 reduction. ZnC2O4 can then be converted to form oxalic acid, but this requires the use of a strong acid and heat. In this study, a system was proposed that can easily convert ZnC2O4 to oxalic acid without the use of a strong acid while also allowing for easy separation. In addition, this proposed system can also further convert the products into glycolic acid which is a high-value-added chemical. ZnC2O4 was effectively separated into Zn(OH)2 powder and oxalate solution through a chemical treatment and a vacuum filtration process. Then the Zn(OH)2 and oxalate were electrochemically converted to zinc and glycolic acid, respectively.

CO2 decomposition characteristics of Ni-ferrite powder (Ni-페라이트 분말을 이용한 CO2 분해 특성)

  • Nam, Sung-Chan;Yoon, Yeo-Il
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.12 no.11
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    • pp.5376-5383
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    • 2011
  • The objective of this study is the development of carbon-recycle technology, that converts carbon dioxide captured from flue gas to carbon monoxide or carbon for reuse in industrial fields. It is difficult to decompose $CO_2$ because $CO_2$ is very stable molecule. And then metal oxide was used as an activation agent or catalyst for the decomposition of $CO_2$ at low temperature. Metal oxides, which converts $CO_2$ to CO or C, were prepared using Ni-ferrite by solid state method and hydrothermal synthesis in this study. TPR/TPO and TGA were used as an analysis method to analyze the decomposition characteristics of $CO_2$. As the results, the reduction area of $H_2$ was high value at 15 wt% of NiO and the decomposition area of $CO_2$ was superior capacity at 5 wt% of NiO. However, TGA data showed contrary results that reduction area of $H_2$ was 28.47wt% and oxidation area by $CO_2$ was 26.95wt% at 2.5 wt% of NiO, one of the Ni-ferrite powders synthesized using solid state method. $CO_2$ decomposition efficiency was 94.66% and it is excellent results in comparison with previous studies.

CO2 Decomposition Characteristics of Zn-ferrite Powder Prepared by Hydrothermal and Solid State Reaction (수열합성법과 고상법을 이용해 제조된 Zn-ferrite 분말의 이산화탄소 분해 특성)

  • Nam, Sung Chan;Park, Sung Youl;Yoon, Yeo Il;Jeong, Soon Kwan
    • Applied Chemistry for Engineering
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    • v.22 no.5
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    • pp.555-561
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    • 2011
  • The objective of this study is the development of carbon recycle technology which converts $CO_2$ captured from flue gas to CO or carbon and reuse in industrial fields. Since $CO_2$ is very stable and difficult to decompose, metal oxide was used as an activation agent for the decomposition of $CO_2$ at low temperature. Metal oxides which convert $CO_2$ to CO or carbon at $500^{\circ}C$ were prepared using Zn-ferrite by the solid state reaction and hydrothermal synthesis. The behaviors of $CO_2$ decomposition were studied using temperature programmed reduction/oxidation (TPR/TPO) and thermogravimetric analyzer (TGA). Zn-ferrite containing 5 wt% ZnO showed the largest reduction and oxidation. Reduction by $H_2$ was 26.53 wt%, oxidation by $CO_2$ was 25.73 wt% and 96.98% of adsorbed $CO_2$ was decomposed to $CO_2$ and carbon with excellent oxidation-reduction behaviors.

Promotion effect of Ru in Ni-based catalyst for combined $H_{2}O$ and $CO_{2}$ reforming of methane (메탄의 수증기/이산화탄소 복합 개질 반응용 니켈 촉매의 루테늄 증진 효과)

  • Jang, Won-Jin;Seo, Yu-Taek;Roh, Hyun-Seog;Koo, Kee-Young;Seo, Dong-Joo;Seo, Yong-Seog;Rhee, Young-Woo;Yoon, Wang-Lai
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.06a
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    • pp.53-56
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    • 2007
  • 미량의 Ru을 증진제로 첨가하여 니켈 촉매의 반응 활성을 증진시킴으로써, 저온 환원성과 장시간 반응에 대한 안정성을 확보하고자 하였다. Ni의 담지량은 12 wt%로 고정하였으며 이에 Ru을 각각 0.1, 0.3, 0.5 wt%로 변화시켜 2차 담지하였다. 메탄의 수증기/이산화탄소 복합 개질 반응에 있어 니켈 촉매에 Ru을 2차 담지 한 촉매는 800 $^{\circ}C$, GHSV(gas hourly space velocity) 265,000 $h^{-1}$ 하에서 100 %에 가까운 $CH_{4}$ 전환율을 보였으며, GHSV 1,060,000 $h^{-1}$ 일 때에도 10시간 동안 90 %의 $CH_{4}$ 전환율을 기록하였다. 또한 이 중 0.3 wt%의 Ru를 담지한 경우가 1,060,000 $h^{-1}$의 조건하에서도 95 %이상으로 가장 높은 $CH_{4}$ 전환율로 유지되었다. $H_{2}-TPR$ 분석 결과, Ni(12)/$MgAl_{2}O_{4}$ 와 비교해 볼 때 Ru(0.5)/Ni(12)/$MgAl_{2}O_{4}$와 Ru(0.3)/Ni(12)/$MgAl_{2}O_{4}$ 촉매의 경우 150 $^{\circ}C$에서 저온 환원이 가능한 $RuO_{2}$의 존재를 확인할 수 있었다.

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