• 제목/요약/키워드: $CO_2$ reforming

검색결과 246건 처리시간 0.027초

수소생산기술현황 (Hydrogen Production Technology)

  • 주오심
    • Korean Chemical Engineering Research
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    • 제49권6호
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    • pp.688-696
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    • 2011
  • 수소는 에너지를 방출하는 과정에서 부산물로 물만 배출하기 때문에 지속가능한 청정에너지원 중의 하나이다. 현재 세계적으로 사용되는 수소는 대부분 화석연료의 개질에 의해 생산되고 있으며 1kg 수소를 생산하는 과정에서 7kg 이상의 이산화탄소를 배출하고 있다. 수소를 생산하는 과정에서 투입되는 에너지와 자원이 지속가능하고 재생 가능해야 수소를 청정에너지원이라 할 수 있다. 바이오매스는 화석연료를 대체할 수 있는 에너지원중의 하나인데, 그 이유는 바이오매스로부터 수소를 생산할 수 있으며 수소생산과정에서 발생하는 이산화탄소는 바이오매스 생산과정에서 소비되기 때문에 이론적으로 이산화탄소를 발생시키지 않는 에너지원이다. 태양에너지와 물로부터 수소를 생산하는 기술은 지구상에 널려있는 자연에너지와 물을 사용하기 때문에 인류가 직면한 에너지와 환경문제를 해결하기 위한 가장 이상적인 기술 중의 하나이다.

100 kW급 용융탄산염 연료전지 시스템 개발 IV(MCFC 시스템 시운전) (System Development of a 100 kW Molten Carbonate Fuel Cell IV(System commisioning for operation)

  • 임희천;안교상
    • 대한전기학회:학술대회논문집
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    • 대한전기학회 2005년도 제36회 하계학술대회 논문집 B
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    • pp.1681-1683
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    • 2005
  • The molten carbonate fuel tell(MCFC) is endowed with the high potential especially in future electric power generation industry by its own outstanding characteristics. KEPCO(KEPRI) started a 100 kW MCFC system development program in 1993 and has been executed 100kW system develpilot plant successfully completed first phaseopment by 2005 on the basis of successful results of 25kW system development. In this program, the components and mechanical structure for 100 kW stack and system construction were completed on last year and now system pre-commissioning was being executed. A 100 kW MCFC power plant was constructed at the site of Boryeong Thermal Power Plant. A 100 kW MCFC system has characterized as a high pressure operation mode, $CO_2$ recycle, and externally reforming power generation system. The 100 kW MCFC system consisted with stacks which was made by two 50 kW sub-stacks, 90 cells with 6,000 cm2 active area and BOP including a reformer, a recycle blower, a catalytic burner, an inverter, and etc. The system will be operated under 3 atm pressure condition and expected to last over 5,000 hours by the end of this year.

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균일용액침전법으로 제조한 MgO 함량에 따른 고활성 Ni-MgO-$Al_2O_3$ 촉매에 대한 연구 (The effect of MgO content on highly active Ni-MgO-$Al_2O_3$ catalysts prepared by homogeneous precipitation method)

  • 정유식;이영우;구기영;정운호;윤왕래;서용석
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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    • pp.155-155
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    • 2011
  • 용융탄산염 연료전지(MCFC)는 $650^{\circ}C$에서 작동하는 고온형 연료전지 시스템이다. 이 시스템은 천연가스 등을 개질하여 생산된 수소를 바로 전기로 생산할 수 있는 시스템으로 열효율이 높으며, 현재 대체 발전시스템으로 각광을 받고 있다. MCFC는 개질방식에 따라 내부개질 방식과 외부개질 방식이 있다. 내부개질 방식은 수소를 생산하는 개질기가 스택내부에 장착된 형식으로 천연가스를 스택내부에서 개질하여 바로 전기를 생산하는 방식이다. 이 내부개질반응에 사용되는 촉매로는 알루미나에 고함량 (약 50 wt.%)으로 담지된 니켈(Ni) 계열촉매이 주로 쓰이고 있다. 이 고함량으로 담지된 촉매는 대부분 높은 활성을 보인다. 비교적 낮은 온도 운전조건 (약 $580{\sim}620^{\circ}C$)을 가지는 MCFC 내부개질에 적용하기 위해서는 활성점인 니켈을 최대한 담지체에 고르게 분산 시켜야한다. 이를 위해서 MgO를 이용하여 촉매의 활성점을 높게 분산시키는 연구를 진행 하였다. 촉매를 제조하는 방법으로 요소(urea)를 이용한 균일용액침전법을 이용하였다. 니켈함량은 50 wt.%로 고정을 한 다음, MgO 양과 $Al_2O_3$ 양을 각각 0 ~ 45 wt.%와 5 ~ 50 wt.%로 조절하면서 촉매를 제조하여 그 특성들을 분석하였다. 물성을 비교하기 위해서, X-선 회절분석 (XRD) 및 TPR, 물리화학흡착 실험을 하였다. 촉매의 활성을 살펴보기 위해서, fresh 상태 및 피독 상태에서 메탄수증기 개질활성 실험을 실시하였다. MgO 함량이 없거나 적은 촉매에서는 높은 BET surface area와 작은 NiO, metallic Ni 결정 크기가 나타났다. 반면 MgO 함량이 높은 촉매에서 낮은 BET surface area와 비교적 큰 NiO, metallic Ni 결정 크기가 나타났다. 또한 XRD 분석에서 MgO 함량이 증가할 수 록 MgO 결정 피크가 명확히 나타났으며, $MgAl_2O_4$ 피크는 나타나지 않았다. TPR 분석에서 촉매들의 환원 피크를 측정한 결과, 저함량의 MgO를 포함한 촉매는 $700^{\circ}C$ 부근에 환원 피크가 관찰되었고 MgO가 고함량인 촉매는 환원 피크가 $400^{\circ}C$ 부근에서 관찰되었다. 촉매의 초기 fresh 상태에서의 활성은 고함량 MgO를 포함한 Ni-90M10A 샘플을 제외하고 모든 촉매가 거의 비슷하게 나타났다. 그러나 $K_2CO_3$ 피독 상태에서는 MgO 함량이 증가할 수 록 활성이 좋지 않았음을 알 수 있었다. 따라서 MgO가 소량 포함된 촉매의 경우 fresh 상태에서는 우수한 물성과 활성을 보이지만, 피독상태에서는 MgO가 포함되지 않은 Ni-$Al_2O_3$ 촉매가 우수한 활성을 보였다.

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수송 연료용 부분산화 개질기의 운전특성 (Operation characteristics of partial oxidation reformer for transportation fuels)

  • 이상호;배중면
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2011년도 춘계학술대회 초록집
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    • pp.159.1-159.1
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    • 2011
  • Partial oxidation reformer was fabricated and operated using commercial transportation fuels. Fuel injector and heating coil were used for fuel atomization and startup, respectively. The reformer was designed to produce syngas for $150{\sim}200W_e$ class solid oxide fuel cell. The reformer was operated in the $O_2$/C range between 0.6 and 0.8 while the capacity was fixed at $150W_e$. The temperature range in catalyst bed was between $500^{\circ}C$ and $900^{\circ}C$. Only 83% fuel was converted to $H_2$, CO, $CO_2$ and $CH_4$ at the operating conditions. The lowest temperature increase to $700^{\circ}C$ when the reformer was operated at $200W_e$, Although the temperature profiles was improved, fuel conversion was 88%. On the other hand, fuel was completely converted when micro-reactor operated at the same condition. This difference maybe due to aromatic compounds formation at homogeneous region. In addition, a significant amount of coke deposition was observed at vent line. Homogeneous reaction depends on the degree of mixing. For this purpose, two fluid nozzle and Ultra sonic injector were compared to investigate the effect of atomization. Sauter mean diameter(SMD) of Ultra sonic injector was lower than two-fluid nozzle at test condition. However, conversion efficiency and fuel conversion were not improved by using two-fluid nozzle. these results imply that the temperature of homogeneous reaction region should be controlled to prevent coke formation.

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Polymer Electrolyte Membrane Fuel Cell 시스템의 환경 전과정평가 (Environmental Life Cycle Assessment (LCA) of Polymer Electrolyte Membrane Fuel Cell (PEMFC) System)

  • 김형석;홍석진;허탁
    • 한국수소및신에너지학회논문집
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    • 제29권1호
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    • pp.111-116
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    • 2018
  • The environmental impacts of a 1 kW polymer electrolyte membrane fuel cell (PEMFC) system are quantitatively assessed by performing a Life Cycle Assessment (LCA) study. A PEMFC system produces electricity and heat simultaneously, so an appropriate allocation of associated inputs and outputs is performed between the electricity and heat produced. The environmental impacts of the PEMFC system on the impact categories such as global warming (GW), abiotic depletion (AD), acidification (AC), and eutrophication (EU) are assessed from the life cycle impact assessment. The impact indicator results of the impact assessment on these impact categories are obtained as $3.70E-01kg\;CO_2\;eq./kWh$, 1.86E-03 kg Sb eq./kWh, $4.09E-04kg\;SO_2\;eq./kWh$, and $1.88E-05kg\;PO_4{^{3-}}/kWh$, respectively. For all impact categories studied the most influential stage is the operation stage, which accounts for 98.8%, 98.7%, 70.3%, and 62.3% of the total impact on GW, AD, AC, and EU, respectively. For the impact categories of AD, AC, and EU, most of the environmental impacts during the operation stage is attributed to the production of city gas. However, for the impact category of GW, $CO_2$ emission from the reforming process of city gas is the main reason for the largest contribution of the operation stage to the total impact results.

KOGAS DME 공정의 실증 시험을 통한 최적화 기술개발 (Optimization of KOGAS DME Process From Demonstration Long-Term Test)

  • 정종태;조원준;백영순;이창하
    • 한국수소및신에너지학회논문집
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    • 제23권5호
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    • pp.559-571
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    • 2012
  • Dimethyl ether (DME) is a new clean fuel as an environmentally-benign energy resource. DME can be manufactured from various energy sources including natural gas, coal, and biomass. In addition to its environmentally friendly properties, DME has similar characteristics to those of LPG. The aim of this article is to represent the development of new DME process with KOGAS's own technologies. KOGAS has investigated and developed new innovative DME synthesis process from synthesis gas in gaseous phase fixed bed reactor. DME has been traditionally produced by the dehydration of methanol which is produced from syngas, a product of natural gas reforming. This traditional process is thus called the two-step method of preparing DME. However, DME can also be manufactured directly from syngas (single-step). The single-step method needs only one reactor for the synthesis of DME, instead of two for the two-step process. It can also alleviate the thermodynamic limitations associated with the synthesis of methanol, by converting the produced methanol into DME, thereby potentially enhancing the overall conversion of syngas into DME. KOGAS had launched the 10 ton/day DME demonstration plant project in 2004 at Incheon KOGAS LNG terminal. In the mid of 2008, KOGAS had finished the construction of this plant and has successively finished the demonstration plant operation. And since 2008, we have established the basic design of commercial plant which can produce 3,000 ton/day DME.

고체산화물 연료전지용 연료.물 직접 분무식 촉매 개질기에 관한 실험적 연구 (An Experimental Study on Catalytic Reformer with Direct Spraying of Fuel and Water for SOFC)

  • 이대근;동상근;양제복;김학주;정헌
    • 한국연소학회:학술대회논문집
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    • 한국연소학회 2006년도 제33회 KOSCO SYMPOSIUM 논문집
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    • pp.260-265
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    • 2006
  • An experimental study on the catalytic reformer adopted in the auxiliary power unit system of solid oxide fuel cell was conducted. A 3-fluid nozzle, by which liquid fuel such as diesel, water and air are sprayed and uniformed mixed, was designed and used in this study. An electrically heated monolith inserted in the reformer was used for the vaporization of fuel and water in the transient state of reformer. The reformer uses the partial oxidizing reaction at the catalyst and the supply of water prevents the flame combustion in the spraying zone and lessens the deactivation of catalyst. The result showed that the reforming of liquid fuel can be started by the electrically heated monolith and the 3-fluid nozzle can give the uniform mixing of fuel, water and air. It was also found that the reformer fueled by n-hexadecane can make the reformate, at best, containing $H_2$ at 15.5% and CO at 11.5% that are used as fuel in the solid oxide fuel cell.

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기존 세라믹 및 초고속 용사 분말피막 표면개질 플런저의 내구성 특성에 관한 연구 (A Study on Durability Characteristics for Plungers of Conventional Ceramic and Surface Modification by Powder Coating Using High Velocity Oxygen Fuel Thermal Spray)

  • 배명환;박병호;정화
    • 한국자동차공학회논문집
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    • 제24권3호
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    • pp.285-293
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    • 2016
  • The high velocity oxygen fuel(HVOF) thermal spray is a kind of surface modification techniques to produce the sprayed coating layer. This process is to form the coating layer after spraying the powder to molten or semi-molten state by the ultra-high speed at the high-temperature heat source and conflicting with a substrate. The efficiency of thermal spraying is dropped, however, because the semi-molten powder in a spray process become a factor that degrades the mechanical property by the formed pore within the coating layer. Therefore, it is necessary to melt completely the thermal spray powder in order to produce the coating layer with an optimal adhesive force. In this study, to improve the wear resistance, corrosion resistance and heat resistance, the plungers of high-speed and ultra-high pressure reciprocating hydraulic pumps used in ironworks are manufactured with STS $420J_2$ and are coated by the powders of WC-Co-Cr and WC-Cr-Ni including the WC of high hardness using a HVOF thermal sprayer developed in this laboratory. These are called by the surface-modified plungers. The surface roughness, hardness, and surface and cross-sectional microstructure of these two surface-modified and conventional ceramic plungers are measured and compared before operation with after operation for 100 days. It is found that the values of centerline average surface roughness and maximum height for conventional ceramic plunger are 9.5 to 10.8 and 5.2 to 5.7 times higher than those of surface-modified ones coated by WC-Co-Cr and WC-Cr-Ni because the fine tops and bottoms on surface roughness curve of conventional ceramic plunger are approximately 100 times higher than those of surface-modified ones. In addition, the pores and scratches in the surface microstructure are considerably formed in the order of conventional ceramic, WC-Cr-Ni and WC-Co-Cr surface-modified plungers. The greater the WC content of high hardness powder is less the change in the plunger surface.

전국 보건소 물리치료실 운영 실태와 활성화 방안 (Improving Physical Therapy Services of Health Centers in Korea)

  • 장은주
    • 대한물리치료과학회지
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    • 제3권2호
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    • pp.1021-1036
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    • 1996
  • The purpose of this study are ( i ) to examine operating situation of physical therapy department and job satisfaction of physical therapists in health centers, (ii) to analyze utilization patterns and patient satisfaction of physical therapy services among health center visitors, and finally, (iii) to suggest policy implications in facilitating improvement on physical therapy services of health centers. The materials are collected from 105 physical therapists among nationwide health centers and 203 patients of 5 health centers in Pusan, Korea. The survey is conducted from February 13 to March 30, 1996 with a structured self - administered questionnaire. Major results of the study are as follows. First, the result of regression analysis between job satisfaction and affecting factors identify following variables as the significant determinants; self-development(+), job itself(+), and co-worker support (+). Second, the current operating situation of physical therapy department shows such problem as; i )shortage and unstable job security of physical therapists, ii )absence of rehabilitation specialist, iii )lack of understanding on physical therapy of co-workers, iv)shortage of physical therapy equipment and facility, v)burdensome task of physical therapists, and vi) inappropriate purchase process of equipment. Third, patient satisfaction for physical therapy services are revealed relatively high. And the result of regression analysis between patient satisfaction and affecting factors identify following variables as the significant determinants; credibility of physical therapist(+), satisfaction for waiting time(+), cleanliness(+). Fourth, the patients appeal about physical therapy services such problem as; i) shortage of physical therapists, physical therapy equipment, and facility, ii) inconvenient administrative procedure for utilization physical therapy services. Fifth and last, recommendations for the improvement of physical therapy services of health centers are as follows; i )recruiting more physical therapists, ii )regular employment of physical therapists instead of daily use employment, iii )re-arrangement of facility for patient's convenience, iv )establishing reasonable purchasing system of equipment for physical therapy, v) reforming administrative procedure for patient focused care.

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우리나라 전력부문의 환경유해보조금 개편 효과분석 : 산업용 교차보조금 개편을 중심으로 (Analysis of the Effect of Korea's Environmentally Harmful Subsidy Reform in the Electric Power Sector : Mainly on its Industrial Cross-subsidies Reform)

  • 강만옥;황욱
    • 환경정책연구
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    • 제9권1호
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    • pp.57-81
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    • 2010
  • 고유가 시대인 현실에서 우리나라는 화석연료에 대한 의존도가 높아 저탄소 녹색성장이 가능한 경제사회 구조로의 전환이 시급하다. 현재 화석연료 사용과 관련된 보조금 개편은 환경에 유해한 투입요소에 대한 보조금을 감축 또는 제거하여 경제적 효율성을 제고하고 환경 피해를 완화시켜 사회 전체적으로 편익을 가져올 수 있는 Win-Win 효과가 기대되는 정책방안이다. 특히, 우리나라 전력부문에서 시행되는 보조금 제도 중에서 산업용, 농업용 및 심야전력에 대한 교차보조금의 경우, 전체 전력부문 보조금의 80% 이상을 차지하는 가장 큰 규모인데 본 논문은 전력부문 환경유해보조금 가운데 가장 큰 비중(연간 약 1조 6,583억원)을 차지하는 교차보조금 제도 중에서 산업용 전기의 환경유해보조금 개편 시 기대될 수 있는 파급효과를 가격탄력성 추정을 통해 파악하였다. 가격탄력성 추정에는 ARDL(자기회귀시차분포) 모형을 이용하였고, 기본 데이터는 1990년부터 2007년까지의 분기별 자료를 이용하였다. 본 연구에서 환경유해보조금 제거로 산업용 전력에 대한 연간 에너지 수요변화량은 -12,475,930MWh만큼 사용량이 감소할 것으로 추정되었으며, 이산화탄소 배출량의 경우를 보면 연간 2,644,897톤이 감소하는 것으로 추정되어 보조금 폐지가 이산화탄소 저감에 상당한 기여를 하는 것으로 나타났다. 또한 EU에서 제시한 오염물질 단위당 환경오염비용을 이용하여 배출저감량을 금액으로 환산하면 산업용 전력보조금 제거로 연간 약 1조 1,914억원의 환경개선편익 발생하는 것으로 나타났다. 그리고 이산화탄소의 경우 톤당 25유로를 적용하여 계산하면 산업용 전력보조금 제거로 연간 약 1,062억원의 환경개선편익이 발생하는 것으로 나타났다.

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