• 자원ㆍ환경경제연구
• /
• 제10권4호
• /
• pp.591-617
• /
• 2001

For the past years, there had been some environmental cooperation among East Asian countries to reduce air pollution emissions from China. However, the progress of cooperation has been under developed because of lacking financial support, poor design of planning, and weak economic incentives for the industries. In this paper, some practical approaches have been suggested. First, electric trade to make Asian Grid among countries will be good alternatives for the fossil fuel, such as coal, for China. Secondly, natural gas pipeline from West China to Siberian pipeline would change the whole energy mix in this area around 2010, Therefore, it is very promising area for the energy industries to involve in gas project and get rid of many institutional barriers from China. Lastly, environmental industry is growing fast in East Asian. In China, waste treatment and management, air pollution control, and water quality management are some promising areas for the future. Hence it is desirable for Korea, Japan and China to make a eco-fund or company to boost up environmental technology as well as environmental market size.

• 동력기계공학회지
• /
• 제12권1호
• /
• pp.35-40
• /
• 2008

This paper presents an effective cooling dehumidification method to remove odorous gas from food-wastes. The odorous gases, such as Styrene, Ammonia, Hydrogen sulfide and Acetaldehyde, are produced in environments where temperature is $50\sim80^{\circ}C$ and humidity is $40\sim70%$. Under such conditions, experiments are performed reiteratively using experiment equipments. The effect of the cooling dehumidification is measured via measuring instrument, and this research is focused on improving efficiency. The effect of cooling dehumidification using measuring instrument is validated. At $80^{\circ}C$, four type of gases that was mentioned previously showed generally better cooling efficiency with a good result for a component concentration. Among them, hydrogen sulfide gas demonstrated the highest reduction of 50%.

• 한국농공학회논문집
• /
• 제50권4호
• /
• pp.51-58
• /
• 2008

Unit costs for energy production in bioenergy facilities are dependent upon both fixed cost for facility construction and operational costs including biomass feedstock supply. With the increase of capacity, unit fixed cost could be decreased while supply cost tends to increase due to the longer transportation distance. It is desirable to take into account biomass availability in planning bioenergy facilities. A cumulative curve relationship was proposed to relate biomass availability and cumulative products of biomass amount and transportation distance. Optimum size of gasification facilities was affected by collection cost, biomass cumulative relationship. Based on biomass availability of Icheon-City, optimum sizes were about $400kW_{th}$ for gas production, and about $200kW_{el}$ for power generation. Unit cost of bioenergy production could be substantially reduced by reducing collection cost through supplying biomass from diverse sources including land development areas where significant amount of waste wood is generated. When planning bioenergy facilities, however, biomass availability and spatial distribution are key factors in determining the size of capacity.

• Journal of Advanced Marine Engineering and Technology
• /
• 제23권5호
• /
• pp.670-678
• /
• 1999

Heat recovery steam generator(HRSG) is a principal component of the combined cycle power plant (CCPP) which utilizes the waste energy of the gas turbine exhaust gas. A design of the HRSG is a keypoint to achieve high cycle efficiency with competitive cost. This paper presents a brief review on the design of a HRSG which covers the basic design parameters and their effects on the performance and the investment cost. Finally the concept of the optimum design point is presented according to the selection of a pinch point temperature difference and a steam pressure as an illustrated case.

• 대한설비공학회:학술대회논문집
• /
• 대한설비공학회 2007년도 동계학술발표대회 논문집
• /
• pp.64-69
• /
• 2007

This study is to develop heat recovery system using high performance heat pipe heat exchanger for Middle-high temperature range industrial exhaust gas. The naphthalene is used as working fluid of heat pipe in this study. Single naphthalene heat pipe could transport over 2,000 watts with $0.05^{\circ}C/W$. The heat pipe heat exchanger consist of 50 naphthalene heat pipes recovered 62 kW when over $400^{\circ}C$ gas exhausted and the maximum recovered heat rate was 173 kW in this study.

• 대한설비공학회:학술대회논문집
• /
• 대한설비공학회 2007년도 동계학술발표대회 논문집
• /
• pp.376-381
• /
• 2007

GHP system utilize national gas as a heat source. It reduces electric peak demand in summer and maintains a constant performance in winter by recovering the waste heat from the engine. Although the initial investment cost of GHP is higher than that of EHP, the overall operating cost of GHP is cheaper than of the EHP. In this study, items for dissatisfaction were summarized based on the results of user questionnaire(200 users), and field tests were made for 10 GHP installation places. The measured COP was estimated much lower than the rated COP by the manufacturer mainly due to partial load operation.

• 설비공학논문집
• /
• 제15권8호
• /
• pp.690-696
• /
• 2003

This paper presents the heat recovery performance of water fluidized-bed heat exchanger. Temperature and humidity ratio of waste gas are considered as important parameters in this study. Therefore, the heat recovery rate through water fluidized-bed heat exchanger for exhaust gases with various temperatures and humidity ratios can be estimated from the results of this study. Mass flow ratio (the ratio of mass flow rate of water to that of gas) and temperature of inlet water are also considered as important operating variables. Increase of heat recovery rate can be obtained through either high mass flow ratio or low temperature of inlet water with resultant low recovered temperature. The heat recovery performance with the mass flow ratio of about up to 10 has been investigated. The effect of number of stages of water fluidized-bed on the heat recovery performance has been also examined in this study.

• 한국지하수토양환경학회:학술대회논문집
• /
• 한국지하수토양환경학회 1996년도 사용종료 매립지의 안정화 에 관한 국제 세미나
• /
• pp.87-95
• /
• 1996

The stabilization and reclamation of old disposal sites is becoming more important as significant numbers of disposal sites are closed and abandoned. This technical paper covers an overview of the key issues and methodologies for stabilizing and constructing facilities on old landfills. The slide portion of this presentation also include photographs showing actual construction activities. The key issues that are prevalent in remediating and closing old landfills are : correcting the stormwater flow, leachate breakout, constructing cover caps, controlling landfill gas migration and odors, cleanup groundwater and stabilizing side slopes. Some key techniques for constructing facilities on old landfills include： use of piling, installation of active landfill gas systems, providing LFG barriers under buildings, using utilidors and flexible utility interfaces and designing for site settlement. This Paper provides proven conceptual methods for solving these problems.

• 에너지공학
• /
• 제23권3호
• /
• pp.125-131
• /
• 2014

본 연구에서는 매립가스 증대를 위한 음폐수의 원활한 주입을 위해 혐기성 산발효 전처리를 수행하였으며 이를 통해 점도 감소와 유기산 생산량을 확인하여 매립지 주입을 위한 최적조건을 확인하고자 하였다. 산발효 후 음폐수 가용화율은 약 15% 증가함을 보였고 체류시간의 변화와 반응기형태를 달리 한 결과 큰 차이를 보이지는 않았다. 반응기형태에 따라 점도변화를 확인한 결과 상향류식 반응기에서 $76.95{\pm}3.27%$로 완전혼합반응기에 비해 약 11.38% 높은 점도 저감효율을 보였으며, VFA생산에서는 체류시간을 3일에서 5일로 증가 시 2.01배(상향류식 반응기), 1.76배(완전혼합반응기) 높은 경향을 보였다. 이는 상향류식 반응기의 경우 고정층담체의 스크린 역할로 분자량이 작은 물질에 비해 큰 물질들이 상대적으로 반응기에 체류하는 시간이 길어져 효율이 높은 것으로 사료된다.

• 공업화학
• /
• 제20권4호
• /
• pp.391-395
• /
• 2009

폐목재의 에너지 전환을 위하여 2톤/일 규모의 고정층 가스화기($0.9m{\times}2.4m$)를 제작하여 실험하였다. 고정층 가스화 설비는 3~5 cm의 목재칩을 이용하였으며 하부에는 회전식 스토커가 설치되어있다. 목재칩 연료 투입은 다단 나이프밸브 방식으로 되어 있으며 관성력 집진설비, 가스냉각용 열교환기, ID Fan 및 Cooling tower 등으로 구성되어져 있다. 가스화기는 $700{\sim}1000^{\circ}C$ 사이에서 조업하였으며 CO: 25~40 vol%, $H_2$: 7~12 vol%, $CH_4$: 2~4 vol%, $CO_2$: 12~24 vol%의 조성을 가지는 합성가스가 생성되었다. 합성가스 발열량은 $1100{\sim}1500kcal/Nm^3$으로 나타나 공업로의 적용이 가능하였다. 또한 합성가스의 가스 엔진을 통한 전력 생산도 가능하여 1~4 kW의 전력을 생산하였다.