• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2001년도 추계학술대회논문집B
• /
• pp.776-781
• /
• 2001

To enhance thermal efficiency of thermal facility through recovery of low and medium temperature waste heat, 1MW organic Rankine cycle system was designed and developed. The exhaust gases of $175^{\circ}C$ at two 100MW power plants in pohang steel works were selected as the representative of low and medium temperature waste heat in industrial process for the heat source of the organic Rankine cycle system. HCFC-123, a kind of harmless refrigerant, was chosen as the working fluid for Rankine cycle. The organic Rankine cycle system with selected exhaust gases and working fluid was designed and constructed. From the operation, it was confirmed that the organic Rankine cycle system is available for low and medium temperature waste heat recovery in industrial process. The optimum operating manuals, such as heat-up of hot water, turbine start-up, and the process of electric power generation, were derived. However, electric power generated was not 1MW as designed but only 670kW. It is due to deficiency of pump capacity for supply of HCFC-123. So it is necessary to increase the pump capacity or to decrease the pressure loss in pipe for more improved HCFC-123 supply.

• 설비공학논문집
• /
• 제28권10호
• /
• pp.408-413
• /
• 2016

The objective of this study is to investigate the performance of a heat recovery heat pump dryer using a R245fa refrigerant experimentally. In this study, the main components of the heat pump dryer were an evaporator, a compressor, a condenser, and an expansion valve. As a result, when the amount of refrigerant varied from 15 kg to 16 kg, the hot air outlet temperature in the condenser and the heat transfer rate were almost kept constant. Therefore, the amount of refrigerant at 16 kg was considered to be a suitable amount in the heat pump. As the air inlet velocity varied from 0.5 m/s to 1.5 m/s, the highest temperature in the condenser could be obtained when the air inlet velocity was 0.5 m/s. The heat transfer rate, system (COP), and hot air outlet temperature were 5.6 kW, 3.4, and $102.5^{\circ}C$, respectively, when the bypass ratio and water temperature were 0% and $60^{\circ}C$.

• 한국가스학회지
• /
• 제15권1호
• /
• pp.40-45
• /
• 2011

공정운전 중 운전자의 실수나 장치의 고장 등으로 형성되는 과압을 방지하기 위해 blowdown system을 통해 가스를 방출시켜 과압을 해소한다. 방출된 가스는 대부분 탄화수소 혼합물로서 가연성과 독성을 가지고 있으므로 플레어스택에서 연소시킨 후, 공기 중으로 배출시킨다. 그러나 화학공장의 규모가 증가하고 복잡해지면서 폐가스의 양이 증가하여 안전상의 이유로 플레어스택의 높이를 높이거나 추가적인 플레어시스템을 설치하여야 하는 문제가 발생하였다. 이 논문에서는 이러한 문제를 해결하기 위해 버려지는 폐가스를 회수하여 연료로 사용하는 Flare Gas Recovery System을 도입한 해결방안을 제시하고자 하였다.

• International Journal of Air-Conditioning and Refrigeration
• /
• 제9권4호
• /
• pp.17-26
• /
• 2001

Simulation was conducted using TRNSYS to evaluate the thermal performance of a facility. This facility has a condensing-type heat exchanger which is able to recover the latent energy for the purpose of reducing the heating energy in winter. The boiler and chiller are selected based on the annual peak loads and controlled to maintain the facility at the set temperature of 14~$17^\circ{C}$. Supplied energy by the boiler and recovered energy by the heat exchanger were calculated as a function of number of pass through heat exchanger, kind of fuel and hot water velocity. Simulation results show that about 20% of the total heating load can be recovered by the heat exchanger and the amount of latent heat is increasing with the number of pass. This means that the efficiency of the waste energy recovery system can be increased by using a condensing-type heat exchanger rather than a traditional sensible heat exchanger.

• Korean Chemical Engineering Research
• /
• 제47권1호
• /
• pp.133-140
• /
• 2009

본 연구에서는 투과도 80 md, 하이드레이트 포화도 30%의 다중공 평판형 시스템에서 열자극 감압법에 의한 생산실험을 수행하여 하이드레이트의 해리양상 및 생산효율을 관측 및 분석하였다. 감압의 크기에 따른 실험결과에서, 운영 압력을 낮게 설정하면 높은 가스회수율을 얻을 수 있지만 생산초기 나타나는 강한 펄스가 생산전 운영에 무리를 줄 수 있다고 판단되었다. 또한 흡열반응에 의한 하이드레이트 재형성으로 오히려 회수율이 감소하는 경우가 발생하였다. 감압법 적용시의 생산거동을 더 상세히 분석하기 위해, 감압크기 140 psi와 320 psi에 대해 각각 4, 6회의 반복실험을 진행하였다. 그 결과, 140 psi로 감압크기를 설정한 경우, 생산초기에 불안정한 거동이 나타나지만, 빠르게 안정화됨을 알 수 있었다. 320 psi의 실험결과에서 불연속적이며 간헐적인 생산거동을 확인할 수 있었다. 열자극 실험은 안정적인 생산거동을 보이며 회수율이 비교적 낮아 열자극의 효과를 잘 관찰할 수 있는 압력차 80 psi를 적정운영 압력으로 설정하여 수행하였다. 열자극감압 혼용기법의 결과로부터 열자극시간이 증가할수록 가스회수율은 증가하였지만, 반면 에너지효율은 오히려 감소하는 것으로 나타났다. 열을 2분간 가한 후 열흡수 시간을 1분으로 설정한 경우 본 시스템에서는 회수율이 상승하였으며, 에너지효율 또한 증가되는 결과를 얻었다. 하지만, 열흡수 시간이 1분 이상일 경우 오히려 더 낮은 회수율과 에너지효율을 보였는데 이는 긴 열흡수 시간으로 인한 열손실에 기인한 것으로 판단된다.

• 한국안전학회지
• /
• 제14권4호
• /
• pp.78-84
• /
• 1999

A compact air-preheating type heat exchanger was developed and tested for the ultra-high temperature heat recovery applications. For the direct use of exhaust gases up to $1200^{\circ}C$, the heat exchanger adopted a ceramic core with high strength and low thermal expansion coefficient less than $1{\times}10^{-6}^{\circ}C^{-1}$. The ceramic core was fabricated by special extrusion and bonding techniques. To minimize thermal stresses in the core, spring-loaded sealing mechanism was designed and successfully installed. 1-pass air flow scheme was adopted for the compactness and cost-savings. The pressure test for the ceramic core showed no failure under 35 kPa and less than 3% leak under 7 kPa. Flue gas simulation system was developed to investigate the performance of the heat exchanger. The test results showed normal operations of the heat exchanger up to $1200^{\circ}C$ of exhaust gases and relatively high heat recovery efficiencies of 31～39% depending upon exhaust gas temperatures..

• 한국태양에너지학회:학술대회논문집
• /
• 한국태양에너지학회 2008년도 추계학술발표대회 논문집
• /
• pp.273-279
• /
• 2008

The purpose of this study is not only to evaluate thermal performance but also to find the stress behavior of heat transfer tubes under the part load operation in Heat Recovery Steam Generator. Flow analysis was performed to know the behavior of exhaust gas from gas turbine and thermal performance was calculated using distribution of hot exhaust velocity. In addition, tubes temperature during operation were gathered from actual plant to verify the uneven flow distribution under part load operation. Stress analysis was performed using tubes temperature data gathered from actual plant under both part and full load operations to know the stress behavior of tubes.

• 대한용접접합학회:학술대회논문집
• /
• 대한용접접합학회 2002년도 Proceedings of the International Welding/Joining Conference-Korea
• /
• pp.378-383
• /
• 2002

In previous study, the decrease and recovery of total stiffness in welded structure was discussed on the basis of experimental examination through tensile loading and unloading test of welded specimen. The recovery of structure stiffness was caused by the release of welding residual stress through mechanical loading. In this study, analysis model that is indispensable for the effective application of MSR method was established on the basis of test and measurement result. Thermal elasto-plastic analysis for welding process was performed by non-coupled analysis. Analysis results of welding process were transfer to elasto-plastic model for tensile loading & unloading by restart technique. In elasto-plastic analysis model for mechanical loading & unloading, hardening appearance of weld metal was considered by rezoning technique and tying technique was used for JIG condition of test machine.

• Geomechanics and Engineering
• /
• 제19권6호
• /
• pp.523-532
• /
• 2019

Based on the formation characteristics, wellbore parameters and insulated tubing (IT) parameters of the Shengli oilfield, Shandong, China, a geomechanical model is built to predict the temperature distributions of the wellbore and formation. The effects of the IT heat conductivity coefficient (HCC), well depth and IT joint on the temperature distribution of the IT, completion casing, cement sheath, and formation are investigated. Results show the temperature of the formation around the wellbore has an exponentially decreasing relation with the distance to the wellbore. The temperature of the formation around the wellbore has an inverse relation with the IT HCC when the temperatures of the steam and the formation are given. The temperature of the casing outer wall is mainly determined by the steam temperature and IT HCC rather than by the initial formation temperature. The temperature of the casing at the IT joint is much larger than that of the other location. Due to the IT joint having a small size, the effects of the IT joint on the casing temperature distribution are limited to a small area only.

• 설비공학논문집
• /
• 제28권4호
• /
• pp.165-170
• /
• 2016

Long-term performance of the enthalpy exchange element is a topic of current interest due to the concern of possible performance degradation over time. In this study, a 350 CMH enthalpy recovery ventilator equipped with an enthalpy exchange element was installed in an office room, and the performance has been traced over the past 5 years. The appearance, overall dimension, thermal performance, leakage ratio and anti-bacterial performance were checked annually. Results showed that the change in thermal performance (sensible, latent and enthalpy efficiency) was negligible with periodic cleaning with an air gun. However, the leakage ratio increased with time, measuring 7.3% after 5 years. Anti-bacterial test revealed that no bacteria were found during the test period. The largest change in the dimension occurred at the middle location of the element, although the change was less than 2% of the initial value.