• Title/Summary/Keyword: 온도차에너지

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A Study on the Ultrasonic Relaxation of Axial-Equatorial Isomerization in Methylcyclohexane (Methylcyclohexane의 초음파 완화현상의 연구)

  • 배종림;김정구
    • The Journal of the Acoustical Society of Korea
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    • v.17 no.6
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    • pp.3-7
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    • 1998
  • Methylcyclohexane의 초음파 흡수측정을 0.1-2MHz의 주파수 범위, 온도 30-60℃에 걸쳐 1MHz이하에서 정확한 초음파 흡수측정이 가능한 광 회절 초음파 공명법을 사용하여 행하였다. 그 결과, axial과 equatorial에 의한 완화는 단일 완화현상을 보였고 그 스펙트럼 으로부터 완화 주파수와 완화강도를 결정하였다. 완화 주파수의 온도 의존성으로부터 활성 화에너지(△H*)=10.0㎉/㏖을, 완화 강도의 온도 의존성에서 엔탈피 차(△H)=1.8㎉/㏖을 각각 구하였다.

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Optimal Ccontrol Strategy of Cooling System for Polymer Electrolyte Membrane Fuel Cell using Hardware-In-the-Loop Simulation (Hardware-In-the-Loop Simulation을 이용한 고분자 전해질 연료전지 냉각시스템 최적 제어기법 연구)

  • Choi, Eunyeong;Ji, Hyunjin
    • Journal of Energy Engineering
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    • v.25 no.1
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    • pp.113-121
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    • 2016
  • Polymer electrolyte membrane fuel cell(PEMFC) requires cooling system to maintain the proper operating temperature(about $65^{\circ}C{\sim}75^{\circ}C$) because the efficiency and power are affected by operating temperature. In order to retain the operating temperature of PEMFC, cooling system and coolant control logic are needed. Hardware-in-the-loop simulation(HILS) is one of effective methods to study and evaluate control algorithm. In this paper, the HILS system was designed to study the coolant control algorithm. The models of HILS system consisted of PEMFC, heat exchanger, and external environment associated with temperature. The hardwares in HILS system are 3-way valves, pumps, and a heat exchanger. The priority control and the control target temperature were investigated to improve the control performance using HILS. The 3-way valve in $1^{st}$ cooling circuit was selected as priority control target. The under limit value of $2^{nd}$ 3-way valve set as a function of PEMFC power and $2^{nd}$ circuit coolant temperature to correct temperature control performance. As a result, the temperature of PEMFC is stably controlled.

A Numerical Study of the 3-D Flow in the Primary Calcinator of Porcelain (도자기 1차 소성로의 3차원 유동장 수치해석에 관한 연구)

  • 김성수;홍성선;박지영;오창섭
    • Journal of Energy Engineering
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    • v.5 no.1
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    • pp.50-55
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    • 1996
  • A numerical simulation on a primary calcinator of porcelain was performed with using Fluent to calculate the heat efficiency by studying velocity vector and temperature profile according to variables such as the location of outlet and porcelain. Control-Volume based Finite Difference Method and Up-wind scheme are used for discretization of differential equation. SIMPLEC Algorithm and standard k-$\varepsilon$ turbulent model are selected to resolve the pressure-velocity coupling and the turbulent. The result of simulation showed that the whole velocity vector field in a calcinator was varied greatly according to the location of outlet. But the whole temperature profile at each zone was still high regardless of the location of outlet because of the radiation. But the temperature of a case with a outlet at sidepart of preheating or cooling zone was little high compared to the case with a outlet on the top of preheating zone. The velocity vector field and temperature profile in a calcinator were almost not affected by the location of porcelain, but the temperature inside a porcelain was much affected according to the place where it was located. The heat efficiency in a calcinator was 44.6% and the gas temperature in the outlet was about 1000 K.

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A Study on Boiling Characteristics of Direct Contact LNG Evaporator (직접접촉식 액화천연가스 기화기의 비등특성 연구)

  • 김남진;김종보
    • Journal of Energy Engineering
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    • v.4 no.3
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    • pp.420-428
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    • 1995
  • 현재 사용하고 있는 액화천연가스 기화기는 관내부로 -162$^{\circ}C$의 액화가스가 흐르고, 관외부로 발전소 증기응축기 출구에서 배출된 20~3$0^{\circ}C$의 해수를 흐르도록 하여, 두 유체사이의 온도차로 기화시키는 간접접촉방식 열교환기가 사용되고 있다. 그러나 간접접촉방식 열교환기는 두 유체사이의 큰 온도차로 인한 금속재료의 피로현상과 해수의 염분에 의한 재질의 부식 및 미생물 부착 등의 원인으로 열전달효율이 저하되고 있다. 따라서 본 연구는 관을 중간매체로 하는 간접접촉식 열교환기대신 액화천연가스와 기화용수인 물을 직접접촉시키는 방법으로 이용하여, 위와 같은 문제점들을 근본적으로 해결하려 한다. 본 실험에서는 기화기내의 수위 500 mm와 물의 유량 10 l/min을 일정하게 고정시키고, 액화천연가스의 유량 0.12 ㅣ/min, 0.36 l/min, 0.6 l/min, 기화기내의 압력을 100 kPa, 300 kPa, 500kPa로 변화시키면서 기화기내의 기포, 온도분포, 급팽창현상, 동결현상 및 기화후 수분함유량등의 비등특성을 규명하였다. 실험결과 기화기내의 압력이 증가할수록 기포는 작고 균일한 분포를 이루고, 폭발적인 급팽창현상은 일어나지 않았다. 또한 동결현상은 액화천연가스의 기화를 방지하지 못하였으며, 기화된 천연가스내의 수분함유량 몰%는 압력과 유량이 증가함에 따라 감소하는 경향을 보이고 있다.

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A study on the required energy of a thermal type desalination plant (증발식 해수담수화설비의 에너지 소모량에 관한 연구)

  • Song, Chi-Sung
    • Journal of Advanced Marine Engineering and Technology
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    • v.38 no.9
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    • pp.1094-1100
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    • 2014
  • TEvaporator is key component in food, seawater distillation and waste water treatment system, which is basically to concentrate the raw liquid by evaporating the pure water under vacuum condition. The liquid concentration is performed through the membrane, electro-dialysis and evaporation. In this study, only the evaporating type was treated for evaluating the economic analysis with the various operating conditions. The results of this study showed that the performance of the OT-MSF desalination system is increased with decreasing the temperature difference between the neighboring evaporators, which means that the number of evaporators is increased, under the determined design conditions.

Kinetic Study on Carbon Dioxide and Methane Hydrate in Silica Gel Pores (실리카겔 공극에서의 이산화탄소 및 메탄 하이드레이트 생성속도)

  • Kang, Seong-Pil;Lee, Jae-Goo
    • 한국신재생에너지학회:학술대회논문집
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    • 2007.11a
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    • pp.590-593
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    • 2007
  • 물을 함유한 공극 크기 6, 30, 100 nm의 실리카겔에 이산화탄소 및 메탄을 반응시켜 온도$0{\sim}4$ $^{\circ}C$, 압력 $15{\sim}40$ bar 의 범위에서 가스 하이드레이트 생성속도를 측정하였다. 공극 크기가 작아짐에 따라 특정 온도에서의 평형압력이 높아지는 열역학적 특성을 감안하여 통일한 압력차 (평형압력과 실험압력의 차)를 얻을 수 있도록 조건을 설정하였다. 이산화탄소의 경우 통일 온도에서 하이드레이트 생성속도는 일반적으로 압력이 높아짐에 따라 가속되는 것을 알 수 있었다. 단위 물 당 포집되는 이산화탄소의 양은 최대 1.0을 넘지 못하였다. 또한 하이드레이트 생성을 위해 필요한 유도시간 (induction time)이 2내지 8시간 수준으로 매우 길었다. 공업적인 하이드레이트 이용을 위해서는 빠른 생성속도가 필요한 만큼 유도시간을 단축, 없애기 위해 계면활성제로 황산 도데실 나트륨 (sodium dodecyl sulphate)이 첨가된 수용액을 이용하였다. 계면활성제가 포함된 수용액에서의 하이드레이트 생성은 유도시간이 사라져 매우 빠르게 바뀌었고, 포집되는 이산화탄소도 15% 정도 증가되었다. 메탄의 경우에는 공극 크기가 작아질수록 하이드레이트 생성속도 및 가스 포집도가 저하되는 결과를 보였다. 이산화탄소의 경우와는 다르게 유도시간이 나타나지 않았으며 비교적 높은 가스 포집도를 얻기 위해서는 평형압력과 실험압력의 차이가 최소 2.0MPa 이상이어야 했다.

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Analysis of Air Temperature and Humidity Distributions and Energy Consumptions according to Use of Air Circulation Fans in a Single-span Greenhouse (단동온실 내 공기순환팬 사용에 따른 온습도 및 에너지소비량 비교 분석)

  • Lee, Tae Seok;Kang, Geum Choon;Kim, Hyung Kweon;Moon, Jong Pil;Oh, Sung Sik;Kwon, Jin Kyung
    • Journal of Bio-Environment Control
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    • v.26 no.4
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    • pp.276-282
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    • 2017
  • The aim of this study was to compare and analyze air temperature and humidity distribution and energy consumptions according to using air circulation fans in single-span greenhouses. The greenhouses located in Cheongnam-myeon, Cheongyang-gun, Chungcheongnam-do, Korea. There were cherry tomatoes in the greenhouses and the size of greenhouses was as follows;ridge height : 3.2 m, wide : 6 m, length : 95 m. The heating system was composed of a hot-water boiler and 6 FCUs(Fan Coil Unit)-4 FCUs were on bottom with duct and 2 FCUs were installed at 2.0 m. A total of 18 air circulation fans(impeller's diameter : 230 mm) were bilaterally arranged in 2 rows in the experimental greenhouse. The sensors for measuring air temperature and humidity were located at a quarter and three quarters of a length. The height of sensors were 0.8 m, 1.8 m. To calculate energy consumption in greenhouses, water temperature at inlet and outlet in a water pump, volume of water were measured. Form February 3rd to March 23th, temperature, humidity and energy consumptions were measured during heating time(6pm~7am). In a greenhouse without fans, the average differences of temperature and humidity were $0.75^{\circ}C$, 2.31%, respectively. The operation of fans showed their differences to $0.42^{\circ}C$, 1.8%. The standard deviation of temperature and humidity between measuring points in the greenhouse with fans was lower than the greenhouse without fans. Total energy consumptions in a greenhouse without fans were 4,673 kWh. In the greenhouse with fans, the total energy consumptions were 4,009 kWh. The energy consumptions in a greenhouse with fans 14.2% were less than the greenhouse without fans. Therefore, air circulation makes temperature and humidity uniform and saves energy consumptions for heating.

A Study on Performance Improvement of the Electrode for PEMFC (고분자 전해질 연료전지용 전극의 성능 향상에 관한 연구)

  • 이정규;하흥용;오인환;최형준;홍성안;전해수
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 1999.11a
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    • pp.89-93
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    • 1999
  • 연료전지는 전기화학 반응에 의해서 전기와 열을 생산하는 발전장치로서 Carnot's 효율에 제한 받는 기존 연소기관보다 높은 효율의 에너지를 얻을 수 있는 장점이 있어 이에 대한 연구가 전 세계적으로 활발하게 진행되어 오고 있다. 그 중에서도 특히 고분자 연료전지는 전해질 누출이 없고 낮은 온도에서 작동하며 부식이 없을 뿐 아니라 stack 디자인의 간편성, 큰 압력차에 대한 내구성, 긴 수명 등의 장점으로 인하여 자동차나 이동전원에 가장 적합한 장치로 평가되고 있다.(중략)

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An Experimental Study on LTD Stirling Engine (MM-7) for the Development of TM Electric Conversion System (TM발전변환기 개발을 위한 저온도차 스털링엔진(MM-7)의 성능실측 연구)

  • Kim, Yeongmin;Chen, Kuan;Chun, Wongee
    • Journal of Energy Engineering
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    • v.25 no.1
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    • pp.9-14
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    • 2016
  • This study has been carried out to develop TM (Thermal to Mechanical) conversion systems for electric power generation using one of the Low Temperature Differential (LTD) Stirling engines called MM-7 capable of harnessing low temperature waste heat whose temperature is only $20{\sim}30^{\circ}C$ above the ambient. Measurements were made on the torque and rpm for a number of temperature differentials between the engine hot and cold ends, which could be effectively applied in developing the most suitable configuration for the high performance TM (Thermal to Mechanical) conversion system.

Design and Estimation of Performance of Heat Regenerator for Small-scale Regenerative Radiant Tube Burner (소형 축열식 복사관 버너시스템용 축열기 설계 및 성능평가)

  • 조한창;조길원;이용국
    • Proceedings of the Korea Society for Energy Engineering kosee Conference
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    • 2004.05a
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    • pp.171-176
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    • 2004
  • Heat regenerator attached in small-scale regenerative radiant tube burner was designed using the theoretical computation code and was confirmed the performance of waste heat recovery ratio. From the computation, when ceramic ball of 4-5kg was used, temperature efficiency and available waste heat recovery ratio were predicted 80% and 70%, respectively. Similar efficiencies were obtained from the experiments using LPG. However, since exhaust gas temperature entered into regenerator was below 85$0^{\circ}C$ which was much lower than that we expected, preheat air temperature was lowered below 80$0^{\circ}C$.

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