• Plant Journal
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• v.17 no.1
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• pp.38-49
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• 2021

In order to increase power plant efficiency, the steam temperature was increased to 610 ℃ which deteriorates the durability of the boiler tube and as the use of low-calorie coal increases the post combustion and delayed combustion phenomenon, the overheating of the final reheater and the tube rupture are becoming frequent. In order to prevent overheating of the final reheater, desuperheater water injection was increased, leading to a decrease in boiler efficiency. In this study install a baffle plate at the back of some overheated tube groups, thereby reduce the temperature of the tube by reducing the amount of combustion gas, and the reduced combustion gas moves to an adjacent place to increase the temperature of other tubes. As a result of the study, the temperature deviation between tubes decreased 1.5. And the heat-reducing injection amount was reduced to 6,929 kg/h and the maximum tube temperature was reduced to 623.4℃ which is 6.6℃ more below than the control standard of 630℃.

• Journal of Advanced Marine Engineering and Technology
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• v.36 no.5
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• pp.580-585
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• 2012

In this paper, the cycle performance analysis for condensation and evaporation capacity, total work and efficiency of ocean thermal energy conversion power system using R744 ($CO_2$) is presented to offer the basic design data for the operating parameters of this system. The operating parameters considered in this study include superheating and subcooling degree, evaporation and condensation temperature, pump and turbine efficiency. The main results were summarized as follows : The evaporation capacity of R744 increases with superheating and subcooling degree, but decreases with the increasing condensation temperature. The total work increases with superheating and subcooling degree of R744, but decreases with the increasing evaporating temperature. And, the efficiency increases with subcooling and superheating degree, but decreases with the increasing condensation temperature. Therefore, superheating and subcooling degree, evaporation and condensation temperature and pump and turbine efficiency of R744 OTEC power system have an effect on the evaporation and condensation capacity, total work and efficiency of this system. With a thorough grasp of these effect, it is necessary to design the OTEC power cycle using R744.

• Journal of the Korean Society of Food Science and Nutrition
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• v.29 no.6
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• pp.1190-1194
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• 2000

과열 수증기 공정처리 효과가 현미의 수화 및 조직특성에 미치는 영향을 조사하기 위하여 현미(동진)를 과열수증기의 압력이 $1kg_{f}/$\textrm{cm}^2$$로 유지되는 상태에서 수증기의 온도를 127, 150, 16$0^{\circ}C$로 달리하면서 과열 수증기 처리를 하였다. 수분흡수속도는 수침온도(60~8$0^{\circ}C$)에 따라서 현미와 백미가 각각 0.03569~0.1049 $cm/min^{-1/2}$와 0.03474~0/1618 $cm/min^{-1/2}$의 범위를 보였다. 현미와 백미의 활성화에너지는 각각 6.98 및 9.59 cal/mole을 나타내어 열수화 특성이 다름을 보였다. 한편, 과열 수증기 처리현미의 경우 $65^{\circ}C$에서의 확산계수는 18.96$\times$$10^{-5}$$\textrm{cm}^2$/min)와 처리하지 않은 현미(22.28$\times$$10^{-5}$$\textrm{cm}^2$/min)의 중간 값을 나타내었다. 과열 수증기처리 후 현미의 표면조직은 균열이 발생하였는데, 수증기 온도가 높을수록 균열의 정도가 컸다. 이상과 같은 수증기 처리는 현미 강층의 구조를 변화시킬 뿐만 아니라, 내부 전분층의 부분적 균열에도 효과적으로 작용하는 결과를 보인 것으로 예측된다.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.10 no.1
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• pp.32-38
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• 2009

In this paper, cycle performance analysis for cooling capacity, compression work and COP of R744($CO_2$) transcritical vapor compression refrigeration system is presented to offer the basic design data for the operating parameters of the system. The operating parameters considered in this study include superheating degree, outlet temperature of gas cooler and evaporating temperature in the R744 vapor compression cycle. The main results were summarized as follows : The cooling capacity of R744 increases with superheating degree, but decreases with the increasing evaporating temperature and outlet temperature of gas cooler. The compression work increases with superheating degree and cooling pressure of R744, but decreases with the increasing evaporating temperature. And, The COP increases with outlet temperature and evaporating temperature of R744 gas cooler, but decreases with the increasing superheating degree. Therefore, superheating degree, outlet temperature and evaporating temperature of R744 vapor compression refrigeration system have an effect on the cooling capacity, compression work and COP of this system. With a thorough grasp of these effect, it is necessary to design the compression refrigeration cycle using R744.

• Proceedings of the KIEE Conference
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• summer
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• pp.1148-1150
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• 2004

본 논문에서는 $400^{\circ}C$ 이상의 과열 증기발생을 위하여 6kW급 유도가열장치를 개발하여 식품건조 시스템에 적용한 예를 보인다. 유도가열장치는 과열 증기의 온도를 제어하기 위하여 인버터 입력 전압을 $100\sim200V$로 가변제어가 가능하게 하였고, 인버터 입력 전압은 벅컨버터를 사용하여 기준 전압을 과열증기의 온도에 대한 전압 값을 사용하여 제어하였으며, LC 공진에 의해 발생한 전류로 증기 가열 챔버를 유도 가열하여 과열 증기를 발생하게 하였다. 발생한 과열 증기는 식품 건조를 위하여 건조로에 투입되어 고온 건조에서 식품의 건조시간을 단축시킬 수 있었으며, 식품의 손상을 줄일 수 있었다. 이의 검증을 위하여 유도 가열 장치를 설계/제작하여 실험하였으며, 식품 건조 테스트를 행하였다.

• Journal of the Institute of Convergence Signal Processing
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• v.11 no.2
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• pp.163-168
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• 2010

This paper presents the practical implementation of an over-temperature protection system for power semiconductor devices. In the proposed system, temperature variation is provided with just using $R_{ds(on)}$ characteristics of power MOSFET, while extra device such as a temperature sensor or an over-temperature detection transistor is needed to monitor the temperature in the conventional method. The proposed protection technique is experimentally tested on IRF840 power MOSFET. The PIC microcontroller PIC16F877A is used for the implementation of the proposed protection algorithm. The built-in 10-bit A/D converter is utilized for detecting voltage variance between a drain and a source of IRF840. The induced temperature-resistance relationship based on the measured drain-source voltage, supplies a gate signal to the power MOSFET. If detected temperature's voltage exceeds any a protection temperature's voltage, the microcontroller removes the trigger signal from the power MOSFET. These test results showed satisfactory performances of the proposed protection system in term of accuracy within 1.5%.

• Proceedings of the KIEE Conference
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• 2009.07a
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• pp.1666_1667
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• 2009

최근 국내 표준 화력발전소는 대부분 초 임계압의 관류형 보일러가 설치되어 운전되고 있다. 보일러 출구 증기온도를 정격치 이내로 운전하는 것은 보일러 운전에 중요한 요소이다. 보일러 효율 상승 등을 고려하여 과열기 Tube 재질의 온도 허용 한계치 이내에서 운전이 되어야 한다. 본 논문은 화력발전소에서 부하변동 범위가 넓고, 고효율 운전이 가능한 초 임계압 관류보일러의 동특성과 과열기 온도제어의 구성 및 실제 운전 중인 발전소의 운전데이터를 분석한 내용에 대하여 기술하고자 한다.

• Proceedings of the Korea Institute of Fire Science and Engineering Conference
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• 2013.04a
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• pp.186-187
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• 2013

본 논문에서는 과부하, 과열에 의한 환풍기 동작 특성을 분석하기 위해 노후, 외부 이물질에 의한 날개의 강제 구속을 상정한 환풍기 내부 3개소의 온도 및 발화 특성을 실험적인 방법으로 분석하였다. 환풍기 신품 조건에서 날개 구속에 의한 실험 결과 온도퓨즈 용단으로 과열에 의한 변형이나 발화 위험의 징조는 발견하지 못하였으며 향후 노후 및 오염, 절연불량 등 추가적인 요인을 고려한 발화 위험의 실험이 필요하다고 사료된다.

• Journal of the Korean Institute of Gas
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• v.16 no.2
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• pp.9-13
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• 2012

The present study has been carried out to diagnose the temperature safety of a boiler desuperheater which decreases abnormally higher temperature of superheated steam in a reheater of a power plant. The liquid water in the desuperheater stays in a closed space. It becomes heated by the high temperature superheated steam and boiling could occur. Boiling might increase internal pressure and it could destroy the desuperheater if the internal pressure exceeds the allowable pressure of the desuperheater. The present study modeled reasonably the desuperheater and four cases of heat transfer analysis are executed with the consideration of insulator and natural convective fluid flow of the inside cooling water. For the case excluded the natural convective fluid flow, the temperature exceeds the allowable temperature and pressure. On the other hand, for the real case included natural convective fluid flow and insulator, the active heat transfer from higher temperature region to lower temperature region occurs and it makes the temperature in the cooling water below the allowable temperature and pressure. From this fact, it could be thought that the desuperheater in the reheater is safe from destroy or back flow.

• Korean Chemical Engineering Research
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• v.59 no.1
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• pp.77-84
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• 2021

To control hot spot in a plug flow reactor (PFR) is important for the yield and purity of products and safety. In this paper, coolant temperature is set as a state variable, and radial distributions of heat and mass are considered to model the PFR more realistic than without considering radial distributions. The model consists of three state variables, reactant concentration, reactant temperature, and the coolant temperature. The flow rate of the isothermal coolant is a manipulated variable. This paper shows that the controller considering the radial distributions of heat and mass is more effective than the controller without them. Assuming that u3,0 is 0.7, the suggested control equation was robust when St is bigger than 1.3, and Ac/A is smaller than 2.0. Under this condition, the hot spot temperature changed within the relative error of one percent when the temperature of input altered within the range of five percent.