• 한국소음진동공학회:학술대회논문집
• /
• 한국소음진동공학회 2009년도 춘계학술대회 논문집
• /
• pp.601-605
• /
• 2009

The paper deals with the proper design of GGH(gas-gas heater) panel elements of desulfurization equipments in a thermoelectric power plant. When fossil fuels such as coal, petroleum et cetera are burnt to ashes, sulfur oxide compounds are produced, and calcareous sludges are deposited at GGH panel elements. In this case, operation of a power plant equipments is interrupted, and a tremendous economic loss comes into existence. One of the purposes of the paper is to find flow velocity distributions and regions of depositions when calcareous sludges pile up on the GGH panel elements through the fluid analysis. In the fluid analysis, flow velocity and position distributions of particles between GGH panel elements are demonstrated according to time variation for ammonia and calcium hydroxide particles.

• 한국콘크리트학회:학술대회논문집
• /
• 한국콘크리트학회 2001년도 봄 학술발표회 논문집
• /
• pp.935-940
• /
• 2001

This study search for absorbing sound and exhaust-gas which aims to manufacture continuous void by using clay and foam, the surface of materials is covered with $TiO_{2}$ powder as heat treatment. According to the results of the experiment, the increase of thickness of manufactured sound absorbing materials caused the increase of absorption rate in the range of low and middle sound and thus it can be an important factor of improving absorption rate. Sound absorbing materials could satisfy 70% of the average of sound absorption ratio in 7cm thickness. Also, the manufactured sound absorbing materials is covered with $TiO_{2}$ showed an excellency in the clarification of exhaust-gas under ultraviolet rays treatment when 70% of removal rate and about 10% of generation rate of $NO_{2}$ is settled by the flow of 2 $\ell$/min NO gas. Especially, manufactured sound absorbing materials could improve compressive strength of continuos porous concrete. in the case of 7% bubble addition, when the substitution rate of coagulator was 30% and 20%, compressive strength was 45kgf/$cm^{2}$ and 65kgf/$cm^{2}$ respectively. As the substitution rate of coagulator reducing, compressive strength increased after preforming burnt clay.

• 한국소음진동공학회논문집
• /
• 제20권7호
• /
• pp.611-619
• /
• 2010

The paper deals with the proper design of GGH(gas-gas heater) panel elements of desulfurization equipments in a thermoelectric power plant. When fossil fuels such as coal, petroleum et cetera are burnt to ashes, sulfur oxide compounds are produced, and calcareous sludges are deposited at GGH panel elements. In this case, operation of a power plant equipments is interrupted, and a tremendous economic loss comes into existence. One of the purposes of the paper is to find flow velocity distributions and regions of depositions when calcareous sludges pile up on the GGH panel elements through the fluid analysis. In the fluid analysis, flow velocity and position distributions of particles between GGH panel elements are demonstrated according to time variation for ammonia and calcium hydroxide particles.

• 한국추진공학회지
• /
• 제24권4호
• /
• pp.55-65
• /
• 2020

본 논문에는 75톤급 액체로켓엔진 가스발생기의 개발시험과 수락시험 결과가 기술되어 있다. 현재까지 44기의 가스발생기 모델을 이용하여 330회 이상, 누적 연소시간 7,000 초 이상의 가스발생기 단독 시험이 수행되었다. 시험을 통해 75톤급 가스발생기가 연소압력, 연소효율, 압력손실, 연소안정성, 연소가스 온도 등에서 신뢰성과 재현성이 높은 특성을 보여준다는 것이 확인되었다. 한국형발사체용 75톤급 가스발생기의 마지막 시리즈에 해당하는 5기는 2019년 말까지 제작 완료되어 2020년 상반기에 수락시험이 수행될 계획이다.

• 한국항공우주학회지
• /
• 제41권8호
• /
• pp.632-638
• /
• 2013

본 논문에서는 네덜란드 부게넘 및 국내 태안 IGCC플랜트의 석탄으로부터 생성된 합성가스의 화염안정성 및 연소불안정성에 대해 기술하였다. GE7EA 모사 가스터빈 연소기를 대상으로 상압 고온 연소시험을 수행하여 입열량 및 질소희석에 따른 연소특성을 관찰하였다. 시험결과를 통해 화염안정화 선도는 화염의 구조에 따라 Regime I부터 VI까지 6개의 영역으로 구분하였고, 2개의 영역(Regime I, II)에서 화염이 안정적으로 연소되는 것을 확인하였다. 태안 및 부게넘 합성가스 모두 안정하게 연소되고, 화염이 외부 재순환 유동과 결합되는 Regime II에 해당하는 것을 확인하였다. 또한 $H_2$/CO비만을 고려하면 수소의 함량이 높은 부게넘 가스가 안정적 연소구간이 넓지만, 질소희석을 고려할 때 부게넘 가스 내의 더 많은 질소가 화염안정성에 부정적 영향을 미치기 때문에 태안 합성가스가 부게넘 합성가스보다 더 안정적으로 연소하였다.

• 한국식품과학회지
• /
• 제39권4호
• /
• pp.366-371
• /
• 2007

어육장의 휘발성 향기 성분들을 용매추출을 이용하여 분리, 농축하였으며, GC-MS로 분석하였다. 총 36가지의 휘발성 성분들이 검출되었으며, 11개의 aliphatic hydrocarbons, 4개의 acids, 2개의 ketones, 5개의 phenols, 7개의 alcohols, 1개의 pyrazine, 4개의 pyrones와 furanones, 2개의 miscellaneous components 등으로 구성되어 있었다. 특히, acids인 butanoic acid가 높은 함량을 나타내었다. 어육장의 향기활성 성분을 규명하기 위해 용매추출을 이용하여 휘발성 성분들을 분리 후 향추출물 희석분석법으로 flavor dilution(FD) $factor(Log_3$ FD)를 구하였다. 이 결과 어육장에서 총 20종의 향기활성 성분들이 확인되었다. 이 중 군덕내의 특성을 지닌 butanoic acid와 구운 감자향을 지닌 methional이 높은 FD factor를 보였으며, 이들 성분 외에 높은$(Log_3$ FD>7)를 나타내는 성분들로는 2-methyl-2-butanol(soysauce-like), 3-hydroxy-2-butanone(buttery), 2-furanmethanol(burnt sugar-like) 등이 있었다. 본 실험에서는 어육장을 시료로 하여 휘발성 향기성분 및 향기활성 성분들을 GC-MS 및 AEDA법에 의해 분석함으로 어육장 특유의 향미특성을 규명하였다. 이는 앞으로 고급화된 장류 제품으로서는 물론, 다양한 식품에서 조미소재로의 어육장의 활용도를 높이는데 기여할 것이다.

• 한국안전학회지
• /
• 제8권4호
• /
• pp.107-113
• /
• 1993

Small rectangular explosion chamber of its size 25cmX25cmX32cm with a circular bursting diaphram at the top was used to study the mechanism of gas explosion to fire transition phenomena, the process of ignition of solid combustibles during a gas explosion. To visulize the explosion to fire transition phenomena, transparent acryl window and high speed camera system were used. The test piece of solid combustible in this experiments was a 5cm$\times$5cm square sheet of newspaper which was placed in the explosion chamber filled with a LPG-air mixture. The mixture was ignited by an electric spark at the center of the chamber. Explosion to fire transition phenomena and the behavior of out flow and in flow of gas through the opening yielded by bursting the diaphram was visualized with shlieren system and without shlieren system. Diameter of a bursting dlaphram at the top of the explosion chamber was varied 5cm, 10cm, and 15cm, and the position of test piece were varied with 6 point. Explosion pressure was measured with strain type pressure transducer, and the weight difference of the test piece before and after each experimental run was measured. By comparing the weight difference of solid combustibles before and after the experiment and the behavior of out flow and inflow of gas after explosion, it was found that the possibility of ignition was depends on the LPG-air mixture concentration and the exposure period of test piece to the burnt gas. Test result of this experiments it was found that the main factor of this phenomena are that heat transfer to the test piece, and the pyrolysis reaction of test piece. Based on the results, the mechanism of the explosion to fire transition phenomena were inferred ; gas explosion- heat transfer to solid combustibiles ; pyrolysis reaction of solid combutibles : air inflow ; mixing of the pyroly gas with air ignition.

• 한국소음진동공학회:학술대회논문집
• /
• 한국소음진동공학회 2011년도 춘계학술대회 논문집
• /
• pp.453-458
• /
• 2011

Air preheater uses the waste heat of the gas which burnt from the boiler from the thermal power plant. Air preheater it is established in the exit of the boiler follows in change of temperature combustion gas and the vibration which it follows in thermal expansion and contraction occurs. Air preheater with ruse the gas the seal the place where it includes a gap in the structure which it does, the vibration which it follows in change of temperature fluctuates the displacement of gap, fluctuation of the leakage quantity which occurs from gap there is a possibility of decreasing an effect to system. Part system it will be able to control the interval of gap in order, control mechanism about under establishing the place where it does the gap control actively, measures a gap the displacement sensor for is necessary. Like this displacement sensor the condition must do continuous running from atmosphere of high temperature was demanded all. This paper investigates the implementation instance of hazard existing which implement the high temperature displacement sensor, it analyzes, produces the result which it examines a model, it was a presentation. These results with the fact that it will contribute in the research for the implementation and a localization of the high temperature displacement sensor and advanced air preheater.

• 한국농공학회논문집
• /
• 제64권5호
• /
• pp.9-16
• /
• 2022

Syngas, also known as synthesis gas, synthetic gas, or producer gas, is a combustible gas mixture generated when organic material (biomass) is heated in a gasifier with a limited airflow at a high temperature and elevated pressure. The present research was aimed at modifying the existing LPG engine generator for fully operated syngas. During this study, the designed gasifier-powered woodchip biomass was used for syngas production to generate power. A 6.0 kW LPG engine generator was modified and tested for operation on syngas. In the experiments, syngas and LPG fuels were tested as test fuels. For syngas production, 3 kg of dry woodchips were fed and burnt into the designed downdraft gasifier. The gasifier was connected to a blower coupled with a slider to help the air supply and control the ignition. The convection cooling system was connected to the syngas flow pipe for cooling the hot produce gas and filtering the impurities. For engine modification, a customized T-shaped flexible air/fuel mixture control device was designed for adjusting the correct stoichiometric air-fuel ratio ranging between 1:1.1 and 1.3 to match the combustion needs of the engine. The composition of produced syngas was analyzed using a gas analyzer and its composition was; 13~15 %, 10.2~13 %, 4.1~4.5 %, and 11.9~14.6 % for CO, H₂, CH₄, and CO₂ respectively with a heating value range of 4.12~5.01 MJ/Nm³. The maximum peak power output generated from syngas and LPG was recorded using a clamp-on power meter and found to be 3,689 watts and 5,001 watts, respectively. The results found from the experiment show that the LPG engine generator operated on syngas can be adopted with a de-ration rate of 73.78 % compared to its regular operating fuel.

• 대한금속재료학회지
• /
• 제50권10호
• /
• pp.753-761
• /
• 2012

The reduction behavior of low level oxides such as (T.Fe), (MnO) and ($P_2O_5$) in molten EAF slag was investigated using commercial reductants. In an air atmosphere, the slag volume increased and the reduction rate of the slag was very low due to the oxidation loss of reductants by oxygen in the air. The reduction rate of the slag was also low when a commercial reductant was used alone in an Ar gas atmosphere. The reason is probably because the material transfer through the interface between the slag and reductant is difficult due to the formation of high melting point oxide. When reductants were mixed with burnt lime in order to form low melting point reaction products, the reduction rate of the slag increased up to the range of 45-70%. By using the mixtures of reductants and burnt lime so as to form a low melting point slag at the reaction end, the reduction rate of the slag was improved up to 60-85%.