• Journal of Welding and Joining
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• 제5권2호
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• pp.17-26
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• 1987

In this study, the experiments were carried out for the purpose of establishment of the arc sparing method which reducing oxides or oxide film by using the inert gas as the carrier gas of atomizing particles. Main results obtained are as follows; 1. Oxides and oxide film which lower the adhesion strength are largely reduced by using the inert gas as the carrier gas of atomizing particles, and adhesion strength of coating film are improved. 2. The coating film characteristics appear to be no difference between the inert gas arc spraying in air environment and that in argon gas environment. 3. Inert gas arc spraying using argon as the carrie gas has higher reduction rate of composition element in coating film than compressed air spraying does.

• 대한기계학회논문집B
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• 제27권2호
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• pp.251-258
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• 2003

Natural gas hydrates typically contain 85 wt.% water and 15 wt.% natural gas, and commonly belongs to cubic structure I and II. When referred to standard conditions, 1㎥ solid hydrates contain up to 172N㎥ of methane gas, depending on the pressure and temperature of production. Such large volumes make natural gas hydrates can be used to store and transport natural gas. So, the tests were performed on the formation of natural gas hydrate is governed by the pressure, temperature, gas composition etc. The results show that the formation pressure of structure II is lower about 65% and the solubility is higher about 3 times than that of structure I.

• 한국대기환경학회지
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• 제17권2호
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• pp.223-231
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• 2001

In order to provide some insights into the influence of electric field, gas composition, and gas temperature on electron energy distribution and electron transport characteristics, the Boltzmann equation was solved by using cross section data for electron collisions, Critical electric fields for the corona development in dry air and flue gas are 150 and 80 Td, respectively. It was seen that the decrease of critical electric field in flue gas is mainly caused by the $H_2O$ addition through the comparison of ionization and attachment coefficients of gas components. Increase of $O_2$, $H_2O$, and $CO_2$ contents in gas affected discharge characteristics according to their reciprocal characteristics between lowering the ionization threshold and increasing the electro-negativity. As electric field increases, electrons with higher energies in the electron energy distribution also increase. The mean and characteristic electron energies also linearly increase with electric field. The variation of flue gas temperature did rarely affect on the electron energy distribution function and electron transport characteristics, because the gas temperature is several hundreds or thousands times lower than the electron temperature.

• 설비공학논문집
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• 제15권8호
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• pp.674-682
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• 2003

Natural gas hydrate typically contains 85 wt.% water and 15 wt.% natural gas, and commonly belongs to cubic structure I and II. Also, 1m$^3$ hydrate of natural gas can be decomposed to 200 m$^3$ natural gas at standard condition. If this characteristic of hydrate is reversely utilized, natural gas is fixed into water and produced to hydrate. Therefore the hydrate is great as a means to transport and store natural gas. So, the tests were performed on the formation of natural gas hydrate is governed by the pressure, temperature, gas composition etc. The results show that the equilibrium pressure of structure II is approximately 65% lower and the solubility is about 3 times higher than structure I. Also if the subcoolings of structure I and structure II are more than 9 K and 11 K respectively, the hydrates are rapidly formed.

• Advances in Energy Research
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• 제3권3호
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• pp.181-194
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• 2015

In this work, an experimental study of the gasification on wood was carried out in downdraft type fixed bed Gasifier attached with 10 kW duel fuel diesel engine. The main objective of the study was to use wood as the biomass fuel for downdraft Gasifier and to evaluate the operating parameter of gasifier unit to predict its performance in terms of gas yield and cold gas efficiency. The influence of different biomass on fuel consumption rate, gas yield and cold gas efficiency was studied. Composition of producer gas was also detected for measuring the lower heating value of producer gas to select the feed stock so that optimum performance in the existing gasifier unit can be achieved. Under the experimental conditions, Lower heating value, of producer gas, cold gas efficiency and gas yields, using wood as a feed stock, are $4.85MJ/m^3$, 46.57% and $0.519m^3/kg$.

• 한국가스학회지
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• 제17권6호
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• pp.27-32
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• 2013

바이오가스, 매립가스와 같은 신재생 가스 연료는 Biomass, 유기성 폐기물 등으로부터 얻을 수 있기 때문에 대기 중의 이산화탄소를 증가시키지 않고 재순환시키는 탄소중립적인 특성이 있어 지구온난화에 대응할 수 있는 장점이 있다. 따라서 다량의 불활성가스로 인한 저발열량, 원료 및 공정에 따른 연료조성 변화 등의 단점에도 불구하고 이를 엔진에 적용하여 에너지를 생산하고자 하는 노력이 계속되어왔다. 이중에서도 연료조성의 변화는 엔진 성능에 큰 영향을 미칠 수 있기 때문에 이에 대한 연구가 필요한 실정이다. 따라서 이번 연구에서는 신재생가스연료에 포함된 불활성가스의 양을 변화시켜 연료 조성 변화를 모사하고 이를 엔진의 연료로 사용함으로써 연료 조성의 변화가 엔진 성능 및 배기배출 특성에 주는 영향을 파악하였다. 또한 엔진 효율 및 배기 성능을 향상시키기 위한 방안에 하나로 보다 긴 전극을 갖는 스파크 플러그를 적용하였으며 그 결과를 기존의 Base 스파크 플러그 시험 결과와 비교하였다.

• 청정기술
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• 제12권3호
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• pp.138-144
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• 2006

저압에서 용량성 라디오 주파수 방전을 이용하여 메탄을 합성가스로 전환시키는 반응을 고찰하였다. 플라즈마에서 발생된 높은 에너지를 갖는 전자들이 메탄분자와 산소를 함유하고 있는 기체 분자들과 충돌에 의해 합성가스로 전환되었다. 입력전력, 함산소화합물의 종류, 함산소화합물과 메탄의 조성이 메탄 전환율 및 수소와 일산화탄소의 수율에 미치는 영향을 살펴보았다. 메탄 전환율은 최대 100%이었으며, 합성가스이외의 다른 화합물들은 거의 생성되지 않았다. 입력전력이 증가함에 따라 메탄전환율과 합성가스의 수율이 증가하였으며, 함산소화합물의 종류에 따라 각각 다른 조성의 합성가스를 생성할 수 있었다. 메탄과 함산소화합물을 함께 반응시킴으로써 순수한 합성가스를 제조할 수 있었는데 함산소화합물의 종류에 따라 합성가스의 조성을 조절할 수 있었으며 불순물이 거의 없는 순수한 생성물을 얻을 수 있었다.

• Asian-Australasian Journal of Animal Sciences
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• 제20권4호
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• pp.517-522
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• 2007

The aim of this study was to compare in vitro gas production kinetics, metabolizable energy (ME), organic matter digestibility (OMD) and microbial protein (MP) production of widely used legume hays in ruminant nutrition in Turkey. Gas production were determined at 0, 3, 6, 12, 24, 48, 72 and 96 h and their kinetics were described using the equation p = a+b ($1-e^{-ct}$). There were significant differences among legume hays in terms of chemical composition. The crude protein content of legume hays ranged from 11.7 to 18.6% of dry matter (DM); crude fat from 2.1 to 3.5% DM; neutral detergent fiber from 35.6 to 52.0% DM; acid detergent fiber from 32.0 to 35.5% DM and acid detergent lignin 1.7 to 11.0% DM. Total gas production after 96 h incubation ranged between 61.67 and 76.00 ml/0.200 g of substrate. At 24, 72 and 96 h incubation the total gas production for common vetch were significantly (p<0.01) higher than those of the other legume hays. The ME, OMD and MP of legume hays ranged from 9.09 to 11.12 MJ/kg DM, 61.30 to 75.54% and 90.35 to 138.05 g/kg DM, respectively. The ME, OMD and MP of common vetch was significantly (p<0.01) higher than those of the other hays due to low cell-wall contents and high crude protein. At the end of the experiment, differences in chemical composition of legume hays resulted in the differences in the in vitro gas production, gas production kinetics and the estimated parameters such as ME, OMD and MP. Common vetch can be recommended to hay producers and ruminant breeders, due to high ME, OMD and MP production.

• 대한환경공학회지
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• 제36권2호
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• pp.147-152
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• 2014

본 연구에서는 폴리설폰 중공사막을 이용하여 화석연료 연소에서 배출되는 온실가스 중 $CO_2$의 회수에 관한 연구를 실시하였다. 고농도의 $CO_2$를 회수하기 위한 막분리 공정에 대한 선행연구이다. 혼합가스 분리거동 관찰을 위하여 이산화탄소가 10% 함유된 배기가스를 사용하였다. 압력, 온도, 주입가스 조성, 다단 막 변화를 주어 스테이지 컷에 따른 분리 성능을 조사하였다. 압력과 온도가 증가 할수록 투과측에 $CO_2$ 농도와 회수율이 증가하였다. 주입 가스 조성 변화 시 $CO_2$의 함량이 높을 경우 회수율 및 분리 효율이 높아졌다. 3단 분리막 시스템을 이용시 $CO_2$ 농도 95% 이상, 회수율 90% 이상 보였으며 1단 분리막 보다 분리율이 향상되었다.

• 한국수소및신에너지학회논문집
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• 제26권5호
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• pp.445-452
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• 2015

A tubular packed bed reactor for the steam-$CO_2$ combined reforming of natural gas to produce the synthesis gas of a target $H_2/CO$ ratio 2.0 was simulated. The effects of the reactor dimension, the feed gas composition, and the gas feeding temperature upon the possibility of coke formation across the catalyst bed were investigated. For this purpose, 2-dimensional heterogeneous reactor model was used to determine the local gas concentrations and temperatures over the catalyst bed. The thermodynamic potential distribution of coke formation was determined by comparing the extent of reaction with the equilibrium constant given by the reaction, $CH_4+2CO{\Leftrightarrow}3C+2H_2O$. The simulation showed that catalysts packed in the central region nearer the entrance of the reactor were more prone to coking because of the regional characteristics of lower temperature, lower concentration of $H_2O$, and higher concentration of CO. With the higher feeding temperature, the feed gas composition of the increased $H_2O$ and correspondingly decreased $CO_2$, or the decrease in the reactor diameter, the volume fraction of the catalyst bed subsequent to coking could be diminished. Throughout the simulation, reactor dimension and reaction condition for coking-free operation were suggested.