• Clean Technology
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• v.25 no.1
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• pp.74-80
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• 2019

Thermochemical treatment of sewage sludge is an energy-intensive process due to its high moisture content. To save the energy consumed during the process, the hydrothermal carbonization process for sewage sludge can be used to convert sewage sludge into clean solid fuel without pre-drying. This study is aimed to investigate co-firing characteristics of the hydrothermally carbonated sewage sludge (HCS) to a pulverized coal combustion system. The purpose of the measurement is to measure the pollutants produced during co-firing and combustion efficiency. The combustion system used in this study is a furnace with a down-firing swirl burner of a $80kW_{th}$ thermal input. Two sub-bituminous coals were used as a main fuel, and co-firing ratio of the sewage sludge was varied from 0% to 10% in a thermal basis. Experimental results show that $NO_x$ is 400 ~ 600 ppm, $SO_x$ is 600 ~ 700 ppm, and CO is less than 100 ppm. Experimental results show that stable combustion was achieved for high co-firing ratio of the HCS. Emission of $NO_x$ and $SO_x$ was decreased for higher co-firing ratio in spite of the higher nitrogen contents in the HCS. In addition, it was found that the pollutant emission is affected significantly by composition of the main fuel, regardless of the co-firing ratios.

• Korean Chemical Engineering Research
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• v.46 no.3
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• pp.561-566
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• 2008

Gasification plant using petroleum coke for refinery and power generation process is increased from considering petroleum coke as a valuable fuel. In this study, gasification of petroleum coke was performed to utilize petroleum coke and to develop essential technology using 1T/D coal gasification system. In case of petroleum coke gasification, because of lower reactivity, consumption of oxygen is higher than coal gasification. The calorific value of syngas from petroleum coke mixed with coal at a mass ratio of 1:1 shows about $6.7{\sim}7.2MJ/Nm^3$. Although carbon conversion could reach more than 92% according to oxygen amount, cold gas efficiency shows lower value than the case of coal. Therefore, it was shown that complemental study in burner design to atomize slurry droplet is required to elevate gasification performance of petroleum coke which has lower reactivity than coal.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.20 no.5
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• pp.1671-1678
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• 1996

In external chemical vapor deposition processes including VAD and OVD the distribution of flame-synthesized silica particles is determined by heat and mass transfer limitations to particle formation. Combustion gas flow velocities are such that the particle diffusion time scale is longer than that of gas flow convection in the zone of particle formation. The consequence of these effects is that the particles formed tend to remain along straight smooth flow stream lines. Silica particles are formed due to oxidation and hydrolysis. In the hydrolysis, the particles are formed in diffuse bands and particle formation thus requires the diffusion of SiCl$\_$4/ toward CH$\_$4//O$\_$2/ combustion zone to react with H$\_$2/O diffusing away from these same zones on the torch face. The conversion kinetics of hydrolysis is fast compared to diffusion and the rate of conversion is thus diffusion-limited. In the language of combustion, the hydrolysis occurs as a Burke-Schumann process. In selected conditions, reaction zone shape and temperature distributions predicted by the Burke-Schumann analysis are introduced and compared with experimental data available. The calculated centerline temperatures inside the reaction zone agree well with the data, but the calculated values outside the reaction zone are a little higher than the data since the analysis does not consider diffusion in the axial direction and mixing of the combustion products with ambient air. The temperatures along the radial direction agree with the data near the centerline, but gradually diverge from the data as the distance is away from the centerline. This is caused by the convection in the radial direction, which is not considered in the analysis. Spatial distribution of silica particles are affected by convection and diffusion, resulting in a Gaussian form in the radial direction.

• Journal of the Korean Society of Propulsion Engineers
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• v.20 no.1
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• pp.37-42
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• 2016

In this study, we examined the burning rate of the uncured propellant (with and without a curing agent application) in order to inspect the process of the HTPB solid propellant. The burning rate of the uncured propellant, that did not contain the curing agent, was approximately 9.7 mm/s at 1000 psi. In relation to the curing time, the burning rate was constant. The propellant, with the curing agent application, was approximately 8.1 mm/s showed a tendency of slowing as it burned. When the cure reaction rate was low, in accordance to the time, there were small changes in burn rate. However, when the cure reaction rate was high, the difference in burning rate was increased. The burning rate of a fully-cured propellant was approximately 6.8 mm/s, which appeared to be the lowest in order.

• Resources Recycling
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• v.29 no.6
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• pp.114-124
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• 2020

In the cement industry, NOx emission is recognized as an important problem, and NOx reduction technologies can be divided into process change, staged combustion, low NOx burner, selective non-catalytic reduction and selective catalytic reduction method. The operation of the selective non-catalytic reduction method, which is the most used in the cement industry, is expected to make it difficult to meet the emission standards to be strengthened in the future, and it is necessary to improve equipment such as SCR and secure technologies. Recently, we are developing technologies for simultaneous application of SNCR and SCR, dust and denitrification filter technology, and removal technology using NO oxidation.

• Journal of Practical Agriculture & Fisheries Research
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• v.9 no.1
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• pp.121-132
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• 2007

1. 버섯종균 개선 버섯의 품질과 수량을 좌우하는 주요 요인은 종균의 활력이다. 그러나 라오스에서는 종균의 활력이 낮아 조그마한 100cc 병에 배양완성하는데 14일이 소요되는 등 볍씨종균의 균사생장과 균사밀도가 매우 낮음을 확인하였다. 따라서 100cc 병을 1000cc 비닐봉지로 개선하여 입봉하는데 소요되는 시간을 10배로 단축 개선하였다. 또한 곡립종균을 액체종균으로 대처한 결과 균사생장속도가 2배가 빨랐으며 작업속도가 4배가 빨라졌다. 2. 버섯배지제조 방법 개선 미세하고 건조한 톱밥에 수분을 첨가하는데 50%이하의 수분함량을 유지함으로서 균사가 표면에만 자라고 있는 것을 확인하고 버섯 배지제조 시 물리성을 개선하기 위하여 볏짚을 잘게 잘라 10%~100%까지 혼합하는 실험을 실시하였다. 그 결과 톱밥 50%에 볏짚 50% 혼합하는 것이 균사생장 속도와 밀도가 좋았다. 또한 왕겨도 30%정도 혼합한 배지처리에서 가장 좋았다. 또한 수분함량도 65%로 향상하여 혼합하도록 지도하였다. 3. 버섯배지살균 방법 개선 라오스에서는 왕겨를 태워 살균을 실시하고 있다. 화력이 약하여 살균한 배지에서 볍씨의 새싹이 돋아나오는 경우를 발견하였다. 이는 살균이 제대로 되지 않았음을 의미한다. 그래서 이동식 직화식 살균을 권하였으나 시설자재값이 감당이 안되어 엄두를 내지 못하였다. 따라서 가스버너를 도입하여 단시간에 화력을 높여 살균을 실시하므로서 세균의 증식을 막아 균사생장속도를 빠르게 하고 균사량의 축적을 높이는데 교육을 하고 컨설팅을 실시하여 개선하였다. 4. 병뚜껑과 형성틀을 대체한 링을 이용한 입봉작업시간 단축과 비용절감 버섯봉지에 배지를 담는 입봉작업을 할 때 병뚜껑과 그의 형성틀을 끼우고 솜을 조금 뜯어 톱밥배지 위에 놓는 작업을 한다. 이는 아주 잘못된 방법이다. 왜 그렇게 하는가하는 것은 이해가 간다. 그렇게 하는 이유는 접종할 때 실내에서 그냥 접종하므로 뚜껑을 열때 보호막 역할을 할 것으로 생각하고 그렇게 하는데 천만의 말이다. 어떻든 뚜껑을 열면 잡균이 들어가는 것은 마찬가지이다. 그래서 이 솜을 배지표면에 놓으면 마른 솜이 그렇지 않아도 수분이 적은데 이 솜이 수분을 또 빼앗아 가버린다. 그래서 균사생장이 늘려 15일이면 다 자라야할 균사배양기간이 한달씩 걸려도 표면만 살짝 잘린 결과가 빗어진다. 이렇게 표면만 균사가 사탕 발림식으로 자라면 품질이 저하되고 수량이 적고 병해충에 저항력이 약해지게 된다. 따라서 뚜껑과 형성틀, 솜을 모두 없애고 봉지 상단부위를 U자형으로 꺽어서 링을 끼우는 방법을 실제로 실험으로 보여준 결과 작업능률이 5배로 빠르고 작업공정이 빨라짐으로서 세균번식밀도가 적어 균사생장 속도가 2배로 빨라졌고 수량이 배가됨을 증명하고 보급하여 많은 호평을 받았다.