• 환경위생공학
• /
• 제11권1호
• /
• pp.39-44
• /
• 1996

The pressure fluctuations in a gas-solid fluidized bed has been analysed using s statistical method interpreting fluidized 냥d behavior. The performing statistical a analysis of the pressure fluctuations in a fluidized bed of 6.7cm-ID. using uniform p particle size of 115 to $1015{\mu}m$ in diameter. The fluidized gas used air(velocity 0.1~1.2m/sec) at settled bed height to diameter ratios which is LlD=l.O. Then, the pressure fluctuations measured by DPT(differantial pressure transducer). The measuring characteristic values of pressure fluctuation were the mean value and standard value, and also, it has been found that the standard deviation of the pressure fluctuations can be effectively used to predict minimum fluidizing velocity and to explain the fluidized phenomena.

• 한국방재학회 논문집
• /
• 제1권3호
• /
• pp.93-102
• /
• 2001

본 연구에서는 HEC-6 모형을 이용하여 태화강 본류하도 하구부에 위치한 방사보의 영향에 따른 하상변동특성을 분석 검토함으로서, 향후 태화강 하도종합개발계획 수립시에 효과적으로 이용할 수 있도록 하였다. 하상변동특성 분석에 필요한 유량 조건은 태화강 하천정비기본계획수립에서 검토된 풍수량, 홍수량 및 계획홍수량 조건을 이용하였다. 먼저, 하상변동폭에 대한 분석 결과, 삼호교 하류 하도구간에서는 유하유량이 클수록 세굴과 퇴적이 활발히 진행되고 있으나 삼호교 상류 하도구간에서는 큰 변동이 없는 것으로 분석되었다. 다음으로, 유사이송능을 검토한 결과, 유하유량이 클수록 유사이송능은 큰 값으로 추정되었으나 계획홍수량 유하시 방사보 철거전후의 태화강 하구부의 유사이동능은 큰 차이가 없는 것으로 분석되었다. 따라서, 방사보 철거로 인한 토사유입량 감소대책을 고려하여 태화강 하류부에서 유입되는 동천지류의 최하류부에 하천유지용수 확보와 태화강으로의 유사량 유입을 감소시키기 위하여 적절한 수리 구조물을 설치한다면 방사보 제거 후에도 태화강 최하류부의 유사량 퇴적을 감소시키는 좋은 방안이 될 것으로 판단된다.

• 한국연소학회:학술대회논문집
• /
• 한국연소학회 2005년도 제31회 KOSCO SYMPOSIUM 논문집
• /
• pp.231-237
• /
• 2005

Interruption of good fluidization in a fluidized bed ash cooler(FBAC) for discharging bed materials such as sand or coal ash particles from the CFB combustor is frequently happened because of agglomeration of the particles in the bed. This unstable operation may, in the worst case, result in an unscheduled boiler shut down. In this study, we examined the operation problems of the FBAC of Tonghae CFB boiler and studied and introduced the simple detection and solution techniques with analyzing the mixing property and the occurrence of defluidization in a simulated fluidized bed ash cooler system (0.5m-H x 0.5m-W x 1.0m-L). The bridge of the large particles at the bed surface could be observed, and this caused to form the defluidization area at the entrance of the FBAC. The defluidization was affected not only by airflow rates but also by the particles discharging rates as well as particle size distribution in the FBAC. The local defluidization could be detected by analysis of the accumulated standard deviation error at a given period of time. Also, the regulation of the overall or local airflow rate made clearing up the local defluidization possible.

• 한국안전학회지
• /
• 제14권3호
• /
• pp.101-109
• /
• 1999

This study attempts to analyse the solid mixing in the feeder and the packing effect for pressure fluctuations in the fluidized bed. To study the mixing characteristics of solid in vibrating feeder for the stable operations of fluidized combustion, the system consisted of two groups of particles such that fine particles were located on the top of the coarse particles before vibratory mixing had started. The effects of packing materials on the pressure fluctuations in a fluidized bed were analysed by using a statistical method to interpret the behavior of fluidized bed. The experiments were carried out in a fluidized bed of 6.7cm-ID, and the experimental variables were particle sizes, of 115 to 1,015$\mu\textrm{m}$ in diameter and the multi-sized particles haying Rosin-Rammler and Gaussian distributions. The settled bed heights of particles to diameter ratios (L/D) were ranged from 0.5 to 2.0. And fluidizing of particles was carried out by air. The packing materials used were screen packing, and the properties of the pressure fluctuations in the fluidized bed were measured by a differential pressure transducer. The properties of the pressure fluctuations calculated were the mean, the standard deviation, and the major frequency of the power spectral density functions. From the characteristics of fluidizing, it was found that the standard deviation of pressure fluctuations could be effectively used to explain the fluidized phenomena, and the packing materials affected severely the properties of the pressure fluctuations. As a result, from the interpretation by spectral analysis, the effects of measuring radius of pressure fluctuations on standard deviation were constant in the case of the fluidized bed with and without packing materials. However, the effects of measuring the height of pressure fluctuations on standard deviations were linear increasing for the fluidized bed with packing materials, but were constant for the fluidized bed without packing materials at 4.5cm above the gas distributor. The major frequency of pressure fluctuations was found to be nearly independent of fluidized system. Also, the major frequency of pressure fluctuations decreased with increasing packing size, and it had maximum value at 10% of the packing amount.

• 한국환경과학회지
• /
• 제5권3호
• /
• pp.361-367
• /
• 1996

An inverse fluidized-bed biofilm reactor (IFBBR) was used for the treatment of highly-emulsified oily wastewater. When the concentration of biomass which was cultivated in the synthetic wastewater reached to 6000 mg/1, the oily wastewater was employed to the reactor with a input COD concentration range of 50 mg/1 to 1900 mg/l. Virtually the IFBBR showed a high stability during the long operation period although soma fluctuation was observed. The COD removal efficiency was maintained over 9% under the condition that organic loading rate should be controlled under the value of 1.5 kgCOD/$m^3$/day, and F/M ratio is 1.0 kgCOD/kgVSS/day at $22{\circ}C$ and HRT of 12 hrs. As increasing organic loading rates, the biomass concentration was decreased steadily with decreasing of biofilm dry density rather than biofilm thickness. Based on the experimental jesuits, it was suggested that the decrease in biofilm dry density was caused by a loss of biomass inside the biofilm.

• 한국안전학회지
• /
• 제14권3호
• /
• pp.84-92
• /
• 1999

The effects of air velocity and excess air on combustion characteristics were studied in a fluidized bed combustor. The domestic low-grade anthracite coal with heating value of 2010 kcal/kg and the imported bituminous coal from Australia with heating value of 6520 kcal/kg were used as coal samples. The combustion characteristics of mixed fuels in a fluidized bed combustor could be interpreted by pressure fluctuation properties, ash distribution and gas emission. The properties of the pressure fluctuations, such as the standard deviation, cross-correlation function, dominant frequency and the power spectral density function, were obtained from the statistical analysis. From this study, the combustion region increased with increasing air velocity but decreased with excess air due to combustion characteristics of anthracite and bituminous coal.

• 한국산학기술학회논문지
• /
• 제9권2호
• /
• pp.487-492
• /
• 2008

본 논문은 유동층반응기에서 메탄 열분해에 의한 수소 생산과 탄소 생성에 대한 연구를 수행하였다. 환경에 대한 영향을 최소화한 상태에서 one-step에 의한 메탄의 전환반응을 메탄 분해촉매활성에 영향을 미치는 인자에 대하여 연구하였다. 측정된 압력요동특성치의 해석을 통하여 유동층 열분해촉매의 유동화현상을 측정하였으며, 유동화특성에 따른 메탄열분해능을 측정하였다. 메탄의 분해능는 생성되는 수소의 농도로부터 측정하였다. 유동층의 특성인 층내 입자 이동성, U-Umf, 마모, 비산유출, 유동화가스의 효율밀도에 따른 분해효율에 미치는 영향을 고찰하였다.

• 대한토목학회논문집
• /
• 제31권4B호
• /
• pp.333-341
• /
• 2011

본 연구에서는 RANS를 지배방정식으로 하는 3치원 수치모의를 이용하여 댐 붕괴로 인한 3차원적인 흐름 특징이 지배하는 댐 직하류에서 댐 붕괴파의 전파 현상, 특히 홍수파의 비정상성과 불연속성, 홍수파와 그 빈사파의 영향, 상류 및 사류 흐름의 혼재, 마른 하도에서의 전파, 이동상 수로에서의 전파와 같은 복잡한 현상을 포함하는 홍수파의 전파를 해석하였다. 부분 댐 붕괴로 인한 홍수파의 전파 해석과 90${\circ}$ 만곡을 가지는 실험수로에서의 홍수파 전파 해석에서는, 2차원 천수방정식을 지배방정식으로 사용하는 수치모의의 한계점으로 지적되었던 댐 붕괴 지점에서의 급격한 수위 변화와 저수지에서의 수위 진동 현상을 제대로 모의할 수 있었다. 또한 댐을 경계로 상류와 하류의 지형이 평행하거나 상류가 높은 또는 하류가 높은 계단형의 이동상 수로에서의 홍수파의 전파 및 하상변동을 성공적으로 모의할 수 있었다.

• 산업기술연구
• /
• 제30권B호
• /
• pp.83-89
• /
• 2010

Generally, the accuracy of the prediction of flood elevation is difficult to identify due to the sedimentation on a river bed, earth and sand being moved by flow, and localized torrential downpours caused by climate change. It is also because of natural and artificial influences on rivers. To predict river floodings successfully, more precise and reliable flood elevation prediction system is needed, in which the concentration time of downstream is numerically interpreted through analyzing and utilizing the watermark of the upper region. Therefore, this research analyzed the prediction methods of the changes in water levels, which use the watermarks of the upper region. The watermarks which impacts the spot being predicted of flood was selected through floodgate analysis and correlation analysis. With the selected watermarks, a statistically reliable regression equation was yielded.

• Journal of Industrial and Engineering Chemistry
• /
• 제68권
• /
• pp.274-281
• /
• 2018

Experimental studies of the hydrodynamic performance of the draft tube conical spout-fluid bed (DCSF) were conducted using pharmaceutical pellets. The experiments were carried out in a DCSF consisted of two sections: (a) a conical section with the cross section of $120mm{\times}250mm$ and the height of 270 mm, (b) a cylindrical section with the diameter of 250 mm and the height of 600 mm. The flow characteristics of solids were investigated with a high speed camera and a pezoresistive absolute pressure transducer simultaneously. These characteristics revealed different flow regimes in the DCSF: packed bed at low gas velocities, fluidized bed in draft tube at higher gas velocities until minimum spouting, and spouted bed. The stable spouting was identified by the presence of two dominant frequencies of the power spectrum density of pressure fluctuation signature: (i) the frequency band 6-9 Hz and (ii) the frequency band 12-15 Hz. The pressure drops across the draft tube as well as the annulus measured in order to better recognize the flow structure in the DCSF. It was observed that the pressure drop across the draft tube, the pressure drop across the annulus, and the minimum spouting velocity increase with the increase in the height of draft tube and distance of the entrainment zone, but with the decrease in the distributor hole pitch. Finally, this study provided novel insight into the hydrodynamic of DCSF, particularly minimum spouting and stable spouting in the DCSF which contains valuable information for process design and scale-up of spouted bed equipment.