• Title/Summary/Keyword: Solid bed

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Effects of Operating Variables on Solid Separation Rate in Two-interconnected Fluidized Beds System for Selective Solid Circulation (선택적 고체순환을 위한 2탑 유동층 시스템에서 고체분리속도에 미치는 조업변수들의 영향)

  • Ryu, Ho-Jung;Jin, Gyoung-Tae;Bae, Dal-Hee;Kim, Hong-Ki
    • Korean Chemical Engineering Research
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    • v.47 no.3
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    • pp.355-361
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    • 2009
  • Effects of operating variables on solid separation rate in two-interconnected fluidized beds system for selective solid circulation have been investigated. Coarse(212~300 or $425{\sim}600{\mu}m$) and fine($63{\sim}106{\mu}m$) particles were separated using the solid separator and the solid separation rate was ranged from 66 to 987 g/min. The solid separation rate increased as the gas velocity through the solid injection nozzle, solid height, diameter of solid injection nozzle, particle size of coarse particles, aperture of the solid separator, and weight fraction of fines in the solid mixture increased. However, the effect of the fluidization velocity was negligible.

Experimental Measurement of Hydrodynamics and CFD Simulation of Circulating Fluidized Bed for MTO Process (MTO 공정을 위한 상온 순환유동층 장치의 수력학적 특성의 측정 및 유동모사)

  • Lim, Jonghun;Lee, Donghyun;Park, Sangsoon;Chae, Hojeong;Jeong, Soonyong
    • 한국신재생에너지학회:학술대회논문집
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    • 2010.06a
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    • pp.163.1-163.1
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    • 2010
  • MTO 공정을 개발하기 위한 순환유동층 장치에서 고체순환량을 높이기 위해 고체 주입량 및 상승관 유속에 따른 수력학적 특성의 파악에 관한 연구를 수행하였다. 전체 높이 2.6m 직경 0.009m의 상승관을 가진 순환유동층 장치에 대해 고체순환량을 조절하기 위한 비기계적 밸브로 각각 Seal-pot과 L-valve가 장착된 두 장치에 대해 고체순환량 및 체류량을 측정하였다. 고체순환량 및 체류량은 두 장치에서 모두 고체의 주입량이 증가함에 따라 증가하는 모습을 나타내었으며, 상승관의 유속에 따라서는 특정한 유속의 범위 내에서 증가하다가 일정 유속 이후 감소하는 모습을 나타내었다. Seal-pot을 사용한 장치에서는 고체순환량이 최대 $87kg/m^2.s$ 가량의 값을 나타내었으나 L-valve를 사용한 장치에서는 최대 $180kg/m^2.s$를 보였다. 이러한 실험 결과를 바탕으로 하여 전산유체역학을 이용한 순환유동층의 유동해석에 관한 연구를 실시하여 실험조건의 변화에 따른 상승관 내부의 수력학적 특성을 비교하였다.

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Numerical Simulation of the Liquid Flow in the Lower Part of the Blast Furnace - A Cold Flow Case (고로하부 액체유동에 대한 수치해석 사례 - 냉간유동)

  • Jin, Hong-Jong;Choi, Sang-Min;Jung, Jin-Kyung
    • Journal of the Korean Society of Combustion
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    • v.13 no.2
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    • pp.33-41
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    • 2008
  • The high permeability of the gas in the molten iron of the dripping zone of the blast furnace is a major factor in achieving the stable operation of a furnace with high productivity. Basic studies of the liquid flow behavior in a packed bed are necessary to grasp the effect of various operational changes on conditions in the dropping zone. Molten iron and slag together playa critical role in the lower zone, transporting mass and energy, while impairing and redistributing the gas flow. In turn, molten iron and slag undergo physical and chemical changes, and are redistributed radially as they descend to the hearth. In this research, mathematical formulations are derived for the gas and the liquid. The solid phase is fixed with constant porosity. The information for the molten iron and slag includes the hold-up, velocity, pressure, and information related to the areas of interaction between the gas and the liquid, and the solid and the liquid. Predictable results include the velocity, pressure and temperature distribution. Additional parameters include the packed particle size and the air blast rate.

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Solid Descending Velocity by Gravity in a Vertical Downcomer (수직관에서 중력에 의한 고체하강속도)

  • Ryu, Ho-Jung;Park, Jaehyeon;Shun, Do-Won;Lee, Seung-Yong
    • Korean Chemical Engineering Research
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    • v.50 no.3
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    • pp.522-526
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    • 2012
  • New experimental method to measure solid descending velocity in a vertical downcomer was presented and effects of downcomer diameter and particle properties on descending velocities for Geldart group A, B, and D particle have been measured and investigated. The effect of initial solid inventory on solid descending velocity was negligible. However, solid flow rate, solid circulation rate and solid descending velocity increased as the downcomer diameter increased. Moreover, solid descending velocity increased linearly as the downcomer diameter increased and showed distinguishable trend for Geldart group D particle from Geldart group A and B particles. Empirical correlations of solid descending velocity for Geldart group D and Geldart group A and B particles have been derived based on the measured values. The correlations could predict well the solid descending velocities.

Biopharmaceutical Evaluation of a Solid Dispersion System Containing Sibutramine Freebase

  • Lee, Min-Suk;Chang, Hee-Chul;Kim, Taewan;Park, Jung-Hwa;Lee, Bong-Sang;Kim, Sung-Hee;Kim, Do-Hwan;Kim, Bo-Gyun;Oh, Seong-Tae;Kang, Myung-Joo;Park, Jong-Hyeok;Lee, Jaehwi;Choi, Young-Wook
    • Bulletin of the Korean Chemical Society
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    • v.29 no.4
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    • pp.749-754
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    • 2008
  • To increase the solubility of sibutramine freebase, the solid dispersion was prepared using a fluid-bed granulator. The solid dispersion containing sibutramine freebase was characterized by differential scanning calorimetry (DSC) and powder X-ray diffraction (XRD). After filling the sibutramine solid dispersion in the gelatin hard capsule, we performed in vitro dissolution test, the stability test under accelerated conditions and pharmacokinetic study in beagle dogs. The DSC and XRD data showed that sibutramine solid dispersion would be amorphous state. The dissolution rate of sibutramine solid dispersion was significantly increased about 70% than sibutramine freebase. The stability of sibutramine solid dispersion capsules was equivalent or above to commercial product of sibutramine. In beagle dogs, the sibutramine solid dispersion showed equivalent pharmacokinetic behavior with commercial product of sibutramine hydrochloride. In conclusion, the solid dispersion system provided a possible way to overcome the low solubility of sibutramine freebase, and the sibutramine solid dispersion can be a bioequivalent with the commercial product in humans.

Modeling of Coking Process in a Coke Oven (코크스 공정에서의 열유동 현상 모델링)

  • Yang, Kwang-Heok;Yang, Won;Choi, Sang-Min
    • Proceedings of the KSME Conference
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    • 2004.11a
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    • pp.1184-1189
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    • 2004
  • Coking process is the thermal decomposition of bituminous coal with final temperature of about $900^{\circ}C$ Because coke plays important roles in ironmaking process in a blast furnace it's essential for developing modeling of coke oven. In this study, An unsteady 2-dimesional model is proposed to simulate coking process in a coke oven. In this model, gas and solid phase are assumed homogeneous continnum and solid bed is assumed as porous media . The model contains governing equations for the solid phase and the gas phase. Complicated phenomena such as swelling, softening, resolidification and shrinkage are neglected and mass loss by drying and devolatilization is reflected by generation of internal pores. Drying, devolatilization, heat transfer and generation of internal pores are also reflected in source terms. Calulated results are compared with experimental data

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Performance comparison of acidogenic fermentation and hydrogen fermentation using bench-scale leaching-bed reactors for food waste (벤치스케일 침출상 반응조를 이용한 음식폐기물 처리 시 신발효 및 수소발효의 거동특성 비교)

  • Han, Sun-Ki
    • Journal of the Korea Organic Resources Recycling Association
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    • v.15 no.3
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    • pp.97-105
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    • 2007
  • This study was conducted to compare the performances of acidogenic fermentation and hydrogen fermentation using bench-scale leaching-bed reactors for organic solid waste. Acidogenic fermenters were operated with dilution rates (D) of 2.0, 3.0 and $4.0d^{-1}$ after employing anaerobic sludge and hydrogen fermenters were operated with D of 2.0, 4.0 and $6.0d^{-1}$ after employing heat-treated anaerobic sludge. The highest chemical oxygen demand (COD) conversion efficiency (56.2%) was obtained in acidogenic fermentation with D of $3.0d^{-1}$. Only volatile fatty acid (VFA) was produced as a metabolite. On the other hand, hydrogen fermentation did not show higher COD conversion efficiency (49.3%) than acidogenic fermentation, but it produced hydrogen gas (5.1% of total COD) which was a clean and environmentally friendly fuel with a high energy yield. Therefore, either acidogenic fermentation or hydrogen fermentation could be applied to organic solid waste depending on the purpose of treatment, which could maximize the economics of anaerobic treatment.

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The Characteristics of Elutriation with Gaussian Particle Size Distributions in a gas-solid fluidized bed (기-고 유동층에서 Gaussian 분포 입자군의 표준편차에 따른 유출 특성)

  • Jang, Hyun-Tae;Cha, Wang-Seog
    • Journal of the Korea Academia-Industrial cooperation Society
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    • v.10 no.11
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    • pp.3274-3279
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    • 2009
  • The elutriation characteristics of particle size distribution were investigated in a gas-solid fluidized bed. Experiments were carried out with the mulit-sized particles of Gaussian distributions. The elutriation rate constant obtained from the experiment was correlated with the standard deviation of particle size and the dimensionless group of the velocity ratio. The standard deviation of pressure fluctuation, mean pressure, major frequency and power spectrum density function were calculated by pressure fluctuation properties. Size distribution of elutriated particles and pressure fluctuations were measured for the particle size distribution of particle system depended largrly on the size distribution. Characteristics of fluidization and elutriation were greatly influenced by the particle size distribution and these characteristics could be interpreted with pressure fluctuation properties.

Investigation of flow-regime characteristics in a sloshing pool with mixed-size solid particles

  • Cheng, Songbai;Jin, Wenhui;Qin, Yitong;Zeng, Xiangchu;Wen, Junlang
    • Nuclear Engineering and Technology
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    • v.52 no.5
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    • pp.925-936
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    • 2020
  • To ascertain the characteristics of pool sloshing behavior that might be encountered during a core disruptive accident of sodium-cooled fast reactors, in our earlier work several series of experiments were conducted under various scenarios including the condition with mono-sized solid particles. It is found that under the particle-bed condition, three typical flow regimes (namely the bubble-impulsion dominant regime, the transitional regime and the bed-inertia dominant regime) could be identified and a flow-regime model (base model) has been even successfully established to estimate the regime transition. In this study, aimed to further understand this behavior at more realistic particle-bed conditions, a series of simulated experiments is newly carried out using mixed-size particles. Through analyses, it is verified that for present scenario, by applying the area mean diameter, our previously-developed base model can provide the most appropriate predictive results among the various effective diameters. To predict the regime transition with a form of extension scheme, a correction factor which is based on the volume-mean diameter and the degree of convergence in particle-size distribution is suggested and validated. The conducted analyses in this work also indicate that under certain conditions, the potential separation between different particle components might exist during the sloshing process.

Development of Solid Culture Medium, Bed and Growing Environment Management System for Ginseng Sprout Based on IoT (사물인터넷 기반 새싹삼용 고형배지, 베드 및 생육환경관리시스템 개발)

  • Joo, Nakkeun
    • Journal of the Korea Institute of Information and Communication Engineering
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    • v.25 no.9
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    • pp.1254-1262
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    • 2021
  • Recently, the agricultural environment in Korea is rapidly changing due to the aging and decline of the agricultural population, and in order to solve these problems, it is urgently required to improve the agricultural productivity and reduce the labor force. To solve this problem, a smart farm fused with ICT technology is being proposed as an alternative. In Korea, smart farms are currently mainly used in greenhouses. In this paper, this smart farm technology is to be applied to the cultivation of sprouted ginseng. To this end, we use seedlings (about 1.0g) to grow a solid medium and bed for cultivating sprouted ginseng, a fresh ginseng that is produced in a short period of time (2~3 months) with a clean environment management technology that does not use chemical pesticides and hydroponics in a greenhouse developed. In addition, an IoT-based growth environment management system was developed to monitor the growth process of sprouted ginseng in such an environment and to control driving devices.