• 한국세라믹학회지
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• 제55권2호
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• pp.126-134
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• 2018

Using aqueous solution free radical polymerization with glacial acrylic acid (GAA), maleic anhydride (MA) and sodium methallyl disulfonate (SMADS), a novel linear polycarboxylate dispersant was synthesized for ceramics. Dispersant linear structural characterization was done by FTIR, $^1H$ NMR, HPLC and GPC, and the ratio of monomers was determined using an orthogonal experiment. This research is focused on the effects of polymerization temperature, monomer mole ratios and dosage of initiator on ceramic slurry viscosity with linear polycarboxylate dispersant for ceramic dosage rate of 0.30% (based on dry slurry), all of which were investigated by single factor test. The best polymerization conditions for linear GAA-MA-SMADS are when n(AA) : n(MA) : n(SMADS) equals 3.0 : 1.0 : 0.5, the molecular weight of the polymer is 4600 daltons, the initiator sodium persulfate accounts for 7% of the total mass of polymerized monomers, the polymerization temperature is $90^{\circ}C$ and the reaction time is 2 h. The ceramic body slurry viscosity drops from $820mPa{\cdot}s$ to $46mPa{\cdot}s$ when the concentration of the polycarboxylate dispersant is 0.30%.

• 한국기계가공학회지
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• 제21권2호
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• pp.101-108
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• 2022

Centrifugal pumps are typically used in many slurry industries to transport solid materials. Solid particles in the slurry frequently shock the walls inside the pump, significantly abrading the flow path. Wear damage causes replacement of the pump components, which wastes manpower and time. Therefore, previous studies have been conducted on factors to improve efficiency and life time. This study identifies trends in pumps supplying lime to desulfurized devices from thermal power plants. The shear stress transport(SST) model is used to determine the erosion trend of the centrifugal pump that transfers lime slurry. The purpose of this study is to identify efficiency and erosion trends by selecting three of the various impeller design elements. The three impeller blade design variables mentioned above represent the inlet draft angle and blade angle of leading edge(L.E) and trailing edge(T.E). The maximum value of the erosion density rate tends to be similar to the Input power.

• 대한기계학회논문집B
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• 제21권8호
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• pp.1068-1076
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• 1997

Emission control of acid exhaust gases from coal-fired power plants and waste incinerators has become an increasing concern of both industries and regulators. Among those gaseous emissions, SO$_{2}$ has been eliminated by a Spray Drying Absorber (SDA) system, where the exhaust gas is mixed with atomized limestone-water slurry droplets and then the chemical reaction of SO$_{2}$ with alkaline components of the liquid feed forms sulfates. Liquid atomization is necessary because it maximizes the reaction efficiency by increasing the total surface area of the alkaline components. An experimental study was performed with a laboratory scale SDA to investigate whether the scrubbing efficiency for SO$_{2}$ reduction increased or not with the application of a DC electric field to the limestone-water slurry. For a selected experimental condition SO$_{2}$ concentrations exited from the reactor were measured with various applied voltages and liquid flow rates. The applied voltage varied from -10 to 10 kV by 1 kV, and the volume flow rate of slurry was set to 15, 25, 35 ml/min which were within the range of emission mode. Consequently, the SO$_{2}$ scrubbing efficiency increased with increasing the applied voltage but was independent of the polarity of the applied voltage. For the electrical and flow conditions considered a theoretical study of estimating average size and charge of the atomized droplets was carried out based on the measured current-voltage characteristics. The droplet charge to mass ratio increased and the droplet diameter decreased as the strength of the applied voltage increased.

• Tribology and Lubricants
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• 제27권1호
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• pp.7-12
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• 2011

Interest in advanced machining process such as AJM(abrasive jet machining) and CMP(chemical-mechanical polishing) using micro/nano-sized abrasives has been on the increasing demand due to wide use of super alloys, composites, semiconductor and ceramics, which are difficult to or cannot be processed by traditional machining methods. In this paper, the effects of pressure, wafer moving velocity and fluid viscosity were investigated by 2-dimensional finite element analysis method considering slurry fluid flow. From the investigation, it could be found that the simulation results quite corresponded well to the Preston's equation that describes pressure/velocity dependency on material removal. The result also revealed that the stress and corresponding material removal induced by the collision of particle may decrease under relatively high wafer moving speed due to the slurry flow resistance. In addition, the increase in slurry fluid viscosity causes the reduction of material removal rate. It should be noted that the viscosity effect can vary with the shape of abrasive particle.

• Korea-Australia Rheology Journal
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• 제15권1호
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• pp.19-25
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• 2003

Since the microstructure of functional thin films depends on the dispersion characteristics of dense slurry, it is important to control the agglomerative nature of slurries under processing. The present authors have been discussing the model prediction of agglomerative nature and local rate of agglomeration in dense suspensions. The experiments have been peformed under shear flow using the nearly spherical and oblate type graphite particles. In this study, the experiment has been conducted using water and glycerol as dispersion media. Stress control type rheometer was used to measure the slurry rheology. Local agglomeration of graphite particles has been predicted by using Usui's model. The experimental results show that both the shape and slurry processing method affect on the local dispersion condition. The agglomeration formed by oblate type graphite particles seems to be more difficult to break up than that of spherical particles.

• 한국입자에어로졸학회지
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• 제12권4호
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• pp.145-150
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• 2016

During the chemical mechanical planarization (CMP) process, slurry that comprises abrasive particles can directly affect the CMP performance and quality. Mainly, the large particles in the slurry can generate the defects on the wafer. Thus, many kinds of filters have been used in the CMP process to remove unwanted over-sized particles. Among these filters, the point-of-use (POU) filter is used just before the slurry is supplied onto the CMP pad. In the CMP research field, analysis of the POU filter has been relatively exceptional, and previous studies have not focused on the standardized filtration efficiency (FE) or filter performance. Furthermore, conventional evaluation methods of filter performance are not appropriate for POU filters, as the POU filter is not a membrane type, but is instead a depth type roll filter. In order to accurately evaluate the POU filter, slurry FE according to particle size was measured in this study. Additionally, a CMP experiment was conducted with filtered slurry to demonstrate the effects of filtered slurry on CMP performance. Depending on the flow rate and the filter retention size, the FE according to particle size was different. When the small and large particles have different FEs, the total filtration efficiency (TFE) can still have a similar value. For this reason, there is a need to measure the FE with respect to the particle size to verify the effects of the POU filter on the CMP process.

• KSBB Journal
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• 제14권4호
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• pp.445-451
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• 1999

E. coli TGI/pDG7 $\alpha$ 와 빵효모의 혼합세포계에 의한 글루타치온 생산을 Aerated Slurry Bioreactor에서 수행하였다. 글루타치온 생산 효소는 34시간 동안 안정성을 보였으며, 글루타치온 수율은 4.6 mM을 유지함을 보였다. 고농도의 혼합세포를 이용한 Aerated Slurry Bioreactor에서 기질의 공급속도가 글루타치온 생산에 미치는 영향을 조사하였다. 세포가 회수되어 기질공급속도 5.2 mL/hr에서 글루타치온의 생산농도는 32시간에서 현탁반응보다 낮아짐을 보였고, 반면 세포가 회수되지 않은 기질공급속도 5.2 mL/hr에서는 22시간 동안 유지되었고 2.6 mL/hr에서는 42시간 동안 유지되었다. 글루타치온의 생산성은 기질공급속도가 10.4 mL/hr에서 25.7 mg/g wet $cell{\cdot}hr$이었으나, 2.6 mL/hr에서는 1.65 mg/g wet $cell{\cdot}hr$이었고 5.2mL/hr에서는 5.28 mg/g wet $cell{\cdot}hr$이었다. 계면활성제(Tween 80)을 사용한 경우, 글루타치온 생산시간을 25시간에서 45시간으로 연장되었다. 글루타치온 생산있어 산소가 세포계의 효소에 산소에 의해 영향을 미칠 것으로 판단되었고, 공기를 질소로 교체하여 글루타치온 생산시간을 40시간으로 연장시켰다.

• 한국초전도ㆍ저온공학회논문지
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• 제21권2호
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• pp.26-30
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• 2019

Coal is the most abundant fossil fuel on Earth and is used in a wide range of applications. The direct combustion of high-sulfur coal produces a large amount of sulfur dioxide, which is a toxic and corrosive gas. A new superconducting high gradient magnetic separation (HGMS) technology was studied to remove sulfur from high sulfur coal. The magnetic separation concentrate was obtained under the optimum parameters, such as a particle size of -200 mesh, a magnetic field strength of 2.0 T, a slurry concentration of 15 g/L, and a slurry flow rate of 600 ml/min. The removal rate of sulfur is up to 59.9%. The method uses a magnetic field to remove sulfur-containing magnetic material from a pulverized coal solution. It is simple process with, high efficiency, and is a new way.

• 한국지하수토양환경학회지:지하수토양환경
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• 제6권2호
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• pp.57-67
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• 2001

본 연구는 난지도 매립지에서 기반암 및 풍화대층을 통해서 거동하는 침출수의 속도와 침출수량을 부정류 상태에서 예측하기 위해 실시되었다. 본 연구에서는 3차원 지하수 거동 모델인 MODFLOW와 지하수에 용해되어 있는 오염물질의 확산, 분산, 화학반응 등을 해석할 수 있는 MT3D를 이용하여 안정화 공사 이후 부정류 상태에서 침출수 거동을 해석하였다. 침출수 발생량은 최근 10년간의 기상자료를 이용해서 HELP모델로 산출하였다. 침출수 거동은 차수벽, 차수층 설치 전,후의 침출수위 변화에 의해 예측되었다.

• Journal of Animal Science and Technology
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• 제44권4호
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• pp.459-474
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• 2002

본 연구는 실험방법이 간단하고 분석비요이 저렴하여, 단시간내에 세균수를 측정할 수 있는 현장적용 가능한 방법을 확립하기 위하여 냉장우육의 총균수를 표준평판배양법과 배양온도를 25$^{\circ}C$, 30$^{\circ}C$, 35$^{\circ}C$ 별로 레자주린 환원색과 환원시간을 측정하여 상관관계를 산출하였다. 연구결과를 보면, 총균수(25$^{\circ}C$/72시간, Y)와 레자주린 환원시간(X)과의 상관계수는 RRT(Resazurin reducion test) 배양온도가 25$^{\circ}C$와 30$^{\circ}C$, 환원색은 청색에서 분홍색으로 변할 때가 각각 -0.95와 -0.94로서 가장 높았다. 상관계수와 환원시간을 감안할 때 RRT 배양온도는 30$^{\circ}C$가 적합하였으며, 이때 회귀방정식은 Y=-0.4386X + 7.7870이었으며, 돼지고기의 총균수가 $10^2$, $10^3$, $10^4$ cfu/$cm^2$일 경우 검사시간은 13.2시간, 10.9시간, 8.6시간이었다. 총균수(30$^{\circ}C$/72시간, Y)와 레자주린 환원시간(X)과의 상관계수는 RRT 배양온도가 30$^{\circ}C$, 환원색은 청색에서 분홍색으로 변할 때가 -0.93으로서 가장 높았다. 이때 회귀방정식은 Y=0-0.417X + 7.5540이었으며, 돼지고기의 총균수가 $10^2$, $10^3$, $10^4$ cfu/$cm^2$일 경우 검사시간은 13.3시간, 10.9시간, 8.5시간이었다. 총균수(35$^{\circ}C$/48시간, Y)와 레자주린 환원시간(X)과의 상관계수는 RRT 배양온도가 30$^{\circ}C$, 환원색은 청색에서 분홍색으로 변할 때가 -0.93으로서 가장 높았다. 이때 회귀방정식은 Y=-0.3514X + 6.7513이었으며, 돼지고기의 총균수가 $10^2$, $10^3$, $10^4$ cfu/$cm^2$일 경우 검사시간은 13.5시간, 10.7시간, 7.8시간이었다.