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Particle size distribution of the as-received raw powder and the ballmilled and microfluidized slurries. Microfluidization was repeated one time and 10 times, which produced a marginal difference in the distribution curves. 

Particle size distribution of the as-received raw powder and the ballmilled and microfluidized slurries. Microfluidization was repeated one time and 10 times, which produced a marginal difference in the distribution curves. 

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In this study, a transparent magnesium aluminate (MgAl2O4) spinel prepared by homogeneous green compaction and sinter-HIP processes was investigated. The uniformity of the particle configuration in a green body could be improved by both a wet shaping via slip casting and a microfluidization process, which effectively disintegrates particle agglomer...

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... particle size distribution of the MgAl 2 O 4 slurry after ball milling and microfluidization is shown in Fig. 2; for comparison, the particle size distribution of the as-received powder is also analyzed. As shown in Fig. 2, the as-received raw powder primarily consisted of several micron-sized agglomerates due to its high specific surface area and large van der Waals attraction. Pulverized by ball milling, the particles in the slurry showed a ...
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... particle size distribution of the MgAl 2 O 4 slurry after ball milling and microfluidization is shown in Fig. 2; for comparison, the particle size distribution of the as-received powder is also analyzed. As shown in Fig. 2, the as-received raw powder primarily consisted of several micron-sized agglomerates due to its high specific surface area and large van der Waals attraction. Pulverized by ball milling, the particles in the slurry showed a significant decrease in the mean particle size from 2.73 μm to 0.195 μm; however, the slurry still contained ...
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... the slurry still contained micron-sized agglomerates, which was exhibited in the particle size distribution curve as three peaks at 0.140 μm, 0.238 μm and 1.87 μm. Conversely, the micro- fluidized slurry showed a unimodal particle size distribution with a lower mean particle size (0.150 μm) without any micron-sized agglomerates. Additionally, Fig. 2 clearly shows that only 1 pass of the slurry through the microfluidizer is sufficient to fully disintegrate the agglomerates, which is accomplished within a few minutes. In this regard, micro- fluidization is shown to be a powerful process for the disintegration of large agglomerates in a nano-powder. The forces introduced for ...
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... increased with time for both slurries, but the viscosity of the ball-milled slurry increased more rapidly with a 58% steeper slope compared to the slope of the microfluidized slurry. While a lower viscosity indicates a weaker interparticle network and less flocculation in the as- milled or as-passed slurry, which agrees with the results of Fig. 2, the slower aging rate can be interpreted as a higher resistivity against re-flocculation and re-coagulation. Recently, Kadosh et al. reported the microstructure of a suspension directly observed by cryo-SEM and showed that a high level of flocculation and inhomogeneous void formations were pro- moted by aging for 30 min; this ...
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... particle size distribution of the MgAl 2 O 4 slurry after ball milling and microfluidization is shown in Fig. 2; for comparison, the particle size distribution of the as-received powder is also analyzed. As shown in Fig. 2, the as-received raw powder primarily consisted of several micron-sized agglomerates due to its high specific surface area and large van der Waals attraction. Pulverized by ball milling, the particles in the slurry showed a significant decrease in the mean particle size from 2.73 μm to 0.195 μm; however, the slurry still contained micron-sized agglomerates, which was exhibited in the particle size distribution curve as three peaks at 0.140 μm, 0.238 μm and 1.87 μm. Conversely, the micro- fluidized slurry showed a unimodal particle size distribution with a lower mean particle size (0.150 μm) without any micron-sized agglomerates. Additionally, Fig. 2 clearly shows that only 1 pass of the slurry through the microfluidizer is sufficient to fully disintegrate the agglomerates, which is accomplished within a few minutes. In this regard, micro- fluidization is shown to be a powerful process for the disintegration of large agglomerates in a nano-powder. The forces introduced for disintegration during microfluidization include a high shear stress applied through the narrow channel and also the cavitation phenomenon that can occur when the slurry passes out of the narrow channel into the connected wider tube. To et al. reported that the rapid expansion of a high-pressure suspension, such as cavitation, is effective at deagglomerating nanoparticle aggregates [25]. Therefore, it is reasonable to conclude that both the high shear stress and the strong cavitation in the proposed process improved the resulting deagglomeration of the MgAl 2 O 4 ...
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... particle size distribution of the MgAl 2 O 4 slurry after ball milling and microfluidization is shown in Fig. 2; for comparison, the particle size distribution of the as-received powder is also analyzed. As shown in Fig. 2, the as-received raw powder primarily consisted of several micron-sized agglomerates due to its high specific surface area and large van der Waals attraction. Pulverized by ball milling, the particles in the slurry showed a significant decrease in the mean particle size from 2.73 μm to 0.195 μm; however, the slurry still contained micron-sized agglomerates, which was exhibited in the particle size distribution curve as three peaks at 0.140 μm, 0.238 μm and 1.87 μm. Conversely, the micro- fluidized slurry showed a unimodal particle size distribution with a lower mean particle size (0.150 μm) without any micron-sized agglomerates. Additionally, Fig. 2 clearly shows that only 1 pass of the slurry through the microfluidizer is sufficient to fully disintegrate the agglomerates, which is accomplished within a few minutes. In this regard, micro- fluidization is shown to be a powerful process for the disintegration of large agglomerates in a nano-powder. The forces introduced for disintegration during microfluidization include a high shear stress applied through the narrow channel and also the cavitation phenomenon that can occur when the slurry passes out of the narrow channel into the connected wider tube. To et al. reported that the rapid expansion of a high-pressure suspension, such as cavitation, is effective at deagglomerating nanoparticle aggregates [25]. Therefore, it is reasonable to conclude that both the high shear stress and the strong cavitation in the proposed process improved the resulting deagglomeration of the MgAl 2 O 4 ...
Context 7
... particle size distribution of the MgAl 2 O 4 slurry after ball milling and microfluidization is shown in Fig. 2; for comparison, the particle size distribution of the as-received powder is also analyzed. As shown in Fig. 2, the as-received raw powder primarily consisted of several micron-sized agglomerates due to its high specific surface area and large van der Waals attraction. Pulverized by ball milling, the particles in the slurry showed a significant decrease in the mean particle size from 2.73 μm to 0.195 μm; however, the slurry still contained micron-sized agglomerates, which was exhibited in the particle size distribution curve as three peaks at 0.140 μm, 0.238 μm and 1.87 μm. Conversely, the micro- fluidized slurry showed a unimodal particle size distribution with a lower mean particle size (0.150 μm) without any micron-sized agglomerates. Additionally, Fig. 2 clearly shows that only 1 pass of the slurry through the microfluidizer is sufficient to fully disintegrate the agglomerates, which is accomplished within a few minutes. In this regard, micro- fluidization is shown to be a powerful process for the disintegration of large agglomerates in a nano-powder. The forces introduced for disintegration during microfluidization include a high shear stress applied through the narrow channel and also the cavitation phenomenon that can occur when the slurry passes out of the narrow channel into the connected wider tube. To et al. reported that the rapid expansion of a high-pressure suspension, such as cavitation, is effective at deagglomerating nanoparticle aggregates [25]. Therefore, it is reasonable to conclude that both the high shear stress and the strong cavitation in the proposed process improved the resulting deagglomeration of the MgAl 2 O 4 ...
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... analysis was conducted on the slurry that passed through the channel 10 times to check for any contamination created during microfluidization; these results are summarized in Table 1. It was found that no impurity inflow or contamina- tion from the fluidizing line had occurred comparing the ball- milled slurry to the microfluidized slurry. When deagglomera- tion is promoted by high-energy milling, impurity contamina- tion due to the abrasion of the milling media and the container is typically unavoidable; however, microfluidization is oper- ated without a milling media and only requires passing the slurry through a narrow channel made by single crystal diamond, allowing a high purity and the resulting composition of MgAl 2 O 4 to be maintained. Fig. 3 shows the rheological properties of the ball-milled and microfluidized slurries. The viscosity versus the shear rate profiles in Fig. 3(a) show that both slurries exhibited a non- Newtonian shear-thinning behavior, which decreases the viscosity as the shear rate increases; however, after reaching a steady viscosity at a sufficiently high shear rate, the viscosity of the microfluidized slurry showed was nearly half of that of the ball-milled slurry. In Fig. 3(b), the time-dependent viscosity profile of the slurries at a constant shear rate (30 s À 1 ) shows that the viscosity increased with time for both slurries, but the viscosity of the ball-milled slurry increased more rapidly with a 58% steeper slope compared to the slope of the microfluidized slurry. While a lower viscosity indicates a weaker interparticle network and less flocculation in the as- milled or as-passed slurry, which agrees with the results of Fig. 2, the slower aging rate can be interpreted as a higher resistivity against re-flocculation and re-coagulation. Recently, Kadosh et al. reported the microstructure of a suspension directly observed by cryo-SEM and showed that a high level of flocculation and inhomogeneous void formations were pro- moted by aging for 30 min; this phenomenon was shown to be caused by an increase of attractive force between particles with time [26]. It is thus inferred that the homogeneous, mono-sized particle distribution in the microfluidized slurry contributed to the higher stability of the slurry by maximizing the average interparticle distance and weakening the resistance of the flow of the suspension against the external shear force. In addition, Hotta et al. reported that microfluidization enhances the electrostatic repulsion between the particles without degrading the dispersant or the particle surface and enhances the steric repulsion by increasing the average polymer molecular weight and length, which increases the interparticle distance and slurry stability [20]. Fig. 4 shows the pore size distribution in the green compacts that were fabricated with varying slurry conditions and consolidation methods; the nomenclature and data of these conditions and methods are summarized in Table 2. The slip- casted body from the microfluidized slurry (MF) showed a narrower pore size distribution with the smaller mean pore size of 25.6 nm compared with the green body prepared from the ball-milled slurry (BM) which displayed a wider distribution with larger mean pore size (28.3 nm). In addition, the green density of MF was higher than that of BM, attributed to the smaller mean pore size in the green compact. It is considered that a narrower particle size distribution without micron-sized agglomerate of microfluidized slurry enabled more uniform and homogeneous particle coordination in the MF green body. Moreover, the higher stability of the microfluidized slurry against re-flocculation which was shown in Fig. 3 is thought to influence the narrow pore size formation during slip casting process that requires a prolonged casting time which may allow the particles to aggregate again. On the other hand, the green bodies fabricated by uniaxial dry pressing of freeze-granules prepared from the ball-milled slurry and microfluidized slurry (DP(BM) and DP(MF), respectively) followed by CIP at 200 MPa showed an overall larger and wider pore size distribution compared to that of the slip-casted specimen, resulting in lower green densities in Table 2. The conditions used here for pressing were not optimal so that the results do not represent the best values attainable by pressing. It was shown by Goldstein et al. [11] and Krell et al. [12] that dry pressing of granules with optimal conditions (i.e. solid loading, solvent, binder, granulation method and CIP schedule) can give a uniform green compact comparable to slip-casted bodies in this study. Nevertheless, it is interesting that when dry pressing was used as a consolida- tion method, the characteristics of the different slurry prepara- tions were shown to marginally affect the properties of the resulting green body; however, using a wet shaping process allowed prominent improvement to the homogeneity of the green compact with respect to different slurry preparation methods. It is inferred that the disintegrating effect of micro- fluidization was readily exploited in slip-casting in absence of a drying process which might cause flocculation or agglom- eration. Thus, the remaining part of the study will only discuss the slip-casted compacts, not dry pressed samples in order to observe the effects of microfluidization and pore size Table 2, and the cumulative distributions were found to fit the cumulative Gaussian distribution function well. distribution of the green body to sintering behavior and optical ...

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Thesis
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