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1 hat is 6 orders of magnitude larger than the particle size.
2 whether microorganisms prefer to adhere to a particle size.
3 ld spikes and using minor proteins to define particle size.
4 glycol and drug formulation, on the aerosol particle size.
5 rface area, structural anisotropy, and small particle size.
6 lysis rate decreased with increasing mineral particle size.
7 avior of spinel ZnFe(2)O(4) as a function of particle size.
8 eased with the number of injections and with particle size.
9 icted, translating into an overestimation of particle size.
10 e than with PAC, likely due to the increased particle size.
11 ignificantly (p < 0.05) increased the powder particle size.
12 overage attaining values comparable with the particle size.
13 in new form factors, especially in terms of particle size.
14 ng and separation efficiency of the specific particle sizes.
15 devices only work well for a narrow range of particle sizes.
16 le size, being lower in samples with smaller particle sizes.
17 -RE nanoalloys with tunable compositions and particle sizes.
18 90% and did not strikingly alter the median particles size.
19 onsistent flow rates entering NTA for proper particle sizing.
20 s by monitoring the associated change in the particles' size.
21 ee trunk), food shape (cuboid or flattened), particle sizes (0.45-1, 1-2, 2-3, or 3-4 mm), and placem
23 lation of GEOs in water-based microemulsion (particle size 10.1nm) showed better antimicrobial activi
25 mum conditions were: steaming time 4.36 min, particle size 23 mm, time from harvesting to steaming 2
28 (diameter 18-26 nm) (-0.02 SD LDL defined by particle size; 95% CI: -0.10 to 0.05 for CETP versus -0.
29 etallic NPs (Pt(3) M/rGO-HF) with ultrasmall particle size (about 3 nm) and dramatic monodispersity.
31 (3) M intermetallic NPs exhibit the smallest particle size among the reported ordered Pt-based interm
34 aph, X-ray photoelectron spectroscopy (XPS), particle size analysis, and fluorescence spectrum (FL) a
35 s have an identical Pt loading, similar Beta particle size and acidity, but different internal struct
39 on of supported metal catalysts with uniform particle size and coordination environment is a challeng
40 cal power absorption and is also affected by particle size and corresponding particle suspension heig
42 we speculate on the observed differences in particle size and density that we found between young pa
44 particulate organic carbon, depending on the particle size and filtration method, and overlook its re
45 in consumer products, there is evidence that particle size and formulation influences skin permeabili
49 ryo-SEM results further showed a decrease in particle size and loss of internal "polyhedral" structur
52 pability was found through the match between particle size and pillar spacing, being consistent with
54 ysisorption yields quantitative agreement in particle size and qualitative agreement in average speci
56 roscope (DHM) enabling determination of both particle size and RI of individual subwavelength particl
60 conventional vapor-phase deposition, and the particle size and structural uniformity enable comparati
62 operties (such as pore size, total porosity, particle size and surface distribution of peptide on the
63 ly involves a tedious sequence that controls particle size and surface properties in separate steps.
68 ides having different crystal structures and particle sizes and measured the power densities they pro
70 pure, homogeneous nanomaterial preparations, particle sizing and counting remains difficult for heter
75 es relationships among the refractive index, particle size, and pattern both numerically and experime
77 The spatial distribution, concentration, particle size, and polymer compositions of microplastics
78 The cross-linking density, external load, particle size, and repeatability of energy recoverabilit
80 found that the applied current, the CaCO(3) particle size, and the feed rate affect the removal of p
82 erview of the state of the art morphologies, particle sizes, and optical properties of YAG:Ce on the
85 he most effective factors for tuning droplet/particle sizes are PLGA concentrations and the flow rate
86 lms: more than 1100 particles mum(-2) with a particle size as small as ~5 nm can be achieved via stra
87 cle counting and EBC was calculated for each particle size as well as the cut-off points that optimiz
88 to different Co(3)O(4) catalyst loadings and particle sizes as well as the mixed Ag + Co(3)O(4) catal
89 NPs) system capable of exhibiting different particle size at different temperature was developed, wh
90 related to the lipid type but rather to the particle size, being lower in samples with smaller parti
91 rmulated microparticles had a mean geometric particle size between 2 and 5 mum, entrapment efficiency
92 ntical physical characteristics to determine particle size but differ in the weighting of the distrib
93 of micellization and subsequent evolution in particle size can be studied when preparing PGMA(29)-PMO
94 varied according to bean genotype and powder particle size: coarse powders resulted in larger (+26%)
96 Optimisation of the stationary phase nature, particle size, column length and internal diameter, as w
97 P = 0.0008, respectively) and increased LDL particle size compared with the milk diet (P = 0.02).
98 pulation, porosity increases with increasing particle size, consistent with the proposed UMN growth m
99 Mn-O stretching Raman bands also varied with particle size, consistent with the ratio of edge to bulk
100 ) concentration, relative humidity (RH), and particle size control reaction rates and mechanisms.
102 H) to increase membrane selectivity, and the particle size cutoff was reduced from 35 to 10 nm post-t
108 perimental results revealed that the average particle size diameter of Horse chestnut starch nanopart
109 cholesterol concentrations in LDL defined by particle size (diameter 18-26 nm) (-0.02 SD LDL defined
110 NP had an average diameter of 210 nm, narrow particle size distribution (polydispersity index ~0.1),
113 Field measurements of the time-resolved particle size distribution (PSD) in a typical room envir
116 The steady-state current scales with the particle size distribution and is limited by the diffusi
117 ules were also additionally analyzed for the particle size distribution and morphological characteriz
119 pproach of incremental complexity to measure particle size distribution and size stability of NEPs, c
120 s into both the average mass of a structured particle size distribution and the average hydrodynamic
121 uences of the soiling of PV modules from the particle size distribution and the cleanliness value.
123 cle tracking analysis, with the variation in particle size distribution being used to determine the r
127 d not differ in terms of dry matter content, particle size distribution or rheological properties.
128 EP assessment, including the measurements of particle size distribution, and are offering wide access
129 o simultaneously determine EV concentration, particle size distribution, and surface immunophenotype.
130 ization function, relative particle density, particle size distribution, and water column density str
131 dictated by an interplay between the aerosol particle size distribution, composition, water availabil
135 the formulations in terms of particle size, particle size distribution, product yield, entrapment ef
136 ticle sizer to measure the time evolution of particle size distribution, which was used to calculate
137 mplexes were studied by measuring turbidity, particle size distribution, zeta-potential, as well as s
141 ws unbiased fitting of the information-laden particle-size distribution (PSD) including its shape.
142 dy modelled the effects of discretization of particles size distribution on sediment deposition and p
143 , the effect of rapid cooling on the silicon particle size, distribution, and morphology of hypereute
144 ing microencapsulation was characterized by: particle size/distribution (span), morphology, drug/gela
145 -gas concentration ratios also depend on the particle size distributions and aerosol loadings in the
146 ch sediments, which differ slightly in their particle size distributions and morphologies but exhibit
148 locity technique that allows us to determine particle size distributions while accounting for colloid
149 te not only important 1D distributions, i.e. particle size distributions, but also nanoparticle struc
152 n were characterized in terms of morphology, particle size, drug encapsulation efficiency, in vitro r
155 spectra (mu(s)') were found less useful for particle size estimation as they lack a characteristic s
156 nutraceutical whereas flours with a smaller particle size (F3 and F4) are more interesting as functi
157 tion, neutralization kept a stable colloidal particle size for pHs decreased to pH 9,8 and 7; however
158 rce-to-receiver distance, printer positions, particle size fraction, and environmental diffusivity es
159 l, and cobalt) were synthesized with average particle sizes from 0.9 to 1.4 nanometers, with tight si
162 cording to this, microplastics in detectable particle sizes (>100 mum) are only found on the surface
164 ring microfluidisation resulted in a smaller particle size, higher WRC and extractability, and an inc
165 d high-density lipoprotein, small and medium particle size (HMSP), GlycA, LP-IR, short-chain dicarbox
166 , a greater porosity, lower agglomerates and particle size, improve the Ca solubility in the intestin
168 1, the Just Noticeable Difference (JND) for particle size in melted chocolate was ~5 mum in a partic
169 egrees C, protein surface hydrophobicity and particle size increased and alpha helical structure decr
170 stributions along a continuum of behavior as particle size increases and slopes get steeper and/or sm
174 e observed effect to be general and that the particle size is the single most important factor govern
175 to control samples, heat treatment increased particle size, light absorbance, centrifugal instability
177 ula: see text] describes the degree to which particle size lowers the melting point and is found to v
185 size) on important properties of wheat bran (particle size, microstructure, chemical composition, wat
186 on microscopy that enables the corresponding particle size, morphology, crystallinity, and other fact
187 The key parameters essential for tailoring particle size, morphology, porosity, acid-base, and redo
188 cles with identical compositions but varying particle size, morphology, stabilizer chain length, and
189 ormulation was characterized with respect to particle size, morphology, surface charge and singlet ox
192 ferent composites was 10 to 224 uM for a BAG particle size of <5 to 150 um in the presence of artific
195 ticles by solvent evaporation, with the mean particle size of 122.0 +/- 2.28 nm and drug loading of 3
196 by solvent evaporation, resulting in a mean particle size of 125.6 +/- 2.3 nm and drug loading of 10
198 Tungsten disulfide (WS(2)) with an average particle size of 2 mum was found to increase the sensiti
200 -TEM revealed an average core metallocorrole particle size of 32 nm, with protein tendrils extending
202 ated nanoparticles (ApoE-NPs), with the mean particle size of 64 nm and drug loading of 10% (w/w).
203 at a N:P ratio of 6 demonstrated an average particle size of 76.6nm with a zeta potential of +16.5mV
204 (PLGA) microspheres (Sunb-malate MS) with a particle size of approximately 15 mum and a drug loading
205 Ejecta with a size much larger than the mean particle size of feedstock powder have been observed in
212 om the moderately alkaline pH and very small particle size of the burial soil, in addition to bronze
215 r and gas interaction and the mineralogy and particle size of the slag are the main factors that have
217 ions, 5FU-SLN(4) was the most effective with particle size of was 263 +/- 3 nm, zeta potential was 0.
218 and maize starch (QR and MR) showed average particle sizes of 107 and 222 nm, encapsulation efficien
219 pants, two solid commercial chocolates (with particle sizes of 19 and 26 mum; i.e., just above the JN
221 ructural elements of FeN(4) sites, including particle sizes of catalysts, Fe content, and Fe-N bond s
224 of this work was to determine the effect of particle sizes of Prosopis flour on its chemical composi
225 oyed to encapsulate the chlorophyll, and the particles size of the composites was controlled through
229 resence of water increase monotonically with particle size on Pt-rich catalysts, suggesting that the
230 red plastic debris and the impact of plastic particle size on removal remain largely unexplored.
231 nce of viscosity to predict the influence of particle size on the glass transition temperature and vi
233 ticles with different shapes, densities, and particle sizes on different sediment beds were experimen
234 er of passes, bran concentration and initial particle size) on important properties of wheat bran (pa
237 interaction between particles by increasing particle size or external field strength leads to a pref
238 this interaction becomes stronger at reduced particle size or, equivalently, with increased surface t
239 l properties of the formulations in terms of particle size, particle size distribution, product yield
240 iculate complexants, and their dependence on particle size, particle type (i.e., reactive sites distr
242 butions showed coherent unimodal and bimodal particle size populations isolated via centrifugation an
243 critical physicochemical properties (such as particle size, porosity, average pore diameter, and drug
244 ) models that are capable of predicting PLGA particle sizes produced by different microfluidic system
245 model eventually allowed rapid prediction of particle sizes produced using various microfluidic syste
246 ion (~10 um) for samples with larger initial particle sizes proved crucial in improving signal stabil
247 cle size in melted chocolate was ~5 mum in a particle size range commonly found in commercial chocola
251 as achieved by a jet mill and flours (JF) of particle size, ranged from 17 to 84 mum, were used.
252 a of polystyrene suspensions, with a nominal particle size ranging from 0.1 to 12 mum in diameter.
254 s of different alloy phases depending on PAE particle size ratio, DNA surface coverage, stoichiometri
259 t high space velocity in the literature, the particle-size-resolved fresh filtration efficiency of se
260 urfaces have identified features such as the particle size, shape and surface charge to influence the
262 ential information to proper risk assessment-particle size, shape, and chemical composition have to b
263 les can change significantly with changes in particle size, shape, composition, and arrangement.
264 and reliable method for the determination of particle sizes, shapes, and numbers is missing, as exist
268 color degradation was better associated with particle size than conjugation and was lowest for PPI-st
269 reated casein aggregates of larger colloidal particle size than primary casein micelle in control MPI
273 microfluidisation reduced wheat bran median particle size to 14.8 mum and disintegrated starch granu
275 ass transport in the electric field, enables particle size to be estimated and explains the feasibili
280 e-shell yields exceeding 99%, tuning the MOF particle size via the solution concentration of AuNRs.
287 nanoparticle tracking analysis and a larger particle size was observed for the oxidized treatment.
291 Both alpha-Al dendrites and the silicon particle sizes were significantly reduced from micron to
292 eved a controlled aggregation with different particle size, which gives a series of different antibac
293 erical geometry progressively increased with particle size, which is consistent with the interpretati
294 -bound carbonyls) and aggregation (increased particle size); while subsequent wet heating induced par
295 sed gas velocity, particle concentration and particle size will exacerbate the erosion and wear rate
296 ictive particle trapping for three different particle sizes (with an estimation error < 10%, not usin
298 ed as a synthetic handle to directly control particle size, with potential implications for industria
299 ysicochemical properties such as morphology, particle size, zeta potential, pGFP encapsulation effici