2012
DOI: 10.1021/la205131e
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Size-Controlled Flow Synthesis of Gold Nanoparticles Using a Segmented Flow Microfluidic Platform

Abstract: Segmented flow is often used in the synthesis of nanomaterials to achieve narrow particle size distribution. The narrowness of the distribution is commonly attributed to the reduced dispersion associated with segmented flows. On the basis of the analysis of flow fields and the resulting particle size distribution, we demonstrate that it is the slip velocity between the two fluids and internal mixing in the continuous-phase slugs that govern the nature of the particle size distribution. The reduction in the axi… Show more

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Cited by 239 publications
(122 citation statements)
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“…There is an increasing need to produce nanoparticles using inexpensive, rapid, and reproducible methods . The microfluidic technology has a variety of advantages over traditional methods for particle synthesis.…”
Section: Introductionmentioning
confidence: 99%
“…There is an increasing need to produce nanoparticles using inexpensive, rapid, and reproducible methods . The microfluidic technology has a variety of advantages over traditional methods for particle synthesis.…”
Section: Introductionmentioning
confidence: 99%
“…The benefits of microfluidic technology have been extensively discussed in refs. , and and allow the controllable formation of nanoparticle formulations of exceptional homogeneity, including CdS, CdSe, PbS, PbSe, SiO 2 , TiO 2 , Fe 3 O 4 , Pd, Ag, and Au . Amongst this growing list of applications are a small number of studies that report the integration of spectroscopic detection techniques for reaction monitoring and optimization, as well as process automation .…”
Section: Introductionmentioning
confidence: 99%
“…1,2 However, despite the great advantages of small scale technologies compared to batch systems, 3 the applicability of continuous droplet flow chemistry platforms for bi-phasic chemical reactions is limited. 5 As a result, in order to obtain similar and efficient mixing behaviors for different processing times (i.e., residence/reaction time), the length of the reactor has to be adjusted accordingly, resulting in reactor lengths exceeding 20 meters for processes with residence times longer than 20 min (with typical flow reactor inner diameter (ID) B1 mm and flow velocity B1 cm s À1 ). The other challenges associated with continuous multi-phase approaches include droplet-to-droplet communication through the lubrication films surrounding the dispersed phase and solubility of the reagents or products in both phases, limiting the accuracy of the measurements.…”
mentioning
confidence: 99%