For the synthesis of the core-shell nanoparticles, iron oxide nanoparticles were firstly synthesized within the droplets of the reactor, as previously described24 (link),34 (link). Briefly, through the first two fused silica capillaries of the reactor, two aqueous solutions were injected at a flow rate of 10 µL/min. The first solution was 0.06 M of FeCl3·6H2O (Alfa Aesar, USA) and 0.03 M of FeCl2∙4H2O (Sigma-Aldrich, USA) dissolved in DI water, and the second solution was 4 M ammonia (Alfa Aesar, USA). As a continuous phase mineral oil (M5904, Sigma-Aldrich USA) with 0.075 vol % Triton X-100 (Samchun Chemical, Korea) and 1.75 vol % Abil EM 90 (Evonik Industrial, Germany) was used, the flowrate injected through the central Tygon tubing was 10 µL/min. For the synthesis of the gold shell around the iron cores, a gold precursor solution was injected into the existing droplets through the single capillaries at 100, 130, and 160 cm. The gold precursor solution consisted of 0.03 M HAuCl4 (Sigma-Aldrich USA) dissolved in DI water. For all three injections, the same flowrate was used and flowrate was determined by a self-optimizing algorithm based on the transmission of the droplets and two initial guesses for the flowrate. To quench the reaction, core-shell nanoparticles were collected in a vial filled with water, once they left the capillary droplet reactor.
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