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To demonstrate the merit of unique structure for the fast mass transfer, sensor based on SnO2 products has been fabricated and the results exhibit excellent sensing performances for toluene detection.
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Among the techniques presented, mass transfer of material to a sensor embedded in a surface is demonstrated to be useful in the further exploration of ultrasonic cleaning of high aspect ratio micropores.
Even though the optode at the tip of the rotating flexitube optical sensor blocks the mass transfer of oxygen at this point, this blockage is insignificant.
The novel nanostructure significantly increases the surface area and mass transfer rate, which improves the biochemical binding effect and sensor signal to noise ratio.
Important design issues for a microreactor, specifically heat and mass transfer, are explored with the design of a micro-flow sensor and the redesign of the reactor heater.
Compared to this area, the rotating flexitube optical sensor system merely blocks 0.77% of the total mass transfer area and, thus, can be disregarded.
This delay arises from the slow mass transfer of glucose from the vasculature to the tissue and ultimately the sensor.
Theoretical approaches demonstrate efficient and uniform mass transfer of the analyte from the bulk flow to small-scale affinity sensors in the base of fluidic channels by (i) active control of the analyte flow speed over the affinity sensor, (ii) non-rectangular channel geometries and (iii) non-uniform distributions of recognition binding sites over the active area of the sensor.
This delay was determined at ∼5 min and used to correct sensor data on each day for the physiological time lag that characterizes mass transfer of glucose from blood to tissue.
The mean liquid saturation and the liquid solid mass transfer rate were determined using classical electrochemical techniques and the local instantaneous hydrodynamics were analyzed using electrochemical shear rate sensors.
Mass transfer coefficient (m/s).
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