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Particle size sensor

Izu, N., Nishizaki, S., Itoh,T., Nishibori, M., Shin, W. and Matsnbara, I. (2009) Gas response, response time and selectivity of a resistive CO sensor based on two connected Ce02 thick films with various particle sizes. Sensors and Actuators B Chemical 136,364-70. [Pg.463]

Fig. 2 HIAC/ROYCO MicroCount 05 (combined light scattering and extinction, single particle sizing sensor)... Fig. 2 HIAC/ROYCO MicroCount 05 (combined light scattering and extinction, single particle sizing sensor)...
A related effect has been described for IR spectroscopy - Surface Enhanced Infrared Absorption spectroscopy (SEIRA). However, as the enhancement factors are significantly lower than for SERS and both the required metal particle size and the activation distance between the target molecule and the particle are more than one order of magnitude smaller, no practically applicable SEIRA sensors have been demonstrated up to now. [Pg.128]

Belt with nucleonic sensor <25 (or <0.3 m3/s) 0.5 to 1 Preferred when material is difficult to handle, e.g. corrosive, hot, dusty, or abrasive. Accuracy greatly improved when particle size, bulk density, and moisture content are constant, when belt load is 70-100 per cent of maximum. [Pg.28]

The basic instrumentation in the present work is a Royco Model 225/518 High Concentration Particle Counter. The location of the air inlet and light sensing unit of the instrument in the card room has been described previously (2). The inlet was fitted with a vertical elutriator preseparator designed to prevent particles >15 vin aerodynamic diameter from entering the light sensor. Thus the collection efficiency of this instrumentation as a function of particle size should be similar to that of the Vertical Elutriator Cotton Dust Sampler. [Pg.124]

Granulation of urea [13] is a complex process that has to be controlled by experienced process operators in order to avoid critical shutdown situations. The parameters most often used for monitoring granulation processes are measured by classical univariate sensors, such as temperature, pressure and flow. However, these standard process measurements carry only little or no relevant information, or are only indirectly related to, for example particle size, clogging of the reactor, or the accumulation of a solids layer on the bottom plate. The response from these sensors often comes with quite a substantial delay time. [Pg.285]

Figure 9.10 PLS-1 model for the average particle size in chambers 2 and 3. Sensors C and D were used in this model based on four PLS components. The model was validated with segmented cross validation with 10 segments. Predicted versus measured (top) and predicted and measured (bottom). Figure 9.10 PLS-1 model for the average particle size in chambers 2 and 3. Sensors C and D were used in this model based on four PLS components. The model was validated with segmented cross validation with 10 segments. Predicted versus measured (top) and predicted and measured (bottom).
There is a wealth of literature on transport and kinetics in microhetero-geneous catalytic systems [175,176], the influence of particle size [177], and complicated situations in which both catalytic microparticles and electron-transfer mediators are dispersed in a polymer matrix [176-179]. The designs and uses of this type of flow-through sensors have been thoroughly reviewed [180,181]. [Pg.147]

Rantanen, J. Rasanen, E. Tenhunen, J. etal, In-line moisture measurement during granulation with a four-wavelength near infrared sensor An evaluation of particle size and binder effects Eur. J. Pharm. Biopharm. 2000, 50, 271-276. [Pg.359]

The available data from emulsion polymerization systems have been obtained almost exclusively through manual, off-line analysis of monomer conversion, emulsifier concentration, particle size, molecular weight, etc. For batch systems this results in a large expenditure of time in order to sample with sufficient frequency to accurately observe the system kinetics. In continuous systems a large number of samples are required to observe interesting system dynamics such as multiple steady states or limit cycles. In addition, feedback control of any process variable other than temperature or pressure is impossible without specialized on-line sensors. This note describes the initial stages of development of two such sensors, (one for the monitoring of reactor conversion and the other for the continuous measurement of surface tension), and their implementation as part of a computer data acquisition system for the emulsion polymerization of methyl methacrylate. [Pg.500]

In any case, the ability to tune their luminescence characteristics by particle size control, combined with relatively high quantum yields, narrow fluorescence emission, very broad absorption spectra and photostability provide new solutions to many of the problems associated with traditional luminescence sensors and hold a strong promise for a completely new set of analytical applications with QDs.18... [Pg.381]


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