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In industrial crystallization, CSD and mean crystal size as well as external habit and internal structure are important characteristics for further use of the crystals.
The existing solid crystals are also shown to have a non-negligible effect on the slurry flow crystallization systems once the mean crystal size reaches 20 µm.
In industrial crystallization, crystal size distribution and mean crystal size as well as external habit and internal structure are important characteristics for further use of the crystals.
Simplified relation was derived for calculation of mean crystal size of product crystals from the batch cooling crystallizer.
The mean crystal size and the coefficient of variation of an ideal batch crystallizer are derived analytically and it is shown that a batch crystallizer utilizing the proposed control scheme approaches the ideal case.
The mean crystal size and the coefficient of variation (c.v).
Similar(29)
Larger mean crystal sizes were obtained for the following conditions: small amount of added methanol (low level of supersaturation), low temperature, low agitation rates and longer residence time.
The calculated average crystal size of SPION was determined by means of Scherrer's formula, yielding ~16 nm.
The crystallization kinetics and design equations are helpful to calculate the crystallizer residence time and the vessel volume required to achieve a given mean product crystal size.
To check this supposition, a high-pressure study up to 53 GPa of the nanodiamond water suspension with a mean diamond crystal size of 25 nm was done.
The resulting mean ice crystal sizes L* could be estimated from the calculated freezing front velocity (R) and the temperature gradient in the frozen zone (G).
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