Circulation of components during microfluidization and/or homogenization of emulsions
a technology of emulsion and microfluidization, which is applied in the direction of antibody medical ingredients, transportation and packaging, rotary stirring mixers, etc., can solve the problems of emulsion degradation during storag
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example 1
[0208]The emulsion components squalene, polysorbate 80, sorbitan trioleate and sodium citrate buffer were introduced into an in-line, high speed, rotor / stator homogenizer (IKA Super Dispax Reactor DRS 2000 / 5). Emulsion starting volumes of 280 L and 250 L were used and the speed of the homogenizer was set at 5000±1000 rpm. The temperature of the emulsion during homogenization was maintained at below 60° C.
[0209]Three test runs were carried out. In the first test run, 280 L of the emulsion components were subject to type I circulation, between the homogenizer and a first premix container, for 20 minutes followed by a single type II circulation, transferring the first emulsion components from a first premix stainless steel container, through the homogenizer to a second premix stainless steel container, and then back through the homogenizer. In the second test run, 280 L of the emulsion components were subjected to type I circulation, between the homogenizer and a first premix stainless...
example 2
[0216]In further experiments a first emulsion was formed by type I (FIG. 5) or type II (FIG. 6) circulation. For five separate runs the average number of larges particles per ml was as follows:
Coefficient ofMeanvariationType I1.70 × 1090.23Type II1.04 × 1090.13
[0217]Thus the type II circulation results in fewer large droplets and less batch-to-batch variation.
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