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The applied feed gas composition closely resembles real exhaust conditions under dynamic operation.
At an applied feed pressure of 10 bar, fructose rejection was found to be 94.14, 60.2 and 98.7% for FPA-150, FPA-250 and RO membranes, respectively.
The incidence of gaping was low across feed treatments, and gaping scores were not correlated to fillet firmness nor influenced by the applied feed or feeding regime over the experiment.
The applied feed streams were deionized water and microfiltered fermentation broth, containing the desired product, sodium lactate.
The pressure loss originates from the structural change of the polymer thin layer membrane material, which is being compressed in a dense form by the applied feed pressure of the feed stream.
Hence, in the present case, the applied feed pressure in the range of 60 70 bar is expected to significantly reduce osmotic backwash flux, as is quite evident from the obtained results.
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However, all of these studies applied feeding of expensive precursors, such as p-coumaric acid10,11,12,13,14,15, tyrosine15,16,17 or phenylalanine18.
Aim of the presented study was the development of a procedure for the analytical differentiation of cow milk according to the applied feeding system origin.
This inconsistency may be due to strain background (Ramon et al. 2007), gene dosage of foreign proteins (Ramon et al. 2007), or the specific applied feeding strategy (Celik et al. 2009), and the underlying mechanisms remain to be elucidated.
Fig. 1 shows the incidence of milk fever obtained in experiments applying feed with different DCAD.
For example, we have noted earlier the possibility of applying feed optimization schemes to condition data ordering.
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