diafiltration system and diafiltration method
A technology of percolation and permeate, applied in the field of percolation system, which can solve problems such as the decrease of electrical conductivity
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example 1
[0056] This example demonstrates that, in accordance with an embodiment of the present invention, with controlled percolation fluid flow (in each channel), from a The feed stream achieved 99% (2-log; NDV=7) removal of impurities.
[0057] The diafiltration system is configured to include a fluid treatment assembly generally as shown in FIG. 4 (A and B), wherein the diafiltration pump and diafiltration system are configured substantially as Figure 1A and 1C Shown in, includes MASTERFLEX L / S Precision Variable Speed Pump Driver (Model: EW-07528-30), and three MASTERFLEX L / S Multi-Channel Pump Heads (Model: 07536-002) and MASTERFLEX L / S High Performance Precision 2-stop tube set (L / S 15, 06421-15) (Cole-Palmer Instrument Company, Vernon Hills, IL).
[0058] The fluid processing module has 6 stages, each stage has 2 cross-flow processing modules in series, each cross-flow processing module includes Delta regenerated cellulose UF membranes, each membrane has a cutoff of 30kDA a...
example 2
[0066]This example demonstrates that, in accordance with an embodiment of the present invention, with controlled percolation fluid flow (in each channel), from a The feed stream achieved 99.9% (3-log; NDV=13) removal of impurities.
[0067] The diafiltration system, fluid treatment components, and feed and DF solutions were as described in Example 1.
[0068] When the feed fluid flow rate is 5mL / min, the percolation fluid flow rate in each channel is about 10.8mL / min, and when the feed fluid flow rate is 10mL / min, the percolation fluid flow rate in each channel is about 22.7mL / min.
[0069] By employing retentate throttling, an approximately 1:1 ratio between feed flow and retentate flow is maintained.
[0070] The result is as follows:
[0071] For a feed fluid flow rate of 5 mL / min, for DF stages 1-6, the flow distribution of each DF stage remained substantially uniform at around 10 mL / min. The pressures for DF grades 1 and 2 were 15 psig and 17 psig respectively, the pr...
example 3
[0075] This example demonstrates that impurity is achieved from a feed stream having a fluid flow rate of 5 mL / min with the percolation fluid flow rate (in each channel) controlled to be about 18.3 mL / min according to one embodiment of the present invention. 99.99% (4-log; NDV=22) of was removed.
[0076] The diafiltration system, fluid treatment components, and feed and DF solutions were as described in Example 1.
[0077] By employing retentate throttling, an approximately 1:1 ratio between feed flow and retentate flow is maintained.
[0078] The result is as follows:
[0079] For DF stages 1-6, the flow profile of each DF stage was kept in the range of about 8-12 mL / min. The pressure profile varied from about 34 psig for DF stage 1 to about 26 psig for DF stage 6 (down about 1 to 2 psig per stage towards the retentate outlet).
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Abstract
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