Systems and methods using multiple solvents for the removal of lipids from fluids
a technology of fluids and solvents, applied in the field of systems, apparatuses and methods for the removal of lipids from fluids, can solve the problems of lipid-protein structure, insoluble lipid particles, and inability to remove lipids from fluids, and achieve the effect of reducing the amount of tim
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first embodiment
A. FIRST EMBODIMENT
1. Initial Phase Subsystem
FIG. 2 shows a delipidation system 10 composed of an initial phase subsystem 12 and an intermediate phase subsystem 14, and FIGS. 9 and 10 show two embodiments of a final phase subsystem 16. Referring to FIG. 2, initial phase subsystem 12 is formed with a HFC 18. While the embodiment depicted in FIG. 2, shows a single HFC, the initial phase subsystem 12 is not limited to a single HFC but may include additional HFCs. The number of HFCs used in each subsystem may be dictated by the amount of lipid removal desired. The number and size of the HFCs are a function of the flow rate of fluids or gases within, the lumens of the hollow fibers and on the shell side of the hollow fibers of the HFC, the porosity of the hollow fibers, and the amount of surface area of the hollow fiber membrane. Adjusting one of these factors requires the other factors be changed in order to yield the same output at the same rate. Additionally, patients having higher ...
second embodiment
B. SECOND EMBODIMENT
1. Initial Phase Subsystem
FIG. 11 depicts an initial phase subsystem 12 composed of a DTC 220 for contacting a first extraction solvent with a fluid containing lipids or lipid-containing organisms, or both, and for removing at least a portion of the total concentration of lipids from the fluid. While FIG. 11 shows a single DTC, initial phase subsystem 12 may be composed of one or more DTCs coupled in series or parallel or any combination thereof. DTC 220 may be configured as shown in FIG. 5.
DTC 220 is in fluid communication with a fluid source 222 for receiving a fluid. Fluid source 222 may be positioned to feed the fluid to DTC 220 using gravity flow, a vacuum, a pump 224, which may be a peristaltic pump or other pump not having vanes that contact the fluid being pumped, or other means. DTC 220 contains a first extraction solvent supplied by first extraction solvent source 226 via gravity, a vacuum, pump 228, which may be a peristaltic pump, centrifugal pump...
third embodiment
C. THIRD EMBODIMENT
1. General Description
FIG. 12 depicts a portion of another embodiment of delipidation system 10 which includes initial phase subsystem and intermediate phase subsystem. This embodiment may be used together with the final phase subsystems shown in FIGS. 9 and 10 as described in more detail below. Unlike the previous systems described above, this embodiment does not use different apparatuses to complete the initial and intermediate phases of the delipidation process. Rather, this embodiment uses a single apparatus for completing the initial and intermediate phases of the delipidation process.
Specifically, FIG. 12 depicts in-line static mixers 270 and 272 coupled to both inlet and outlet sides of a vortexer 274. In-line static mixers 270 and 272 may be formed from many designs, but typically include single or multiple tubes containing one or more flow vanes along their length. Further, this embodiment is not limited to two in-line static mixers, but may comprise ...
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Abstract
Description
Claims
Application Information
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