Patent classifications
B01D71/10
Fibrillated fibers for liquid filtration media
Fiber webs which are used in filter media are described herein. In some embodiments, the fiber webs include fibrillated fibers and optionally non-fibrillated fibers, amongst other optional components (e.g., binder resin). In some embodiments, the fiber webs include limited amounts of, or no, glass fiber. The respective characteristics and amounts of the fibrillated fibers are selected to impart desirable properties including mechanical properties and filtration properties (e.g., dust holding capacity and efficiency), amongst other benefits.
Fibrillated fibers for liquid filtration media
Fiber webs which are used in filter media are described herein. In some embodiments, the fiber webs include fibrillated fibers and optionally non-fibrillated fibers, amongst other optional components (e.g., binder resin). In some embodiments, the fiber webs include limited amounts of, or no, glass fiber. The respective characteristics and amounts of the fibrillated fibers are selected to impart desirable properties including mechanical properties and filtration properties (e.g., dust holding capacity and efficiency), amongst other benefits.
Method for preparing a membrane from fibril cellulose and fibril, cellulose membrane
Method for preparing a membrane from fibril cellulose includes supplying fibril cellulose dispersion on a filter layer, draining liquid from a fibril cellulose dispersion by the effect of reduced pressure through the filter layer that is impermeable to fibrils of the fibril cellulose but permeable to the liquid to form a membrane sheet on the filter fabric, applying heat on the opposite side of the membrane sheet to the membrane sheet while continuing draining of the liquid through the filter layer by pressure difference over the filter layer, and removing the membrane sheet from the filter layer as a freestanding membrane.
Method for preparing a membrane from fibril cellulose and fibril, cellulose membrane
Method for preparing a membrane from fibril cellulose includes supplying fibril cellulose dispersion on a filter layer, draining liquid from a fibril cellulose dispersion by the effect of reduced pressure through the filter layer that is impermeable to fibrils of the fibril cellulose but permeable to the liquid to form a membrane sheet on the filter fabric, applying heat on the opposite side of the membrane sheet to the membrane sheet while continuing draining of the liquid through the filter layer by pressure difference over the filter layer, and removing the membrane sheet from the filter layer as a freestanding membrane.
CHROMATOGRAPHY-FREE ANTIBODY PURIFICATION METHOD
The present invention relates method for purifying antibodies, said method comprising a limited number of steps while still allowing obtaining high yields of purified antibodies with an appropriate degree of purity. Briefly, this method comprises only filtration and precipitation steps, omitting the need for chromatography steps.
CHROMATOGRAPHY-FREE ANTIBODY PURIFICATION METHOD
The present invention relates method for purifying antibodies, said method comprising a limited number of steps while still allowing obtaining high yields of purified antibodies with an appropriate degree of purity. Briefly, this method comprises only filtration and precipitation steps, omitting the need for chromatography steps.
PREPARATION AND USE OF CELLULOSE NANOFIBER MEMBRANE
A filtration membrane comprising cellulose fibres, the membrane having a pore size distribution such that the modal pore diameter is between 10 nm and 25 nm and/or wherein less than 5% of the pore volume comprises pores of greater than 40 nm and having a total porosity greater than 30%.
PREPARATION AND USE OF CELLULOSE NANOFIBER MEMBRANE
A filtration membrane comprising cellulose fibres, the membrane having a pore size distribution such that the modal pore diameter is between 10 nm and 25 nm and/or wherein less than 5% of the pore volume comprises pores of greater than 40 nm and having a total porosity greater than 30%.
FILTRATION
The present invention provides method of removing particles from a feed fluid, the method comprising: passing the fluid through a first filtration medium having a thickness of from 5 to 20 μm, wherein passing the feed fluid through the first filtration medium provides a particle removal probability log10 reduction value (LRV) of greater than or equal to 1 for particles having a diameter of from about 10 to about 40 nm and a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles greater than about 40 nm in diameter; and passing the fluid through a second filtration medium having a thickness of from 20 to 70 μm (e.g. 20 to 45 μm) 20 to 45 pm, wherein passing the feed fluid through the second filtration medium provides a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles having a diameter of from about 10 to about 40 nm and a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles having a diameter of greater than or equal to about 40 nm; so as to retain at least a portion of the particles on each medium to produce a filtrate containing a lower concentration of the particles than the feed fluid.
FILTRATION
The present invention provides method of removing particles from a feed fluid, the method comprising: passing the fluid through a first filtration medium having a thickness of from 5 to 20 μm, wherein passing the feed fluid through the first filtration medium provides a particle removal probability log10 reduction value (LRV) of greater than or equal to 1 for particles having a diameter of from about 10 to about 40 nm and a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles greater than about 40 nm in diameter; and passing the fluid through a second filtration medium having a thickness of from 20 to 70 μm (e.g. 20 to 45 μm) 20 to 45 pm, wherein passing the feed fluid through the second filtration medium provides a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles having a diameter of from about 10 to about 40 nm and a particle removal probability log10 reduction value (LRV) of greater than or equal to 3 for particles having a diameter of greater than or equal to about 40 nm; so as to retain at least a portion of the particles on each medium to produce a filtrate containing a lower concentration of the particles than the feed fluid.