Fibrous filter media and process for producing same

Claim 2

An improved fibrous filter material for filtration of fluid media, said media being comprised largely of fibers, which comprises (a) a random-laid sheet-like filter structure formed of a substantial fraction of lignin-containing fibers derived from the disc refining in a substantially dry condition of substantially undelignified wood chips having a lignin content of at least about 10%, under steam pressures in the range of about 90 psig to about 120 psig, at temperatures in the range of from about 330° F. to about 350° F., and using energy levels in the range of from about 8 to about 35 HPD/ADT, (b) said disc refining taking place in the absence of substantial liquid medium in said refiner, (c) said ligin-containing fibers being characterized by having most of their original lignin content and by having a smooth wall structure, substantially free of fiber-bonding surface fibrils and being substantially non-self-bonding to adjacent like fibers in the absence of elevated temperatures, (d) said lignin-containing fiber fraction having a freeness of not less than about 725 ml (CSF).

Claim 3

Improved filter media according to claim 1, further characterized by (a) said lignin-containing fibers being present in amounts of about 30% or more, in combination with other fibers, (b) said other fibers comprising at least in part fibers from flash dried softwood, flash dried hardwood pulp, alpha pulp, or synthetic fiber, or combinations thereof.

Claim 4

Improved filter media according to claim 2, further characterized by (a) said lignin-containing fibers being those capable of passing thorugh circumferentially aligned slots of a rotary screen, in which the slots have a width of about 6 mils, (b) said fibers having a size distribution such that approximately 60% is retained on a 28 mesh screen.

Claim 5

The process of making fibrous filter material for the filtration of fluid media, which comprises (a) furnishing a fibrous, substantially undelignified, lignin-containing raw material having a lignin content of at least about 10%, (b) reducing said lignin-containing material to individual pieces of a size appropriate for disc refining, (c) preheating said lignin-containing material pieces by steam at a temperature of from about 330° F. to about 350° F. and a pressure of from about 90 psig to about 120 psig for a period sufficient to enable the material to be heated and the lignin content thereof to be softened, (d) deriving from said raw material lignin-containing fibers having most of their original lignin content by disc refining said preheated material in a substantially dry condition and while maintaining said steam temperature of from about 330° F. to about 350° F. and pressure of from about 90 psig to about 120 psig and under refiner settings requiring an average energy usage for refining of the lignin-containing material of from about 8 to about 35 HPD/ADT, (e) screening a slurry of said disc refined material to remove oversize fibers and shives, (f) said screened material having a freeness of not less than about 725 ml (CSF), (g) laying the screened, lignin-containing fibers in a random fashion to form a free, porous sheet-like filter structure with minimum self-bonding between said screened fibers, and (h) imparting to said laid fibers sufficient bonding characteristics to effect at least a minimum degree of bonding between fibers in the region of fiber contact areas.

Claim 6

The process of making fibrous filter material for the filtration of fluid media, which comprises (a) furnishing a fibrous, substantially undelignified, lignin-containing raw material having a lignin content of at least about 10%, (b) reducing said lignin-containing material to individual pieces of a size appropriate for disc refining, (c) preheating said lignin-containing material pieces by steam at a temperature of from about 330° F. to about 350° F. and a pressure of from about 90 psig to about 120 psig for a period sufficient to enable the material to be heated and the lignin content thereof to be softened, (d) deriving from said raw material lignin-containing fibers having most of their original lignin content by disc refining said preheated material in a substantially dry condition and while maintaining said steam temperature of from about 330° F. to about 350° F. and pressure of from about 90 psig to about 120 psig and under refiner settings requiring an average energy usage for refining of the lignin-containing material of from about 8 to about 35 HPD/ADT, (e) screening a slurry of said disc refined material to remove oversize fibers and shives, (f) said screened material having a freeness of not less than about 725 ml (CSF), (g) laying the screened, lignin-containing fibers in a random fashion to form a free, porous sheet-like filter structure with minimum self-bonding between said screened fibers, and (h) imparting to said laid fibers sufficient bonding characteristics to effect at least a minimum degree of bonding between fibers in the region of fiber contact areas.

Claim 7

The process of claim 4, further characterized by (a) said lignin-containing material comprising pulp wood logs, (b) said pulp wood logs being initially debarked and then cut into chips having a typical minimum dimension of about 3/8 inch and a typical maximum dimension about one inch.

Claim 8

The process of claim 5, further characterized by (a) said pulp wood chips being refined in a double disc, counter-rotating disc refiner, (b) the discs of said refiner being set to provide an outlet peripheral gap which will control the energy usage between about 8 HPD/ADT and about 35 HPD/ADT, during refining of said pulp wood.

Claim 9

The process of claim 6, further characterized by (a) mixing the lignin-containing fibers, after refining, with sufficient water to form a screenable slurry, and (b) screening said slurry in a rotatable screen having circumferentially aligned slots for the acceptance and passage of desired fibers.

Claim 10

The process of claim 4, further characterized by (a) said lignin-containing material being preheated by steam for a period of approximately three minutes, in direct contact with said steam.

Claim 11

The process of claim 8, further characterized by (a) said lignin-containing material comprising chips of debarked pulp wood, (b) said chips having typical minimum dimensions of about 3/8 inch and typical maximum dimensions of about one inch, and (c) said chips being retained in contact with said steam, during the preheating phase, for time sufficient to bring the core of the chip to a temperature of within about 10° F. of the temperature of the steam.

Claim 12

An improved fibrous filter material for the filtration of fluid media, comprised largely of fibers, which comprises (a) a substantial fraction of lignin-containing fibers derived from the rotary disc refining in a substantially dry state of substantially undelignified, lignin-containing material having a lignin content of at least about 10%, (b) said lignin-containing fibers having been derived from said disc refining under steam pressures in the range of about 90 psig to about 120 psig and at temperatures in the range of from about 330° F. to about 350° F. and with energy usage in the range of from about 8 to about 35 HPD/ADT, (c) said lignin-containing fibers being combined with other papermaking type fibers and randomly laid to form a web, (d) said web being impregnated with sufficient binder resin to accommodate handling and forming, (e) said lignin containing fiber fraction having a freeness of not less than about 725 mL (CSF), (f) said lignin containing fiber fraction having a bulk characteristic, when formed into an unpressed sheet, corresponding to a caliper of about 0.040 inch in a sheet having a basis weight of about 65 lbs. (per 3000 sq. ft.).

Claim 13

An improved fibrous filter material for the filtration of fluid media, comprised largely of fibers, which comprises (a) a substantial fraction of lignin-containing fibers derived from the rotary disc refining in a substantially dry state of substantially undelignified, lignin-containing material having a lignin content of at least about 10%, (b) said lignin-containing fibers having been derived from said disc refining under steam pressures in the range of about 90 psig to about 120 psig and at temperatures in the range of from about 330° F. to about 350° F. and with energy usage in the range of from about 8 to about 35 HPD/ADT, (c) said lignin-containing fibers being combined with other papermaking type fibers and randomly laid to form a web, (d) said web being impregnated with sufficient binder resin to accommodate handling and forming, (e) said lignin containing fiber fraction having a freeness of not less than about 725 mL (CSF), (f) said lignin containing fiber fraction having a bulk characteristic, when formed into an unpressed sheet, corresponding to a caliper of about 0.040 inch in a sheet having a basis weight of about 65 lbs. (per 3000 sq. ft.).

Claim 14

A filter web according to claim 10, further characterized by (a) said lignin-containing fibers containing, in the finished form of said filter web, major amounts of their original lignin content, (b) said lignin-containing fibers being characterized by a smooth wall structure substantially free of fiber-bonding fibrils and being substantially non-self-bonding to adjacent like fibers.

Claim 15

A filter web according to claim 11, further characterized by (a) said other paper-making type fibers including any one or more of polyester, cotton linters, or flash dried hardwood.

Claim 16

The process of making filter material for the filtration of fluid media, which comprises (a) selecting a source of lignin-containing fibers having an initial lignin content of not less than about 10%, (b) subjecting said lignin-containing fiber source to a preheating treatment for at least about three minutes in a pressurized steam atmosphere at a temperature of from about 330° F. to about 350° F. and at a pressure of from about 90 psig to about 120 psig, (c) thereafter abraisively refining said fiber source in a substantially dry condition and while maintaining a steam atmosphere at a temperature of from about 330` F. to about 350° F. and pressure of from about 90 psig to about 120 psig, (d) carrying out said refining under energy usage conditions of from about 8 to about 35 HPD/ADT to produce lignin-containing fibers having a smooth lignin-coated outer surface and containing most of their initial lignin content, said lignin-containing fibers having a freeness of at least about 725 ml (CSF), and (e) forming a random-laid mass comprising at least a substantial fraction of said fibers to constitute a filter product having superior dust capacity.

Claim 17

The process of making filter material for the filtration of fluid media, which comprises (a) selecting a source of lignin-containing fibers having an initial lignin content of not less than about 10%, (b) subjecting said lignin-containing fiber source to a preheating treatment for at least about three minutes in a pressurized steam atmosphere at a temperature of from about 330° F. to about 350° F. and at a pressure of from about 90 psig to about 120 psig, (c) thereafter abraisively refining said fiber source in a substantially dry condition and while maintaining a steam atmosphere at a temperature of from about 330` F. to about 350° F. and pressure of from about 90 psig to about 120 psig, (d) carrying out said refining under energy usage conditions of from about 8 to about 35 HPD/ADT to produce lignin-containing fibers having a smooth lignin-coated outer surface and containing most of their initial lignin content, said lignin-containing fibers having a freeness of at least about 725 ml (CSF), and (e) forming a random-laid mass comprising at least a substantial fraction of said fibers to constitute a filter product having superior dust capacity.

Claim 18

The process of claim 13, further characterized by (a) said fiber source comprising debarked pulp wood, and (b) said pulp wood being cut into chips.

Claim 19

The process of claim 14, further characterized by (a) said lignin-containing fibers being random-laid in continuous web form and having combined therein fibers from one or more additional fiber sources.

Claim 20

The process of claim 15, further characterized by (a) said fibers from additional sources including one or more of flash dried kraft fibers and polyester fibers.