The present invention provides a creped tissue web having a CD Wet/Dry ratio that meets or exceeds satisfactory levels without the excess use of a wet strength resin. The satisfactory level of CD Wet/Dry ratio is generally greater than about 0.40, more preferably greater than about 0.42 and still more preferably greater than about 0.44, such as from about 0.40 to about 0.45. The satisfactory level of CD Wet/Dry ratio is surprisingly achieved by treating the tissue making furnish with a relatively modest amount of non-wood synthetic fibers, preferably fibrillated acrylic fiber.

The present invention provides a creped tissue web having a CD Wet/Dry ratio that meets or exceeds satisfactory levels without the excess use of a wet strength resin. The satisfactory level of CD Wet/Dry ratio is generally greater than about 0.40, more preferably greater than about 0.42 and still more preferably greater than about 0.44, such as from about 0.40 to about 0.45. The satisfactory level of CD Wet/Dry ratio is surprisingly achieved by treating the tissue making furnish with a relatively modest amount of non-wood synthetic fibers, preferably fibrillated acrylic fiber.

A spinning nozzle which has a perforated part in which ejection holes have been arranged in a density as high as 600-1,200 holes/mm.sup.2. This process for producing a fibrous bundle comprises ejecting a spinning dope having a viscosity as measured at 50° C. of 30-200 P from the ejection holes of the spinning nozzle to produce a fibrous bundle. This fibrous bundle has a single-fiber fineness of 0.005-0.01 dtex. By the wet-process direct spinning, a mass of nanofibers which are stably uniform and continuous can be produced at a high efficiency.

A spinning nozzle which has a perforated part in which ejection holes have been arranged in a density as high as 600-1,200 holes/mm.sup.2. This process for producing a fibrous bundle comprises ejecting a spinning dope having a viscosity as measured at 50° C. of 30-200 P from the ejection holes of the spinning nozzle to produce a fibrous bundle. This fibrous bundle has a single-fiber fineness of 0.005-0.01 dtex. By the wet-process direct spinning, a mass of nanofibers which are stably uniform and continuous can be produced at a high efficiency.

The present invention relates to a biodegradable paper sheet for filter element comprising refined cellulose fibers and hydrophobic fibers.

The present invention relates to a biodegradable paper sheet for filter element comprising refined cellulose fibers and hydrophobic fibers.

An airlaid substrate includes at least one bicomponent fiber having a first region and a second region. The first region includes polypropylene and the second includes a blend of an ethylene-base polymer and an ethylene acid copolymer. The ethylene-base polymer has a density from 0.920 g/cm.sup.3 to 0.970 g/cm.sup.3 and a melt index (I.sub.2) from 0.5 g/10 min to 150 g/10 min. The ethylene acid copolymer includes the polymerized reaction product of from 60 wt % to 99 wt % ethylene monomer and from 1 wt % to 40 wt % unsaturated dicarboxylic acid comonomer, based on the total weight of the monomers in the ethylene acid copolymer. The ethylene acid copolymer having a melt index (I.sub.2) from 0.5 g/10 min to 500 g/10 min.

An airlaid substrate includes at least one bicomponent fiber having a first region and a second region. The first region includes polypropylene and the second includes a blend of an ethylene-base polymer and an ethylene acid copolymer. The ethylene-base polymer has a density from 0.920 g/cm.sup.3 to 0.970 g/cm.sup.3 and a melt index (I.sub.2) from 0.5 g/10 min to 150 g/10 min. The ethylene acid copolymer includes the polymerized reaction product of from 60 wt % to 99 wt % ethylene monomer and from 1 wt % to 40 wt % unsaturated dicarboxylic acid comonomer, based on the total weight of the monomers in the ethylene acid copolymer. The ethylene acid copolymer having a melt index (I.sub.2) from 0.5 g/10 min to 500 g/10 min.

An airlaid substrate includes at least one bicomponent fiber having a first region and a second region. The first region includes polypropylene and the second includes a blend of an ethylene-base polymer and an ethylene acid copolymer. The ethylene-base polymer has a density from 0.920 g/cm.sup.3 to 0.970 g/cm.sup.3 and a melt index (I.sub.2) from 0.5 g/10 min to 150 g/10 min. The ethylene acid copolymer includes the polymerized reaction product of from 60 wt % to 99 wt % ethylene monomer and from 1 wt % to 40 wt % unsaturated dicarboxylic acid comonomer, based on the total weight of the monomers in the ethylene acid copolymer. The ethylene acid copolymer having a melt index (I.sub.2) from 0.5 g/10 min to 500 g/10 min.

An airlaid substrate includes at least one bicomponent fiber having a first region and a second region. The first region includes polypropylene and the second includes a blend of an ethylene-base polymer and an ethylene acid copolymer. The ethylene-base polymer has a density from 0.920 g/cm.sup.3 to 0.970 g/cm.sup.3 and a melt index (I.sub.2) from 0.5 g/10 min to 150 g/10 min. The ethylene acid copolymer includes the polymerized reaction product of from 60 wt % to 99 wt % ethylene monomer and from 1 wt % to 40 wt % unsaturated dicarboxylic acid comonomer, based on the total weight of the monomers in the ethylene acid copolymer. The ethylene acid copolymer having a melt index (I.sub.2) from 0.5 g/10 min to 500 g/10 min.