Method of making a non compacted paper web containing refined long fiber using a charge controlled headbox and a single ply towel made by the process

A single ply towel product having a basis weight from 15 to 35 lb/rm;

• a geometric mean wet tensile strength from 500 to 2200 g/3 in;
• an absorbency from 125 to 400 g/m2;
• and a tensile modulus of stiffness from 50 to 150 g/in-% made by a process comprising:
• supply to a headbox an aqueous stream comprising a major proportion of refined long fiber having an average weight-weighted fiber length of from at least about 2 mm to about 3.5 mm, and a minor portion of a second fiber selected from the group consisting of hardwood fiber, recycle fiber, secondary fiber, nonwoody fibers, eucalyptus fibers, high yield fibers, thermally curled fibers, thermally cross-linked bulking fibers, and mixtures thereof;
• supplying to said aqueous stream a cationic wet strength agent selected from the group consisting of polyamide-epihalohydrin resins, thermosetting polyacrylamide resins, urea-formaldehyde resins, melamine formaldehyde resins, and mixtures thereof in an amount of from about 15 to about 30 lbs/tons of the total fiber in the furnish;
• supplying to said aqueous stream an anionic strength agent selected from the group consisting of carboxymethyl celluloses, carboxymethyl guar gums, anionic starches, anionic guar gums, anionic polyacrylamides, and mixtures thereof;
• measuring the total anionic charge carried by the aqueous stream;
• controlling the amount of cationic wet strength agent and anionic strength agent so that the net charge of the aqueous stream in the headbox is maintained in the range of from less than about zero to about −115 meq×10−6 per 10 ml;
• depositing said aqueous stream on a first moving foraminous support to form a web;
• non-compactively dewatering said web deposited on said first moving foraminous support to a consistency in the range of from about 10% to about 30%;
• transferring said web to a second moving foraminous support wherein the speed of said second moving foraminous support is at least about 2% less than the speed of the first moving foraminous support, thereby imparting a fabric crepe to said web of at least about 2%;
• drying said web to a consistency of at least about 40%;
• transferring said web to an internally heated drying cylinder;
• removing said web from said internally heated drying cylinder by a creping step wherein said creping imparts a reel crepe to said web of at least about 2%;
• embossing said web to a sufficient degree to reduce its tensile modulus of stiffness by at least 10%.

A single ply towel product having a basis weight from 15 to 35 lb/rm;

• a geometric mean wet tensile strength from 500 to 2200 g/3″;
• an absorbency from 125 to 400 g/m2;
• and a tensile modulus of stiffness from 50 to 150 g/in-% made by a process comprising:
• supplying to a headbox an aqueous stream comprising a major proportion of refined long fiber having an average weight-weighted fiber length of from at least about 2 mm to about 3.5 mm, and a minor portion of a second fiber selected from the group consisting of hardwood fibers, recycle fibers, secondary fibers, nonwoody fibers, eucalyptus fibers, high yield fibers, thermally curled fibers, thermally cross-linked bulking fibers, and mixtures thereof;
• supplying to said aqueous stream a cationic wet strength agent selected from the group consisting of polyamide-epihalohydrin resins, thermosetting polyacrylamide resins, urea-formaldehyde resins, melamine formaldehyde resins, and mixtures thereof in an amount of from about 15 to about 30 lbs/ton of total fiber in the furnish;
• supplying to said aqueous stream an anionic strength agent selected from the group consisting of carboxymethyl celluloses, carboxymethyl guar gums, anionic starches, anionic guar gums, anionic polyacrylamides, and mixtures thereof;
• measuring the total anionic charge carried by the aqueous stream;
• controlling the amount of cationic wet strength agent and anionic strength agent so that the net charge of the aqueous stream in the headbox is maintained in the range of from less than about zero to about −115 meq×10−6 per 10 ml;
• depositing said aqueous stream on a first moving foraminous support to form a web;
• non-compactively dewatering said web deposited on said first moving foraminous support to a consistency in the range of from about 10% to about 30%;
• transferring said web to a second moving foraminous support;
• drying said web to a consistency of at most about 98%;
• removing said web from said foraminous support.

An aqueous web produced by the method comprising:

• supplying to a headbox an aqueous stream comprising a major proportion of refined long fiber having an average weight-weighted fiber length of from at least about 2 mm to about 3.5 mm, and a minor portion of a second fiber selected from the group consisting of hardwood fibers, recycle fibers, secondary fibers, nonwoody fibers, eucalyptus fibers, high yield fibers, thermally curled fibers, thermally cross-linked bulking fibers, and mixtures thereof;
• supplying to said aqueous stream a cationic wet strength agent selected from the group consisting of polyamide-epihalohydrin resins, thermosetting polyacrylamide resins, urea-formaldehyde resins, melamine formaldehyde resins, and mixtures thereof in an amount of from about 15 to about 30 lbs/ton of total fiber in the furnish;
• supplying to said aqueous stream an anionic strength agent selected from the group consisting of carboxymethyl celluloses, carboxymethyl guar gums, anionic starches, anionic guar gums, anionic polyacrylamides, and mixtures thereof;
• measuring the total anionic charge carried by said aqueous stream;
• controlling the amount of cationic wet strength agent and anionic strength agent so that the net charge of said aqueous stream in the headbox is maintained in the range of from less than about zero to about −115 meq×10−6 per 10 ml;
• depositing said aqueous stream on a first moving foraminous support to form a web;
• non-compactively dewatering the web deposited on the first moving foraminous support to a consistency in the range of from about 10% to about 30%;
• transferring the web to a second moving foraminous support;
• drying the web to a consistency of at most about 98%;
• removing the web from the foraminous support.