Self-metering liquid retentive pad and process for producing same

A process for producing a self-metering ink retentive printer comprising:

• I. mixing salt of a size of 2 to 450 microns with a polymeric material in a weight ratio of 2.5:1 to 10:1 salt to polymer;
• II. heating the polymer to a molten state and dispersing the salt to form a salt-polymer composite;
• III. feeding the composite to an extruder and extruding to desired shape, whereby a more dense skin portion is formed on the upper surface of the extruded polymer;
• IV. cutting and finishing the extruded polymer, to desired printer size;
• V. leaching out the salt with solvent;
• VI. drying the extruded polymeric matrix to evaporate leaching solvent;
• and
• VII. impregnating the printer with ink.

A process for producing a self-metering ink-retentive printer comprising:

• I. mixing salt of a size of 2 to 450 microns with a polymeric material in a weight ratio of 2.5:1 to 10:1, salt to polymer;
• II. heating the polymer to a molten state and dispersing the salt in the molten polymer to form a salt-polymer composite;
• III. feeding the composite to an extruder and extruding to desired shape;
• IV. repeating Steps I and II to form additional composites and extruding onto the existing extruded polymer until the desired number of layers are constructed, wherein the density is greatest on the top layer and wherein the top layer has a pronounced skin portion on the surface;
• V. cutting and finishing the extruded polymer to desired printer shape;
• VI. leaching out the salts with solvent;
• VII. drying the extruded polymer matrices to evaporate the leaching solvent;
• VIII. impregnating the printer with ink.

A process for producing a high-speed self-metering single layer ink retentive printer comprising:

• I. mixing sodium nitrate salt of 2 to 38 microns with a polymeric elastomer in a weight ratio of from 4:1 to 8:1 salt to polymer;
• II. heating at 60.degree.-176.degree. C. to disperse sodium nitrate in polymer and to form a salt-polymer composite;
• III. feeding the composite to an extruder;
• IV. extruding at an extruder barrel temperature of 48.degree.-205.degree. C. and an average die pressure of 4500-5000 p.s.i. with a screw design having a length to outer diameter ratio of 10:1 to 32:1 and a compression ratio of 1:1 to 5:1,
• V. recovering the extruded composite at a die temperature of 65.degree. to 205.degree. C.;
• VI. achieving a skin thickness of 40 to 50 microns on the extruded composite;
• VII. cutting and finishing the extruded composite to desired printer size;
• VIII. leaching out the sodium nitrate with hot water at 45.degree. to 55.degree. C.;
• and
• IX. drying the extruded leached composite in a forced air oven at 45.degree. to 95.degree. C.

A process for producing a high-speed self-metering multi-layer ink retentive printer comprising:

• I. mixing sodium nitrate salt of 2 to 450 microns with a polymeric elastomer in a weight ratio from 5:1 to 10:1 salt to polymer;
• II. heating at 60.degree. to 176.degree. C. to disperse sodium nitrate in polymer and to form a salt-polymer composite;
• III. feeding the composite to an extruder;
• IV. extruding at 48.degree. to 205.degree. C. and an average die pressure of 4,000-5,000 p.s.i. with a screw design having a length to outer diameter ratio of 10:1 to 32:1 and a compression ratio of 1:1 to 5:1 to form a rigid extruded body;
• V. mixing sodium nitrate salt of 2 to 38 microns with a polymeric elastomer in a weight ratio from 2.5:1 to 8:1 salt to polymer;
• VI. heating at 60.degree.-176.degree. C. to disperse the sodium nitrate in the polymer and to form a second salt-polymer composite;
• VII. feeding the second composite to the extruder;
• VIII. extruding onto the first extruded body at 48.degree. to 205.degree. C. and an average die pressure of 4000 to 5000 p.s.i. with a screw design of length to diameter of 10:1 to 32:1 and a compression ratio of 1:1 to 5:1 to form a multi-layer extruded body;
• IX. recovering the extruded multi-layered composite at a die temperature of 65.degree. to 205.degree. C.;
• X. achieving a skin thickness of 40 to 50 microns on the second extruded polymer layer;
• XI. cutting and finishing the multi-layer extruded body to desired printer size;
• XII. leaching out the sodium nitrate with hot water at 45.degree. to 55.degree. C.;
• XIII. drying the extruded leached body in a forced air oven at 45.degree. to 95.degree. C.

A process for producing low-speed self-metering single layer ink retentive printer comprising:

• I. mixing sodium nitrate salt of 2 to 450 microns with a polymeric elastomer in a weight ratio from 5:1 to 10:1 salt to polymer;
• II. heating at 60.degree.-176.degree. C. to disperse sodium nitrate in polymer and to form a salt-polymer composite;
• III. feeding the composite to an extruder;
• IV. extruding at 48.degree. to 205.degree. C. and an average die pressure of 4,000-5,000 p.s.i. with a screw design of length to outer diameter of 10:1 to 32:1 to form an extruded composite;
• V. recovering the extruded composite at a die temperature of 65.degree. to 205.degree. C.;
• VI. achieving a skin thickness of 40 to 50 microns on the extruded composite;
• VII. cutting and finishing the extruded composite to desired printer size;
• VIII. leaching out the sodium nitrate with hot water at 45.degree. to 55.degree. C.;
• IX. drying the extruded leached composite in a forced air oven at 45.degree. to 95.degree. C.

A process for producing a low-speed self-metering multi-layer ink retentive printer comprising:

• I. mixing sodium nitrate salt of 2 to 450 microns with a polymeric elastomer in a weight ratio from 5:1 to 10:1 salt to polymer;
• II. heating at 60.degree.-176.degree. C. to disperse sodium nitrate in polymer and to form a salt-polymer composite;
• III. feeding the composite to an extruder;
• IV. extruding at 48.degree. to 205.degree. C. and an average pressure of 4,000 to 5,000 p.s.i. with a screw design of length to outer diameter of 10:1 to 32:1 to form a rigid extruded body;
• V. mixing sodium nitrate salt of 74 to 150 microns with a polymeric elastomer in a weight ratio from 4:1 to 8:1 salt to polymer to form a second salt-polymer composite;
• VI. feeding the second composite to an extruder;
• VII. extruding the second composite onto the first extruded body at 48.degree. to 205.degree. C. and an average die pressure of 4,000 to 5,000 p.s.i. with a screw design of length to outer diameter of 10:1 to 32:1 and a compression ratio of 1:1 to 5:1 to form a multi-layer extruded body;
• VIII. achieving a skin thickness of 40 to 50 microns on the multi-layer extruded body;
• IX. cutting and finishing the multi-layer extruded body to desired printer size;
• X. leaching out the sodum nitrate with hot water at 45.degree. to 205.degree. C.
• XI. drying the multi-layer extruded body in a forced air oven at 45.degree. to 95.degree. C.

A multi-layer ink printer comprising in combination:

• A. an extruded microporous polymer layer;
• B. an outer skin portion of the extruded microporous polymer layer with channels and pores of a size smaller than the channels and pores of the microporous polymer layer integral therewith;
• C. a second additional extruded porous polymer layer connected to the underside of the first microporous polymer layer so that the channels and the pores of the second layer are of a size greater than the size of the pores in the first layer and wherein the density of the layers is greatest at the skin portion and decreases with the cross section;
• and this second layer is extruded onto a solid profile
• and
• D. ink contained in the channels and pores of both layers self-metering in use.

An ink printer comprising in combination:

• a pad composed of
• A. a microporous polymer layer integral with a skin portion but with channels and pores larger than the outer skin portion;
• B. an outer skin portion of an extruded microporous polymer layer wherein the density is greatest at the skin portion
• wherein said pad is produced by the steps of:
• I. mixing salt of a size of 2 to 450 microns with a polymeric material in a weight ratio of 2.5:1 to 10:1 salt to polymer;
• II. heating the polymer to a molten state and dispersing the salt to form a salt-polymer composite;
• III. feeding the composite to an extruder and extruding to desired shape, whereby a more dense skin portion is formed on the upper surface of the extruded polymer;
• IV. cutting and finishing the extruded polymer to desired pad size;
• V. leaching out the salt with solvent;
• and
• VI. drying the extruded polymeric matrix to evaporate leaching solvent and
• C. ink contained in the channels and pores of said layers.

A multi-layer ink printer comprising in combination:

• A. an extruded microporous polymer layer;
• B. an outer skin portion of the extruded microporous polymer layer with channels and pores of a size smaller than the channels and pores of the microporous polymer layers integral therewith;
• C. at least one additional extruded porous polymer layer connected to the underside of the first microporous polymer layer so that the channels and the pores of the second layer connect with the channels and the pores of the first layer and wherein the pores and channels of the second layer are of a size greater than the size of the pores in the first layer and wherein the density of the layers is greatest at the skin portion and decreases with the cross section;
• and
• wherein said pad is produced by the steps of:
• I. mixing salt of a size of 2 to 450 microns with a polymeric material in a weight ratio of 2.5:1 to 10:1, salt to polymer;
• II. heating the polymer to a molten state and dispersing the salt in the molten polymer to form a salt-polymer composite;
• III. feeding the composite to an extruder and extruding to desired shape;
• IV. repeating Steps I and II to form at least one additional composite and extruding it onto the existing extruder polymer until the desired number of layers are constructed, wherein the density is greatest on the top layer and wherein the top layer has a pronounced skin portion on the surface;
• V. cutting and finishing the extruded polymer to desired printer shape;
• VI. leaching out the salts with solvent;
• VII. drying the extruded polymer matrices to evaporate the leaching solvent;
• and
• D. ink contained in the channels and pores of all layers selt-metering in use.