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EP1023493A1 - Cellulose filter paper saturant - Google Patents

Cellulose filter paper saturant

Info

Publication number
EP1023493A1
EP1023493A1 EP98944792A EP98944792A EP1023493A1 EP 1023493 A1 EP1023493 A1 EP 1023493A1 EP 98944792 A EP98944792 A EP 98944792A EP 98944792 A EP98944792 A EP 98944792A EP 1023493 A1 EP1023493 A1 EP 1023493A1
Authority
EP
European Patent Office
Prior art keywords
saturant
filter paper
formaldehyde resin
polyvinyl alcohol
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP98944792A
Other languages
German (de)
French (fr)
Other versions
EP1023493A4 (en
Inventor
Norman Lifshutz
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hollingsworth and Vose Co
Original Assignee
Hollingsworth and Vose Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hollingsworth and Vose Co filed Critical Hollingsworth and Vose Co
Publication of EP1023493A1 publication Critical patent/EP1023493A1/en
Publication of EP1023493A4 publication Critical patent/EP1023493A4/en
Withdrawn legal-status Critical Current

Links

Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D39/00—Filtering material for liquid or gaseous fluids
    • B01D39/14—Other self-supporting filtering material ; Other filtering material
    • B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/18—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being cellulose or derivatives thereof
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/08—Filter paper
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/36—Polyalkenyalcohols; Polyalkenylethers; Polyalkenylesters
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47—Condensation polymers of aldehydes or ketones

Definitions

  • the invention is directed to saturants for cellulose paper, and more particularly for saturants for cellulose filter paper.
  • Cellulose filter papers are well known for many applications, such as automotive and heavy-duty oil and air filtration. Generally, they are produced by dispersing cellulose fibers, such as wood pulps, in water and filtering the fiber suspension through the continuous screen or wire of a paper machine. Conventionally, the resulting paper is dried once, then saturated with an aqueous or non-aqueous solution or suspension of polymer or resin, and finally dried again. Alternatively, while still wet, the freshly formed paper is saturated with the aqueous or non-aqueous solution or suspension of polymer or resin, and then dried only once. The dried, saturated paper may be then pleated, dimpled, or otherwise formed into a filter configuration, and possibly given a thermal cure to develop its final properties.
  • cellulose fibers such as wood pulps
  • the saturant In order to perform adequately in automotive and heavy-duty (truck) oil and air filtration applications, the saturant must confer high Mullen burst strength, tensile strength, and particularly stiffness, under cured, wet, or elevated temperature conditions. In addition, since wood pulp is typically much less expensive than the polymers and resins comprising the saturant, it is economically desirable to achieve these mechanical properties using the lowest possible saturant content in the finished paper.
  • One convenient method of characterizing stiffness at a range of elevated temperatures is through the use of a Dynamic Mechanical Analyzer in bending beam mode, e.g. the "DMA-7" from Perkin Elmer.
  • a Dynamic Mechanical Analyzer in bending beam mode, e.g. the "DMA-7" from Perkin Elmer.
  • Such an instrument can measure the "in phase” bending modulus (elastic stiffness), and the "out of phase” loss modulus of the paper as the temperature is scanned from about room temperature to about 200°C.
  • Previously known saturants typically have been low molecular weight formaldehyde resins of phenol, urea or melamine, dissolved in organic solvent or water.
  • saturants have included aqueous dispersions of high molecular weight polymers such as polyvinyl acetate, polyvinyl chloride, or polyacrylic esters dispersed, but not dissolved, in water, or combinations of such polymers.
  • U.S. Pat. No. 4,461,858 discloses an acidic colloidal system for use in cellulose pulp slurries that includes a stable aqueous polyvinyl- alcohol/melamine-formaldehyde resin interaction product that comprises a polyvinyl alcohol polymer and a cationic melamine-formaldehyde resin colloid in a polyvinyl alcohol/ melamine formaldehyde resin acid colloid.
  • 4,324,833 discloses an acidic aqueous phenolic resin-urea wet process mat binder comprising an aqueous solution of a partially methylated melamine-formaldehyde resin and a polyvinyl alcohol, the aqueous solution having a pH within the range of from about 3.5 to about 6.5.
  • the invention is directed to a filter paper made with a saturant comprising a hydrolyzed polyvinyl alcohol and a formaldehyde resin, wherein the polyvinyl alcohol and the formaldehyde resin are substantially or completely dissolved in the system.
  • the saturant is applied to a filter base paper, such as a cellulose base paper, such that the saturant forms about 5 % to 20% of the filter paper in the dried condition.
  • the saturant used with the invention is an aqueous solution of a fully hydrolyzed high molecular weight polyvinyl alcohol and a water-soluble, low molecular weight, methylol-containing resin.
  • the methylol-containing resin is preferably a formaldehyde resin of phenol, urea or melamine.
  • the formaldehyde resin acts as a crosslinking agent for the polyvinyl alcohol.
  • the system includes a solution of polyvinyl alcohol and a formaldehyde resin of phenol having a pH within the range of from about 7.5 to about 10.5.
  • An inorganic salt can be used as a catalyst to assist the crosslinking of urea and melamine resins.
  • the invention is also directed to methods for making and using the water- based saturant.
  • FIG. 1 is a graph comparing the stiffness of cellulose paper made in accordance with the present invention, containing phenolic and polyvinyl alcohol resins, and cellulose paper made with either resin alone;
  • FIG. 2 is a graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention.
  • FIG. 3 is a graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention.
  • FIG. 4 is graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention.
  • the invention is directed to a filter paper formed with a saturant that comprises of an aqueous solution of a hydrolyzed polyvinyl alcohol and a formalde- hyde resin, where the formaldehyde resin and the polyvinyl alcohol are completely or substantially dissolved.
  • the polyvinyl alcohol is present in a sufficient amount to enable the system to function as a saturant in cellulose papermaking operations.
  • the polyvinyl alcohol is present in the dried saturant composition in an amount that ranges from about 25 % to 95 % by weight.
  • the polyvinyl alcohol is present in the dried saturant composition in an amount that ranges from about 25 % to 95 % by weight.
  • the polyvinyl alcohol is sufficiently hydrolyzed so that when it is combined with the formaldehyde resin and water, the formaldehyde resin crosslinks with the polyvinyl alcohol.
  • the polyvinyl alcohol is hydrolyzed at least about 98% .
  • Suitable polyvinyl alcohols include Airvol ® 103, 107, 125 and 165, available from Air Products Inc., and Elvanol ® 70-06, 71- 30 and 90-50, available from duPont de Nemours & Co.
  • the molecular weight of the polyvinyl alcohol is generally in the range of
  • the molecular weight of the polyvinyl alcohol ranges from about 30,000 to about 50,000.
  • the methylol containing formaldehyde resin of phenol, urea or melamine preferably is water soluble and has the functionality to act as a crosslinking or curing agent for polyvinyl alcohol resin.
  • the crosslinking resin has an average degree of polymerization of 1 to 3.
  • Suitable formaldehyde resins of phenol include Arofene 72155, Arotap 8095 and Arofene DR 343, all available from Ashland Chemical Co.
  • An exemplary formaldehyde resin of melamine includes
  • the formaldehyde resin is ordinarily present in a dry saturant composition in an amount from about 75 % to 5 % by weight, but other ranges are within the scope of the invention.
  • the formaldehyde resin is a resin of phenol. Suitable urea and melamine resins may also be used. Exemplary ureas and melamines include urea glyoxal formaldehyde condensate (BERSET 2300, available from Bercen, Inc. of Cranston, Rhode Island), and melamine formaldehyde resins such as BERSET 2003 (available from Bercen, Inc. of Cranston, Rhode Island), SEQUA MEL-80 (available from Sequa Chemicals, Inc. of Chester, South Carolina), AURAMEL 484, AURAMEL M-75, and AURAREZ 963 (available from BERSET 2300, available from Bercen, Inc. of Cranston, Rhode Island), and melamine formaldehyde resins such as BERSET 2003 (available from Ber
  • an acid salt can be used as a catalyst to assist the crosslinking of urea and formaldehyde resins.
  • Suitable acid salts are those formed from a weak base and a strong acid which, upon hydrolysis, yield a strong acid.
  • Exemplary acid salts useful as catalysts in this invention include magnesium chloride, ammonium sulfate, ammonium nitrate, ammonium chloride, and aluminum chloride.
  • a particularly preferred acid salt is magnesium chloride.
  • Such an acid salt is generally used at a concentration in the range of about 2.5 to 7.5 wt. % solids in the saturant.
  • the saturant generally has a pH that is sufficiently high to maintain all or substantially all of the formaldehyde resin soluble.
  • the pH of the saturant can be adjusted with a base to be within the range of 7.5 to 10.5.
  • Suitable bases include a fixed base such as potassium or sodium hydroxide, or a fugitive base such as ammonium hydroxide. Other pH ranges are within the scope of the invention.
  • the water-based saturant of the invention may be made with conventional preparation techniques. Normally, the polyvinyl alcohol is dissolved in water at 185°F and cooled with additional water. The pH is adjusted, and the crosslinking resin is then added.
  • the saturant imparts improved stiffness and strength to cellulose filter paper under a variety of papermaking conditions. For instance, the saturant imparts improved stiffness and strength during normal conditions and/or wet conditions when applied to cellulose filter papers at lower than normal add on levels.
  • the saturant may be applied at a concentration of 5 % to 25 % by weight in water in order to attain a binder content of 5% to 20% by weight in the dried finished paper.
  • the polyvinyl alcohol is present in an amount ranging from about 50% to 75% on a dry weight basis, and the formaldehyde resin of phenol is present in an amount from about 50% to 25% on a dry weight basis.
  • a particularly preferred composition is
  • the preferred binder content is approximately 10% by weight polymer in the dried finished paper.
  • This saturant may be applied to the paper in a variety of ways, including size press, gravure roll, and other techniques known to one of ordinary skill in the art.
  • the preferred method of application is by size press.
  • EXAMPLE 1 In this Example, saturants of the invention were prepared by first dissolving polyvinyl alcohol in water at 185°F, cooling with additional water, adjusting the pH and then adding formaldehyde resin. Solutions of the resins and polymers in Table 1 were prepared at various concentrations in water and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet.
  • Table 1 lists the measured resin content of each of the samples.
  • the resulting sheets were tested in a Perkin Elmer DMA-7 Dynamic Mechanical Analyzer in the bending beam mode using 20 mm x 5 mm samples cut in the machine direction of the paper. The actual span of the beam was 15 mm. The samples were run twice in the temperature range from about 25 to 240° C. The sheets were run the first time to characterize the cure rate of the material, and the second time to characterize the fully cured mechanical properties of the resin saturated sheet. The results are shown in Figure 1.
  • EXAMPLE 2 Solutions were prepared as specified in Table 2 and used to saturate a standard all cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 2 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 1, and the results are shown in Figure 2. Figure 2 shows that solution D5, having the highest PVOH/PhOH ratio of the solutions (75:25) performed best.
  • the sheets were cured. After curing the sheets 10 minutes at 300°F, the MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured before and after a 5 minute soak in a 2.5 % solution of a commercial liquid cleanser. The dry and wet physical properties are listed in Table 2.
  • EXAMPLE 3 Solutions were prepared as specified in Table 3 and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 3 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 2, and the results are shown in Figure 3.
  • the sheets were then cured for 10 minutes at 300°F.
  • the MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured again before and after a 5 minute soak in a 2.5% solution of a commercial liquid cleanser.
  • the dry and wet physical properties are also listed in Table 3.
  • EXAMPLE 4 Solutions were prepared as specified in Table 4 and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 4 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 1, and the results are shown in Figure 4. Again, after curing the sheets 10 minutes at 300°F, the MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured before and after a 5 minute soak in a 2.5% solution of a commercial liquid cleanser. The dry and wet physical properties are also listed in Table 4.
  • EXAMPLE 5 Solutions were prepared as specified in Table 5 with various urea and melamine formaldehyde resins. The prepared solutions were then used to saturate a standard all cellulose base paper in a laboratory size press. All solutions included Berchem 3009 magnesium chloride which functions as a catalyst for a cross linking reaction involving the formaldehyde urea and melamine resins. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in a finished "dry" sheet was determined by the weight gain of the sheet. The sheets were cured for 10 minutes at 300°F, and tested for MD tensile strength, MD stiffness and Mullen burst strength.
  • the sheets were also soaked for one minute in a 2.5 % solution of a commercial liquid cleanser; the resulting "wet” sheets were then retested for MD tensile strength, MD stiffness and Mullen burst strength. These physical properties of the "dry” and “wet” sheets are also included in Table 5.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)
  • Filtering Materials (AREA)

Abstract

An aqueous saturant for cellulose papers comprising a hydrolyzed polyvinyl alcohol and a formaldehyde resin, wherein the polyvinyl alcohol and the formaldehyde resin are substantially or completely dissolved in the system. The invention is also directed to methods for making and using the saturant. The system is also directed to paper, e.g., filter paper, made with the saturant as well as methods for making paper with the saturant.

Description

CELLULOSE FILTER PAPER SATURANT
FIELD OF THE INVENTION
The invention is directed to saturants for cellulose paper, and more particularly for saturants for cellulose filter paper.
BACKGROUND OF THE INVENTION
Cellulose filter papers are well known for many applications, such as automotive and heavy-duty oil and air filtration. Generally, they are produced by dispersing cellulose fibers, such as wood pulps, in water and filtering the fiber suspension through the continuous screen or wire of a paper machine. Conventionally, the resulting paper is dried once, then saturated with an aqueous or non-aqueous solution or suspension of polymer or resin, and finally dried again. Alternatively, while still wet, the freshly formed paper is saturated with the aqueous or non-aqueous solution or suspension of polymer or resin, and then dried only once. The dried, saturated paper may be then pleated, dimpled, or otherwise formed into a filter configuration, and possibly given a thermal cure to develop its final properties.
In order to perform adequately in automotive and heavy-duty (truck) oil and air filtration applications, the saturant must confer high Mullen burst strength, tensile strength, and particularly stiffness, under cured, wet, or elevated temperature conditions. In addition, since wood pulp is typically much less expensive than the polymers and resins comprising the saturant, it is economically desirable to achieve these mechanical properties using the lowest possible saturant content in the finished paper.
One convenient method of characterizing stiffness at a range of elevated temperatures is through the use of a Dynamic Mechanical Analyzer in bending beam mode, e.g. the "DMA-7" from Perkin Elmer. Such an instrument can measure the "in phase" bending modulus (elastic stiffness), and the "out of phase" loss modulus of the paper as the temperature is scanned from about room temperature to about 200°C. Previously known saturants typically have been low molecular weight formaldehyde resins of phenol, urea or melamine, dissolved in organic solvent or water. Other saturants have included aqueous dispersions of high molecular weight polymers such as polyvinyl acetate, polyvinyl chloride, or polyacrylic esters dispersed, but not dissolved, in water, or combinations of such polymers.
U.S. Pat. No. 4,461,858 (Adelman), for instance, discloses an acidic colloidal system for use in cellulose pulp slurries that includes a stable aqueous polyvinyl- alcohol/melamine-formaldehyde resin interaction product that comprises a polyvinyl alcohol polymer and a cationic melamine-formaldehyde resin colloid in a polyvinyl alcohol/ melamine formaldehyde resin acid colloid. U.S. Pat. No. 4,324,833 (Yau) discloses an acidic aqueous phenolic resin-urea wet process mat binder comprising an aqueous solution of a partially methylated melamine-formaldehyde resin and a polyvinyl alcohol, the aqueous solution having a pH within the range of from about 3.5 to about 6.5.
SUMMARY OF THE INVENTION
The invention is directed to a filter paper made with a saturant comprising a hydrolyzed polyvinyl alcohol and a formaldehyde resin, wherein the polyvinyl alcohol and the formaldehyde resin are substantially or completely dissolved in the system. The saturant is applied to a filter base paper, such as a cellulose base paper, such that the saturant forms about 5 % to 20% of the filter paper in the dried condition.
Preferably, the saturant used with the invention is an aqueous solution of a fully hydrolyzed high molecular weight polyvinyl alcohol and a water-soluble, low molecular weight, methylol-containing resin. The methylol-containing resin is preferably a formaldehyde resin of phenol, urea or melamine. The formaldehyde resin acts as a crosslinking agent for the polyvinyl alcohol. In one embodiment, the system includes a solution of polyvinyl alcohol and a formaldehyde resin of phenol having a pH within the range of from about 7.5 to about 10.5. An inorganic salt can be used as a catalyst to assist the crosslinking of urea and melamine resins. The invention is also directed to methods for making and using the water- based saturant.
BRIEF DESCRIPTION OF THE DRAWINGS
A more complete understanding of the present invention and the attendant advantages and features thereof will be more readily understood by reference to the following detailed description when it is considered in conjunction with the accompanying drawings, wherein:
FIG. 1 is a graph comparing the stiffness of cellulose paper made in accordance with the present invention, containing phenolic and polyvinyl alcohol resins, and cellulose paper made with either resin alone;
FIG. 2 is a graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention;
FIG. 3 is a graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention; and FIG. 4 is graph comparing the stiffness of cellulose paper made in accordance with various embodiments of the present invention.
DETAILED DESCRIPTION OF THE INVENTION
The invention is directed to a filter paper formed with a saturant that comprises of an aqueous solution of a hydrolyzed polyvinyl alcohol and a formalde- hyde resin, where the formaldehyde resin and the polyvinyl alcohol are completely or substantially dissolved.
The polyvinyl alcohol is present in a sufficient amount to enable the system to function as a saturant in cellulose papermaking operations. Preferably, the polyvinyl alcohol is present in the dried saturant composition in an amount that ranges from about 25 % to 95 % by weight. One of ordinary skill in the art will appreciate that other ranges are within the scope of the invention.
The polyvinyl alcohol is sufficiently hydrolyzed so that when it is combined with the formaldehyde resin and water, the formaldehyde resin crosslinks with the polyvinyl alcohol. Preferably, the polyvinyl alcohol is hydrolyzed at least about 98% . One of ordinary skill in the art, however, will appreciate that other ranges are within the scope of the invention. Suitable polyvinyl alcohols include Airvol® 103, 107, 125 and 165, available from Air Products Inc., and Elvanol® 70-06, 71- 30 and 90-50, available from duPont de Nemours & Co. The molecular weight of the polyvinyl alcohol is generally in the range of
10,000 to 190,000. In one embodiment, the molecular weight of the polyvinyl alcohol ranges from about 30,000 to about 50,000. One of ordinary skill in the art will appreciate that other polyvinyl alcohols having other molecular weight ranges may be used as well. The methylol containing formaldehyde resin of phenol, urea or melamine preferably is water soluble and has the functionality to act as a crosslinking or curing agent for polyvinyl alcohol resin. Preferably, the crosslinking resin has an average degree of polymerization of 1 to 3. Suitable formaldehyde resins of phenol include Arofene 72155, Arotap 8095 and Arofene DR 343, all available from Ashland Chemical Co. An exemplary formaldehyde resin of melamine includes
Parez 707, available from Cytec Industries. The formaldehyde resin is ordinarily present in a dry saturant composition in an amount from about 75 % to 5 % by weight, but other ranges are within the scope of the invention. Preferably, the formaldehyde resin is a resin of phenol. Suitable urea and melamine resins may also be used. Exemplary ureas and melamines include urea glyoxal formaldehyde condensate (BERSET 2300, available from Bercen, Inc. of Cranston, Rhode Island), and melamine formaldehyde resins such as BERSET 2003 (available from Bercen, Inc. of Cranston, Rhode Island), SEQUA MEL-80 (available from Sequa Chemicals, Inc. of Chester, South Carolina), AURAMEL 484, AURAMEL M-75, and AURAREZ 963 (available from
Sybron-Tanatex, Inc).
Optionally, an acid salt can be used as a catalyst to assist the crosslinking of urea and formaldehyde resins. Suitable acid salts are those formed from a weak base and a strong acid which, upon hydrolysis, yield a strong acid. Exemplary acid salts useful as catalysts in this invention include magnesium chloride, ammonium sulfate, ammonium nitrate, ammonium chloride, and aluminum chloride. A particularly preferred acid salt is magnesium chloride. Such an acid salt is generally used at a concentration in the range of about 2.5 to 7.5 wt. % solids in the saturant.
The saturant generally has a pH that is sufficiently high to maintain all or substantially all of the formaldehyde resin soluble. The pH of the saturant can be adjusted with a base to be within the range of 7.5 to 10.5. Suitable bases include a fixed base such as potassium or sodium hydroxide, or a fugitive base such as ammonium hydroxide. Other pH ranges are within the scope of the invention.
The water-based saturant of the invention may be made with conventional preparation techniques. Normally, the polyvinyl alcohol is dissolved in water at 185°F and cooled with additional water. The pH is adjusted, and the crosslinking resin is then added.
In use, the saturant imparts improved stiffness and strength to cellulose filter paper under a variety of papermaking conditions. For instance, the saturant imparts improved stiffness and strength during normal conditions and/or wet conditions when applied to cellulose filter papers at lower than normal add on levels. The saturant may be applied at a concentration of 5 % to 25 % by weight in water in order to attain a binder content of 5% to 20% by weight in the dried finished paper.
In a preferred saturant that is suitable for making cellulose filter paper, the polyvinyl alcohol is present in an amount ranging from about 50% to 75% on a dry weight basis, and the formaldehyde resin of phenol is present in an amount from about 50% to 25% on a dry weight basis. A particularly preferred composition is
65% polyvinyl alcohol and 35 % phenol formaldehyde resin, on a dry weight basis. The preferred binder content is approximately 10% by weight polymer in the dried finished paper.
This saturant may be applied to the paper in a variety of ways, including size press, gravure roll, and other techniques known to one of ordinary skill in the art.
The preferred method of application is by size press.
The invention is further described in the following illustrative examples. One of ordinary skill in the art will further appreciate that minor modifications may be made to the invention described herein without departing from its intended scope. All references noted herein are expressly incorporated by reference in their entirety. EXAMPLE 1 In this Example, saturants of the invention were prepared by first dissolving polyvinyl alcohol in water at 185°F, cooling with additional water, adjusting the pH and then adding formaldehyde resin. Solutions of the resins and polymers in Table 1 were prepared at various concentrations in water and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet.
Table 1 lists the measured resin content of each of the samples.
TABLE 1
The resulting sheets were tested in a Perkin Elmer DMA-7 Dynamic Mechanical Analyzer in the bending beam mode using 20 mm x 5 mm samples cut in the machine direction of the paper. The actual span of the beam was 15 mm. The samples were run twice in the temperature range from about 25 to 240° C. The sheets were run the first time to characterize the cure rate of the material, and the second time to characterize the fully cured mechanical properties of the resin saturated sheet. The results are shown in Figure 1.
EXAMPLE 2 Solutions were prepared as specified in Table 2 and used to saturate a standard all cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 2 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 1, and the results are shown in Figure 2. Figure 2 shows that solution D5, having the highest PVOH/PhOH ratio of the solutions (75:25) performed best.
Thereafter, the sheets were cured. After curing the sheets 10 minutes at 300°F, the MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured before and after a 5 minute soak in a 2.5 % solution of a commercial liquid cleanser. The dry and wet physical properties are listed in Table 2.
TABLE 2
EXAMPLE 3 Solutions were prepared as specified in Table 3 and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 3 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 2, and the results are shown in Figure 3.
The sheets were then cured for 10 minutes at 300°F. The MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured again before and after a 5 minute soak in a 2.5% solution of a commercial liquid cleanser. The dry and wet physical properties are also listed in Table 3.
TABLE 3
EXAMPLE 4 Solutions were prepared as specified in Table 4 and used to saturate a standard all-cellulose base paper in a laboratory size press. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in the finished sheets was determined by the weight gain of the sheet. Table 4 lists the measured resin pickup of each of the samples. The resulting sheets in the DMA-7 were tested again according to Example 1, and the results are shown in Figure 4. Again, after curing the sheets 10 minutes at 300°F, the MD Tensile Strength, Mullen Burst Strength, and MD Stiffness of the resulting sheets were measured before and after a 5 minute soak in a 2.5% solution of a commercial liquid cleanser. The dry and wet physical properties are also listed in Table 4.
TABLE 4
EXAMPLE 5 Solutions were prepared as specified in Table 5 with various urea and melamine formaldehyde resins. The prepared solutions were then used to saturate a standard all cellulose base paper in a laboratory size press. All solutions included Berchem 3009 magnesium chloride which functions as a catalyst for a cross linking reaction involving the formaldehyde urea and melamine resins. The resulting saturated sheets were dried on photo dryers, and the resulting resin content in a finished "dry" sheet was determined by the weight gain of the sheet. The sheets were cured for 10 minutes at 300°F, and tested for MD tensile strength, MD stiffness and Mullen burst strength. The sheets were also soaked for one minute in a 2.5 % solution of a commercial liquid cleanser; the resulting "wet" sheets were then retested for MD tensile strength, MD stiffness and Mullen burst strength. These physical properties of the "dry" and "wet" sheets are also included in Table 5.
TABLE 5

Claims

What is claimed is:
1. A filter paper, comprising: a cellulose base paper substrate; and a saturant formed from an aqueous solution of from about 25 % to 95 % by weight of polyvinyl alcohol and about 5% to 75% by weight of a formaldehyde resin, the saturant forming about 5% to 20% of the filter paper in a dried condition.
2. The filter paper of claim 1, wherein the polyvinyl alcohol is substantially fully hydrolyzed.
3. The filter paper of claim 1 , wherein the molecular weight of the polyvinyl alcohol is between about 10,000 and about 190,000.
4. The filter paper of claim 1, wherein the formaldehyde resin has an average degree of polymerization of 1 to 3 and is effective to crosslink the polyvinyl alcohol.
5. The filter paper of claim 1, wherein the formaldehyde resin is a methylol containing resin.
6. The filter paper of claim 1, wherein the formaldehyde resin is selected from the group consisting of phenol, urea and melamine.
7. A method of making a filter paper, comprising: providing a cellulose base paper substrate; forming an aqueous saturant having substantially dissolved therein approximately 25 % to 95 % by weight polyvinyl alcohol and approximately 5 % to 75 % by weight of a formaldehyde resin; and applying the saturant to the base paper in a quantity sufficient to achieve, upon drying, a filter paper having the saturant at about 5% to 20% by weight.
8. The method of claim 7, wherein the polyvinyl alcohol is substantially fully hydrolyzed.
9. The method of claim 7, wherein the molecular weight of the polyvinyl alcohol is between about 25,000 and about 190,000.
10. The method of claim 7, wherein the formaldehyde resin has an average degree of polymerization of 1 to 3 and is effective to crosslink the polyvinyl alcohol.
11. The method of claim 7, wherein the formaldehyde resin is a methylol containing resin.
12. The method of claim 7, wherein the formaldehyde resin is selected from the group consisting of phenol, urea and melamine.
13. The method of claim 7, wherein the formaldehyde resin is selected from the group consisting of urea formaldehyde resins and melamine formaldehyde resins.
14. The method of claim 13, further including providing with the aqueous saturant an inorganic salt catalyst at a concentration in the range of about 2.5 to 7.5 wt. % solids in the saturant.
15. The method of claim 14, wherein the inorganic salt catalyst is selected from the group consisting of magnesium chloride, ammonium sulfate, ammonium chloride, aluminum chloride, and ammonium nitrate. AMENDED CLAIMS
[received by the International Bureau on 1 February 1999 (01.02.99); new claims 16 - 21 added; remaining claims unchanged (3 pages)]
1. A filter paper, comprising: a cellulose base paper substrate; and a saturant formed from an aqueous solution of from about 25 % to 95 % by weight of polyvinyl alcohol and about 5 % to 75 % by weight of a formaldehyde resin, the saturant forming about 5% to 20% of the filter paper in a dried condition.
2. The filter paper of claim 1, wherein the polyvinyl alcohol is substantially fully hydrolyzed.
3. The filter paper of claim 1 , wherein the molecular weight of the polyvinyl alcohol is between about 10,000 and about 190,000.
4. The filter paper of claim 1, wherein the formaldehyde resin has an average degree of polymerization of 1 to 3 and is effective to crosslink the polyvinyl alcohol.
5. The filter paper of claim 1, wherein the formaldehyde resin is a methylol containing resin.
6. The filter paper of claim 1, wherein the formaldehyde resin is selected from the group consisting of phenol, urea and melamine.
AMENDED SHEET (ARTICLE 19)
7. A method of making a filter paper, comprising: providing a cellulose base paper substrate; forming an aqueous saturant having substantially dissolved therein approximately 25 % to 95 % by weight polyvinyl alcohol and approximately 5 % to 75 % by weight of a formaldehyde resin; and applying the saturant to the base paper in a quantity sufficient to achieve, upon drying, a filter paper having the saturant at about 5% to 20% by weight.
8. The method of claim 7, wherein the polyvinyl alcohol is substantially fully hydrolyzed.
9. The method of claim 7, wherein the molecular weight of the polyvinyl alcohol is between about 25,000 and about 190,000.
10. The method of claim 7, wherein the formaldehyde resin has an average degree of polymerization of 1 to 3 and is effective to crosslink the polyvinyl alcohol.
11. The method of claim 7, wherein the formaldehyde resin is a methylol containing resin.
12. The method of claim 7, wherein the formaldehyde resin is selected from the group consisting of phenol, urea and melamine.
13. The method of claim 7, wherein the formaldehyde resin is selected from the group consisting of urea formaldehyde resins and melamine formaldehyde resins.
14. The method of claim 13, further including providing with the aqueous saturant an inorganic salt catalyst at a concentration in the range of about 2.5 to 7.5 wt. % solids in the saturant.
AMENDED SHEET (ARTICLE 19)
15. The method of claim 14, wherein the inorganic salt catalyst is selected from the group consisting of magnesium chloride, ammonium sulfate, ammonium chloride, aluminum chloride, and ammonium nitrate.
16. A filter paper, comprising: a cellulose base paper substrate; and a saturant formed from an aqueous solution of from about 25 % to 95 % by weight of polyvinyl alcohol and about 5% to 75% by weight of a crosslinking agent, the saturant forming about 5% to 20% of the filter paper in a dried condition.
17. The filter paper of claim 16, wherein the crosslinking agent is a formaldehyde resin.
18. The filter paper of claim 17, wherein the formaldehyde resin is a methylol containing resin.
19. A method of making a filter paper, comprising: providing a cellulose base paper substrate; forming an aqueous saturant having substantially dissolved therein approximately 25 % to 95 % by weight polyvinyl alcohol and approximately 5 % to 75 % by weight of a crosslinking agent; and applying the saturant to the base paper in a quantity sufficient to achieve, upon drying, a filter paper having the saturant at about 5% to 20% by weight.
20. The method of claim 7, wherein the crosslinking agent is a formaldehyde resin.
21. The method of claim 19, wherein the formaldehyde resin is a methylol containing resin.
AMENDED SHEET (ARTICLE 19)
EP98944792A 1997-09-18 1998-09-08 Cellulose filter paper saturant Withdrawn EP1023493A4 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US5967597P 1997-09-18 1997-09-18
US59675P 1997-09-18
PCT/US1998/018624 WO1999014431A1 (en) 1997-09-18 1998-09-08 Cellulose filter paper saturant

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EP1023493A1 true EP1023493A1 (en) 2000-08-02
EP1023493A4 EP1023493A4 (en) 2001-10-24

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Publication number Priority date Publication date Assignee Title
US7138057B2 (en) * 2004-07-22 2006-11-21 Gore Enterprise Holdings, Inc. Filter media
CN103774503A (en) * 2014-01-16 2014-05-07 北京联飞翔科技股份有限公司 Filter paper for environmental-friendly automobile filter and preparation method of filter paper
CN109577006A (en) * 2018-10-30 2019-04-05 湖州南浔善琏墨艺工艺品有限公司 A kind of production method of textile auxiliary melamine formaldehyde resin

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AU9224598A (en) 1999-04-05
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EP1023493A4 (en) 2001-10-24
WO1999014431A1 (en) 1999-03-25

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