← Back to Patent Explorer
US4299654A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing sized paper and cardboard with polyelectrolytes and epoxide-amine-polyamide reaction products

Assignee: BASF Corp
•
Filing: 1979-12-31
•
Granted: 1981-11-10
•
Expires: 1999-12-31
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for producing paper or cardboard sized in the pulp with epoxide-amine-polyamide reaction products is disclosed. This process comprises adding to the fibre suspension, which has a pH value of 5 to 8, (A) at least one water-soluble higher molecular polyelectrolyte, which is cationic if the pH value of the fibre suspension is 6.5 to 8 and anionic if the pH value of the fibre suspension is 5 to 7, followed by (B) at least one water-soluble or water-dispersible salt of an epoxide-amine-polyamide reaction product, and further processing the fibre suspension into the form of paper or cardboard.

Inventors

  • 👤 Hugo Tlach
  • 👤 Klaus-Dieter Leifels
  • 👤 Werner Mischler

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 02:40
CPC Classifications
D; D21; D21H; D21H17/00; D21H17/20; D21H17/33; D21H17/46; D21H17/54; D21H17/55; D21H23/00; D21H23/02; D21H23/04; D21H23/06; D21H23/08; D21H23/10; D21H23/76; D21H23/765

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 439 words
A process for producing paper or cardboard, sized in the pulp, on a paper machine, with an epoxide-amine-polyamide reaction product, comprising the steps of adding to the pulp fiber suspension, which has a pH value of 5 to 8, (A) a water-soluble high molecular weight polyelectrolyte, which is cationic if the pH value of the fiber suspension is 6.5 to 8 and anionic if the pH value of the fiber suspension is 5 to 7, followed by (B) A water-soluble or water-dispersible salt of an epoxide-amine-polyamide reaction product; wherein the cationic polyelectrolyte is selected from the group consisting of a cationically modified starch; cationically modified carbohydrates from guar flour or locust bean flour having molecular weights of 250,000 to 350,000; a cationally modified alginic acid having a degree of polymerization of 800 to 1200; a condensation product from dicyandiamide or cyanamide, formaldehyde and an ammonium halide; a cationic polyacrylic amide; an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine and an aliphatic dicarboxylic acid; an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine and dicyandiamide or cyanamide; and an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine, dicyandiamide or cyanamide, and an aliphatic dicarboxylic acid which is unesterified or esterified with alkanols; wherein the anionic polyelectrolyte is selected from the group consisting of a dimerized condensation product from a naphthalenesulphonic acid and formaldehyde; a copolymer from acrylic acid and acrylic amide; or an alkali metal salt or ammonium salt of alginic acid, having a degree of polymerization of 800 to 1200; wherein component (B) is a salt of the reaction product from (a) 1.0 epoxide group equivalent of a polyglycidyl ether of 2,2-bis(4'-hydroxyphenyl)-propane, (b) 0.4 to 0.6 amino group equivalent of a mono-fatty amine having 16 to 18 carbon atoms, and (c) 0.3 to 0.5 amino group equivalent of a polyalkeneaminopolyamide from (c') polymerised linoleic or linolenic acid, and (c") diethylenetriamine, triethylenetetramine or tetraethylenepentamine, in the form of an aqueous preparation having a solids content of 25 to 35 percent by weight and a pH value of 4 to 5; wherein component (A) is added in an amount which is 0.01 to 1 percent by weight, relative to the dry-fiber content of the fiber suspension; wherein component (B) is added in an amount which is 0.1 to 3 percent by weight, relative to the dry-fiber content of the fiber suspension; and wherein component (A) is added 8 to 80 seconds before the fiber suspension reaches the breastbox of the paper machine, and component (B) 3 to 50 seconds before the fiber suspension reaches the breastbox, however at least 5 seconds after the addition of component (A).
Claim 2
Dependent Claim 439 words
A process for producing paper or cardboard, sized in the pulp, on a paper machine, with an epoxide-amine-polyamide reaction product, comprising the steps of adding to the pulp fiber suspension, which has a pH value of 5 to 8, (A) a water-soluble high molecular weight polyelectrolyte, which is cationic if the pH value of the fiber suspension is 6.5 to 8 and anionic if the pH value of the fiber suspension is 5 to 7, followed by (B) A water-soluble or water-dispersible salt of an epoxide-amine-polyamide reaction product; wherein the cationic polyelectrolyte is selected from the group consisting of a cationically modified starch; cationically modified carbohydrates from guar flour or locust bean flour having molecular weights of 250,000 to 350,000; a cationally modified alginic acid having a degree of polymerization of 800 to 1200; a condensation product from dicyandiamide or cyanamide, formaldehyde and an ammonium halide; a cationic polyacrylic amide; an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine and an aliphatic dicarboxylic acid; an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine and dicyandiamide or cyanamide; and an epichlorohydrin adduct of a reaction product from a polyalkylenepolyamine, dicyandiamide or cyanamide, and an aliphatic dicarboxylic acid which is unesterified or esterified with alkanols; wherein the anionic polyelectrolyte is selected from the group consisting of a dimerized condensation product from a naphthalenesulphonic acid and formaldehyde; a copolymer from acrylic acid and acrylic amide; or an alkali metal salt or ammonium salt of alginic acid, having a degree of polymerization of 800 to 1200; wherein component (B) is a salt of the reaction product from (a) 1.0 epoxide group equivalent of a polyglycidyl ether of 2,2-bis(4'-hydroxyphenyl)-propane, (b) 0.4 to 0.6 amino group equivalent of a mono-fatty amine having 16 to 18 carbon atoms, and (c) 0.3 to 0.5 amino group equivalent of a polyalkeneaminopolyamide from (c') polymerised linoleic or linolenic acid, and (c") diethylenetriamine, triethylenetetramine or tetraethylenepentamine, in the form of an aqueous preparation having a solids content of 25 to 35 percent by weight and a pH value of 4 to 5; wherein component (A) is added in an amount which is 0.01 to 1 percent by weight, relative to the dry-fiber content of the fiber suspension; wherein component (B) is added in an amount which is 0.1 to 3 percent by weight, relative to the dry-fiber content of the fiber suspension; and wherein component (A) is added 8 to 80 seconds before the fiber suspension reaches the breastbox of the paper machine, and component (B) 3 to 50 seconds before the fiber suspension reaches the breastbox, however at least 5 seconds after the addition of component (A).
Claim 3
Dependent Claim 96 words
A process according to claim 1, in which there is added as component (A) at a pH value of the fiber suspension of 6.5 to 8: a condensation product from dicyanamide, formaldehyde and ammonium chloride; a cationic polyacrylic amide, having a density of about 100 kg/m 3 and a dynamic viscosity at 20° C. of 5000 to 7000 mPa.s (Brookfield spindle 4, 20 rpm); a cationically modified galactomannan from guar flour having a substitution degree of 0.10 to 0.15; or a maize starch or potato starch cationically modified with a propylene oxide containing quaternary ammonium groups.
Claim 4
Dependent Claim 26 words
A process according to claim 1, in which the pH value of the fiber suspension is adjusted to 5 to less than 7 with aluminium sulfate.
Claim 5
Dependent Claim 115 words
A process according to claim 1, in which there is added as component (B) an aqueous preparation of a salt of an epoxide-amine-polyamide reaction product, which is produced in a water-soluble aliphatic alcohol or ether having 1 to 10 carbon atoms, as an inert solvent from a polyglycidyl ether having an epoxide content of 5 to 5.5 equivalents per kilogram as component (a), and a mono-fatty amine and a polyalkyleneaminopolyamide each having an amino group content of 3 to 4 amino group equivalents per kilogram as components (b) and (c), respectively, the pH value of this preparation being adjusted to 4 to 5 by means of an alkanecarboxylic acid having 1 to 3 carbon atoms.
Claim 6
Dependent Claim 20 words
A process according to claim 1, in which the fiber suspension has a Schopper-Riegler freeness value of 20° to 45°.
Claim 7
Dependent Claim 31 words
A process according to claim 1, in which the pH value of the fiber suspension is adjusted with kaolin to 5 to 7, or with calcium carbonate to 7 to 8.
Claim 8
Dependent Claim 27 words
A process according to claim 1, in which the fiber suspension contains sulfite pulp from the wood of conifers, sulfate pulp from beechwood and mechanical wood pulp.
Claim 9
Dependent Claim 24 words
A process according to claim 1, in which the fiber suspension contains sulfite pulp from the wood of conifers and sulfate pulp from beechwood.

References Cited (Backward Citations)

US3392085A Cited
US3709847A Cited
JPS4924162A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-11-09 1985-05-11 1985-11-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-11-09 1989-05-11 1989-11-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-11-09 1993-05-11 1993-11-10 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag