Patent US4299654A successfully refreshed from Google Patents.
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
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 21:32
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)
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 |