Preparation of aqueous nonwoven binders of low formaldehyde emission on curing based on urea, formaldehyde and glyoxal

• US 5,017,641 A
• Filed: 05/02/1989
• Issued: 05/21/1991
• Est. Priority Date: 05/07/1988
• Status: Expired due to Fees

• Current Assignee: BASF AG (BASF SE)
• Original Assignee: BASF AG (BASF SE)
• Inventors: Flory, Klaus, Neubach, Werner, Kempter, Fritz E., Matejcek, Franz
• Primary Examiner(s): Foelak, Morton
• Assistant Examiner(s): KRASS, FREDERICK F
• Application Number:
  US07/347,437
• Time in Patent Office: 749 Days
• Field of Search: 524/598, 528/245
• US Class Current: 524/598
• CPC Class Codes: C08G 12/12 Ureas; Thioureas

Abstract

Aqueous nonwoven binders that give reduced formaldehyde emission on curing are based on condensation products of urea or derivatives thereof, formaldehyde and glyoxal in a molar ratio, based on the solid binder, of from 1.5 to 2.5 moles of formaldehyde and from 0.1 to 0.5 mole of glyoxal per mole of the total urea used.

Claims

1. A process for preparing an aqueous nonwoven binder of reduced formaldehyde emission on curing that is based on a condensation product of urea, a urea derivative, or a mixture thereof, formaldehyde and glyoxal in a molar ration, based on the solid binder, of from 1.5 to 2.5 moles of formaldehyde and from 0.1 to 0.5 mole of glyoxal per mole of the total urea used, which comprises the following sequential steps:

(A) condensing urea and formaldehyde in an aqueous solution in a molar ratio of 1;

(2.0-10) at a pH of from 1 to 10 and at from 20°

to 95°

C., then

(B) condensing the condensate of step (A) with glyoxal in a molar ratio of urea;

glyoxal of 1;

(0.1-0.5) at a pH of from 2.0 to 6.8 and at from 60°

to 100°

C. and then

(C) further reacting the condensate of step (B) with such an amount of urea, 2-oxo-hexahydro-1,3,5-triazine or a 2-oxo-4,6-dialkyl-hexahydro-1,3,5,-triazine in an amount, based on the solid binder, of from 2 to 20% by weight, based on the unsubstituted urea or the urea used for preparing the triazine, at a pH of from 5.0 to 8.5 and at from 20°

to 100°

C., and with up to 70% by weight of glyoxal, based on the total amount of glyoxal, so as to produce the stated overall molar ratio.

2. A process as claimed in claim 1, wherein in stage (A) the uronyl-free or -containing condensate is reacted with a primary alkylamine.

3. A process as claimed in claim 1, wherein triethanolamine is used to set the pH in stage (A).

4. A process as claimed in claim 1, wherein the glyoxal used in stages (B) and (C) is added portionwise.

5. A process as claimed in claim 1, wherein in stage (C) the reaction product of dimethylolurea and ammonia is used.

6. A process as claimed in claim 1, wherein in stage (C) urea is used.

7. A process as claimed of claim 1, wherein the pH in the stage (C) is set with triethanolamine, a reaction product of triethanolamine and urea or a 2-oxo-5-alkylhexahydro-1,3,5-triazine.