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US4205138A Expired / Lapsed US ⏱️ 0.0 years remaining

Polyurethane foams and elastomers prepared from low molecular weight polyhydroxyl compounds

Assignee: Bayer AG
•
Filing: 1979-05-10
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Granted: 1980-05-27
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Expires: 1999-05-10
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Abstract

Abstract This invention relates to an improved process for the production of a mixture of low molecular weight polyhydric alcohols, hydroxy aldehydes and hydroxy ketones by condensing formaldehyde hydrate in the presence of calcium hydroxide as catalyst and in the presence of compounds capable of enediol formation as co-catalyst. A formaldehyde-containing enediol formation as co-catalyst. A formaldehyde containing solution of the co-catalyst in water and, optionally, low molecular weight monohydric or polyhydric alcohols and/or relatively high molecular weight polyhydroxyl compounds is adjusted to a pH value of from 9 to 12, preferably from 9 to 10, by the addition of calcium hydroxide at a temperature of from 80° to 110° C., preferably from 90° to 105° C., so that condensation of the formaldehyde hydrate is initiated. An aqueous formalin solution and/or paraformaldehyde dispersion containing from 20 to 65%, by weight, of formaldehyde and calcium hydroxide are then introduced in such a quantity that the reaction mixture is maintained at a pH value of from 7.5 to 9.5, preferably from 8 to 9, at a temperature of from 80° to 110° C., preferably from 90° to 105° C. The concentration of formaldehyde is maintained at from 0.5 to 10%, by weight, preferably from 1.2 to 6%, by weight, based on the reaction mixture as a whole, throughout the condensation reaction. Finally, the residual quantity of formaldehyde, amounting to from 0.5 to 10%, by weight, is optionally removed by further condensation at pH values below 7 or by reaction with other compounds that are reactive with formaldehyde hydrate.

Inventors

  • 👤 Hanns P. Muller
  • 👤 Kuno Wagner

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 05:53
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/48; C08G18/4829; C07; C07C; C07C29/00; C07C29/132; C07C29/136; C07C29/14; C07C29/141; C07C29/143; C07C29/145; C07C45/00; C07C45/61; C07C45/67; C07C45/68; C07C45/70; C07C45/71; C07C45/72; C07C45/75; C07H; C07H3/00; C07H3/02; C07H3/04; C08G18/30; C08G18/32; C08G18/3203; C08G18/3206; C08G18/3209; C08G18/42; C08G18/4297

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 228 words
A process for the preparation of cellular or non-cellular polyurethane resins by the reaction of (a) polyisocyanates with (b) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 32 to 400, optionally (c) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 400 to 10,000, and optionally (d) blowing agents, catalysts and other known additives, characterized in that the compounds used as component (b) are low molecular weight polyhydroxyl compounds prepared by condensing formaldehyde hydrate in the presence of calcium hydroxide as catalyst and in the presence of compounds capable of enediol formation as co-catalyst, adjusting a formaldehyde-containing solution of the co-catalyst in water to a pH value of from 9 to 12 by the addition of calcium hydroxide at a temperature of from 80° to 110° C. so that condensation of the formaldehyde hydrate is started, and then adding to this reaction mixture, (1) an aqueous formalin solution and/or paraformaldehyde dispersion containing from 20 to 65%, by weight, of formaldehyde, and (2) calcium hydroxide at such a rate that the reaction mixture is maintained at a pH value of from 7.5 to 9.5 at a temperature of from 80° to 110° C., the concentration of formaldehyde being maintained at from 0.5 to 10%, by weight, based on the total reaction mixture, throughout the condensation reaction.
Claim 2
Dependent Claim 228 words
A process for the preparation of cellular or non-cellular polyurethane resins by the reaction of (a) polyisocyanates with (b) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 32 to 400, optionally (c) compounds containing at least 2 active hydrogen atoms and having a molecular weight of from 400 to 10,000, and optionally (d) blowing agents, catalysts and other known additives, characterized in that the compounds used as component (b) are low molecular weight polyhydroxyl compounds prepared by condensing formaldehyde hydrate in the presence of calcium hydroxide as catalyst and in the presence of compounds capable of enediol formation as co-catalyst, adjusting a formaldehyde-containing solution of the co-catalyst in water to a pH value of from 9 to 12 by the addition of calcium hydroxide at a temperature of from 80° to 110° C. so that condensation of the formaldehyde hydrate is started, and then adding to this reaction mixture, (1) an aqueous formalin solution and/or paraformaldehyde dispersion containing from 20 to 65%, by weight, of formaldehyde, and (2) calcium hydroxide at such a rate that the reaction mixture is maintained at a pH value of from 7.5 to 9.5 at a temperature of from 80° to 110° C., the concentration of formaldehyde being maintained at from 0.5 to 10%, by weight, based on the total reaction mixture, throughout the condensation reaction.

References Cited (Backward Citations)

US2224910A Cited
US2334761A Cited
US2269935A Cited
US2760983A Cited
GB745557A Cited
US2775621A Cited
US3243414A Cited
US3378527A Cited
US3876706A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-05-27 1983-11-26 1984-05-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-05-27 1987-11-26 1988-05-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-05-27 1991-11-26 1992-05-27 $7700.00 Window Closed / Lapsed

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