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US3970625A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of urea-formaldehyde concentrates

Assignee: FERTILIZER INDUSTRIES Inc
•
Filing: 1974-11-14
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Granted: 1976-07-20
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Expires: 1994-11-14
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Abstract

Abstract A process for preparing an improved urea-formaldehyde concentrate particularly adapted for production of slow-release nitrogenous fertilizers. The improvement is achieved by accurately controlling the buffer strength and the degree of polymerization of the urea-formaldehyde concentrate within specified critical limits. The process can be operated to also produce a different urea-formaldehyde concentrate suitable for use in adhesives.

Inventors

  • 👤 William Percy Moore
  • 👤 James Earl Sansing
  • 👤 Harold Daniel Williamson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 09:09
CPC Classifications
C; C08; C08G; C08G12/00; C08G12/02; C08G12/04; C08G12/10; C08G12/12; C05; C05C; C05C9/00; C05C9/02; C09; C09J; C09J161/00; C09J161/20; C09J161/22; C09J161/24

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 252 words
In a process for the production of a stable, aqueous solution of urea-formaldehyde reaction products which comprises incorporating an aqueous formaldehyde solution containing from 30 to 50% by weight formaldehyde and no more than 0.02% by weight of formic acid based on the formaldehyde, with urea containing no more than 0.015% by weight of ammonia, in amount such that the resulting mixture contains a mol ratio of 4.4 to 7.3 mols of formaldehyde for every mol of urea, adjusting the pH of the reaction mixture thus prepared to within the range pH 8.8 to 9.5, thereafter heating said reaction mixture at temperatures in the range 50° to 60°C. for 30 to 60 minutes, and thereafter rapidly evaporating water from said mixture by distillation at temperatures in the range of about 45° to 60°C. under reduced pressure below atmopsheric, at which water is vaporized from the mixture until the liquid residue of the evaporation contains 60 to 90% by weight total solids calculated as formaldehyde and urea, the improvement which comprises: a. heat-treating a portion of said liquid residue of the evaporation for about 48 hours at a temperature of 45° to 50°C., thereby producing a urea-formaldehyde concentrate particularly suitable for manufacture of solid complete fertilizers containing water-insoluble, slow-release nitrogen; and b. cooling another portion of said liquid residue of the evaporation to ambient temperature and adding sufficient ammonia to said liquid residue to increase the buffer capacity to 12 to 16, thereby producing a urea-formaldehyde concentrate particularly suitable for manufacture of adhesives.
Claim 2
Dependent Claim 252 words
In a process for the production of a stable, aqueous solution of urea-formaldehyde reaction products which comprises incorporating an aqueous formaldehyde solution containing from 30 to 50% by weight formaldehyde and no more than 0.02% by weight of formic acid based on the formaldehyde, with urea containing no more than 0.015% by weight of ammonia, in amount such that the resulting mixture contains a mol ratio of 4.4 to 7.3 mols of formaldehyde for every mol of urea, adjusting the pH of the reaction mixture thus prepared to within the range pH 8.8 to 9.5, thereafter heating said reaction mixture at temperatures in the range 50° to 60°C. for 30 to 60 minutes, and thereafter rapidly evaporating water from said mixture by distillation at temperatures in the range of about 45° to 60°C. under reduced pressure below atmopsheric, at which water is vaporized from the mixture until the liquid residue of the evaporation contains 60 to 90% by weight total solids calculated as formaldehyde and urea, the improvement which comprises: a. heat-treating a portion of said liquid residue of the evaporation for about 48 hours at a temperature of 45° to 50°C., thereby producing a urea-formaldehyde concentrate particularly suitable for manufacture of solid complete fertilizers containing water-insoluble, slow-release nitrogen; and b. cooling another portion of said liquid residue of the evaporation to ambient temperature and adding sufficient ammonia to said liquid residue to increase the buffer capacity to 12 to 16, thereby producing a urea-formaldehyde concentrate particularly suitable for manufacture of adhesives.

References Cited (Backward Citations)

US2255027A Cited
US2652377A Cited
US2625524A Cited
US3092486A Cited
US3629176A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-07-20 1980-01-19 1980-07-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-07-20 1984-01-19 1984-07-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-07-20 1988-01-19 1988-07-20 $7700.00 Window Closed / Lapsed

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