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US3674847A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for urea production in combination with ammonia synthesis

Assignee: Stamicarbon BV
•
Filing: 1969-03-17
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Granted: 1972-07-04
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Expires: 1989-03-17
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Abstract

Abstract A process for the production of urea from ammonia and carbon dioxide, combined with the preparation of ammonia, is disclosed wherein ammonium carbamate in the urea solution produced is removed from said urea solution by subjecting the urea solution to two stripping stages. The first stripping stage uses the urea synthesis starting gas, which contains hydrogen, nitrogen and carbon dioxide. The second stripping stage, which is at substantially the same pressure as the first stripping stage, uses a gas containing at least one of the components needed in the ammonia synthesis. This second stripping gas is substantially free of ammonia and carbon dioxide. The disclosed process has the advantage, compared to prior processes, that the stripping gases need not be compressed at relatively high temperatures.

Inventors

  • 👤 Petrus J C Kaasenbrood
  • 👤 Petrus J M Van Nassau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 21:08
CPC Classifications
C; C07; C07C; C07C273/00; C07C273/02; C07C273/10; C01; C01C; C01C1/00; C01C1/02; C01C1/04; C01C1/0405; C01C1/0488; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 109 words
a secondary stripping stage operated at substantially the same pressure level as said primary stripping stage wherein said first urea solution is stripped with a secondary stripping gas, said secondary stripping gas being substantially free of ammonia and carbon dioxide and selected from the group consisting of hydrogen, nitrogen,, or combinations thereof, yielding a second urea solution of further reduced ammonium carbamate and free ammonia content and a second stripping off-gas containing carbon dioxide and ammonia, and delivering said second stripping off-gas to said carbamate condensing stage, wherein ammonia and carbon dioxide are removed from said first and said second stripping off-gases and recycled to said urea synthesis reactor.
Claim 2
Dependent Claim 32 words
The process of claim 1 wherein said secondary stripping gas is at least a portion of said synthesis gas substantially free of ammonia and carbon dioxide obtained from said carbamate condensing stage.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein said synthesis gas containing hydrogen and carbon dioxide additionally contains nitrogen.
Claim 4
Dependent Claim 15 words
The process of claim 1 wherein said secondary stripping gas comprises essentially hydrogen and nitrogen.
Claim 5
Dependent Claim 23 words
The process of claim 1 wherein said primary stripping stage and said secondary stripping stage are carried out at substantially the urea-synthesis pressure.
Claim 6
Dependent Claim 14 words
The process of claim 5 wherein said urea-synthesis pressure is at least 300 atmospheres.

References Cited (Backward Citations)

NL6704780A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1975-07-04 1976-01-03 1976-07-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1979-07-04 1980-01-03 1980-07-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1983-07-04 1984-01-03 1984-07-04 $7700.00 Window Closed / Lapsed

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