U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Method for the production of urea and purification of water

Patent 4314077 Issued on February 2, 1982. Estimated Expiration Date: Icon_subject December 15, 2000. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

3120563

3826815

3876696

3922222

Method of recovering unreacted ammonium carbamate in urea synthesis
Patent #: 3944605
Issued on: 03/16/1976
Inventor: Inoue ,   et al.

Integrated urea-ammonia process
Patent #: 4012443
Issued on: 03/15/1977
Inventor: Bonetti

Process for preparing urea
Patent #: 4036878
Issued on: 07/19/1977
Inventor: Kaasenbrood ,   et al.

Method of recovering unreacted materials and heat in urea synthesis
Patent #: 4053507
Issued on: 10/11/1977
Inventor: Inoue ,   et al.

Method for the condensation of carbammate in urea-synthesis installations
Patent #: 4082797
Issued on: 04/04/1978
Inventor: Zardi, et al.

Treatment of water vapor generated in concentrating an aqueous urea solution Patent #: 4207256
Issued on: 06/10/1980
Inventor: Inoue ,   et al.

Inventors

Assignee

Application

No. 06/216303 filed on 12/15/1980

US Classes:

564/70, With decomposition of by-product ammonium carbamate (i.e., decomposition of HNH-COO-HHNHH)564/72In plural stages

Examiners

Primary: Hearn, Brian E.

Attorney, Agent or Firm

International Classes

C07C 273/00 (20060101)
C07C 273/04 (20060101)
C02F 1/02 (20060101)
C02F 11/08 (20060101)
C02F 9/00 (20060101)
C02F 11/06 (20060101)

Foreign Application Priority Data

1976-09-09 IT

Abstract

In a urea producing method by synthesis, the improvement which consists in feeding liquid ammonia in excess to the reactor so that a urea solution which contains ammonium carbamate is produced, the carbamate is decomposed in a high-pressure decomposer and the stripping agent is an inert, oxygen-containing gaseous stream, the carbamate decomposition products are sent to a high pressure condenser and ammonium carbamate is formed, whereafter the carbamate is separated from the inerts and the solution of urea coming from the high-pressure decomposer is fed to a medium-pressure decomposer which is fed through its bottom with inerts. The heat for operating the medium-pressure decomposer is a hot condensate from the high-pressure-decomposer-heating steam, and the products of decomposition of the carbamate coming from the medium-pressure decomposer are sent to a medium-pressure condenser together with a solution of ammonium carbonate coming from the low-pressure sections of the installation. Virtually pure, nonpolluting waters can be discharged from the installation.

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