IP Library Granted Patent US 8,383,856
Granted Patent B2
US 8,383,856 · App. 11/817,186 · Granted Feb 26, 2013

Process for urea production and related plant

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Quick Facts
Patent No.
US 8,383,856
App. No.
11/817,186
Granted
Feb 26, 2013
Kind
B2
Abstract

A process for urea production from ammonia and carbon dioxide, made to react at a predetermined high pressure in an appropriate synthesis reactor ( 112 ), from the reaction between NH 3 and CO 2 being obtained a reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution, from which a recovery of ammonium carbamate and ammonia is carried out with their subsequent recycle to the synthesis reactor ( 112 ), said recovery from the reaction mixture taking place through operative steps of decomposition of the ammonium carbamate into NH 3 and CO 2 and of their stripping and a subsequent operative step of their recondensation into ammonium carbamate that is recycled to the synthesis reactor, the said reaction mixture obtained from the reaction between ammonia and carbon dioxide being pumped to the operative steps of decomposition and stripping.

Claims (9)

1. A process for urea production from ammonia and carbon dioxide, comprising the steps of:

feeding ammonia and carbon dioxide to an appropriate synthesis reactor;

reacting said ammonia and carbon dioxide at a predetermined pressure in said appropriate synthesis reactor obtaining a reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution;

recovering ammonium carbamate and ammonia from said reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution through the operative steps of:

decomposing and stripping the ammonium carbamate into NH 3 and CO 2;

feeding a minority portion of a gaseous flow comprising NH 3 and CO 2 from the operative steps of decomposition and stripping directly to the synthesis reactor; and

feeding a majority portion of said gaseous flow comprising NH 3 and CO 2 to a total recondensing step comprising recondensing said NH 3 and CO 2 in said majority portion into ammonium carbamate; and

recycling said recovered ammonium carbamate and ammonia to said synthesis reactor, said steps of reacting, recovering and recycling belonging to a same pressure loop;

wherein said reaction mixture comprising urea, ammonium carbamate and free ammonia in aqueous solution obtained in said synthesis reactor is pumped to the operative steps of decomposition and stripping using at least one canned rotor pump.

Assignments (2)
MERGER Recorded Dec 4, 2014
From: AMMONIA CASALE SA; UREA CASALE SA; METHANOL CASALE SA; CASALE CHEMICALS SA
To: CASALE SA
Reel/Frame 034533/0456 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 2, 2007
From: ROMITI, DOMENICO; STICCHI, PAOLO
To: UREA CASALE S.A.
Reel/Frame 020062/0487 →