Patent EA-001299-B1 (EA)
Title: Improved process for the synthesis of urea and equipment therefor
Inventor: KOJIMA YASUHIKO
IPC: B01J10/00
Filed: 1998-12-17
Abstract: 1. A urea synthesis process comprising reacting ammonia with carbon dioxide at a urea synthesis temperature and a urea synthesis pressure in a urea synthesis column, heating the resultant urea synthesis solution comprising urea, unreacted ammonia, unreacted carbon dioxide and water in a stripper at a pressure substantially equal to the urea synthesis pressure while bringing said solution into contact or no contact with at least part of feed carbon dioxide or feed ammonia to separate said unreacted ammonia and said unreacted carbon dioxide as a gaseous mixture of ammonia, carbon dioxide and water, treating further the urea synthesis solution containing unseparated unreacted ammonia and unreacted carbon dioxide to obtain urea, separately introducing the gaseous mixture separated in said stripper into a condenser having a tubular cooler to bring the mixture into contact with an absorption medium under cooling, thereby condensing said gaseous mixture, and recycling the thus-obtained condensate to the urea synthesis column, wherein sites, that are to be in contact with said condensate, of the joints of cooling tubes and a tube plate in said condenser are enveloped with liquid ammonia or a solution rich in ammonia to prevent corrosion of said sites due to said condensate. 2. The process as claimed in claim 1, wherein said sites of the joints of the tube plate and the cooling tubes are covered with a baffle plate through which said tubes penetrate with minute clearances held inbetween, and at least part of feed liquid ammonia is supplied to the space between said tube plate and said baffle plate so that said space is filled with liquid ammonia or a solution rich in ammonia. 3. The process as claimed in claim 1 or 2, wherein said condenser is installed on or above said urea synthesis column, and said condensate is allowed to flow down by gravity through a piping connecting the top part of said condenser with the bottom part of said urea synthesis column. 4. The process as claimed in claim 1,2 or 3 wherein said condensate is pressurized by means of an ejector driven by feed liquid ammonia so that it is recycled to the urea synthesis column. 5. A urea synthesis apparatus comprising a urea synthesis column (A) for reacting ammonia and carbon dioxide at a urea synthesis pressure and a urea synthesis temperature, a stripper (C) for separating unreacted ammonia and carbon dioxide by heating the urea synthesis solution from said urea synthesis column (A) at a pressure substantially equal to the urea synthesis pressure, a condenser (B) having a multi-tubular cooler for condensing the unreacted ammonia and carbon dioxide from said stripper (C) by bringing them into contact with an absorption medium, and a piping for introducing the condensate obtained in said condenser (B) into the bottom part of the urea synthesis column (A), wherein said multi-tubular cooler has a baffle plate (4) which covers, sites, that are to be protected from corrosion, of the joints of a tube plate (2) and cooling tubes (3) and through which said cooling tubes (3) penetrate with minute clearances held inbetween, and has an inlet nozzle or nozzles for supplying liquid ammonia to the space between said tube plate (2) and said baffle plate (4). 6. The apparatus as claimed in claim 5, wherein said stripper (C) has, at the bottom part thereof, an inlet nozzle or nozzles for supplying at least part of feed ammonia or carbon dioxide as a stripping agent. 7. The apparatus as claimed in claim 5, wherein said condenser (B)is installed on or above said urea synthesis column (A),and said piping from said condenser (B) to said urea synthesis column (A) is for allowing a condensate from said condenser(B) to flow down by gravity to the bottom part of said urea synthesis column (A). 8. The apparatus as claimed in claim 5, wherein the piping for introducing said condensate from said condenser (B) to said urea synthesis column (A) has an ejector (G) for pressurizing said condensate, driven by feed liquid ammonia.