IP Library Granted Patent US 9,024,020
Granted Patent B2
US 9,024,020 · App. 13/806,157 · Granted May 5, 2015

Horizontal high-pressure melamine reactor

Inventors: Arne Schadt (Pasching, AT); Robert Schlesinger (Linz, AT)
Assignee: Casale SA
B01J10/005C07D251/62B01J3/042B01J4/002B01J10/00B01J19/006B01J19/24B01J2219/00083B01J2219/00101B01J2219/00768B01J2219/182B01J2219/1943C07D251/60
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Quick Facts
Patent No.
US 9,024,020
App. No.
13/806,157
Granted
May 5, 2015
Kind
B2
Abstract

A high-pressure melamine reactor is provided. The high-pressure melamine reactor comprising at least one horizontal reactor body having a bottom and a top side with at least one dome integrally formed on the top side of the reactor body. The at least one horizontal reactor body comprises at least two compartments separated by at least one baffle, in particular an overflow baffle. The at least one dome is solely located above at least one of the compartments serving as melamine synthesis unit, wherein the at least one compartment serving as melamine synthesis unit comprises at least one heating element.

Claims (23)

1. A high-pressure melamine reactor comprising:

at least one horizontal reactor body having a bottom and a top side with at least one dome integrally formed on the top side of the reactor body, wherein

the at least one horizontal reactor body comprises at least two compartments separated by at least one baffle,

the at least one dome is solely located above at least one of the compartments serving as a melamine synthesis unit,

the at least one compartment serving as a melamine synthesis unit comprises at least one heating element, and

the at least one dome comprises at least one inlet for urea melt, at least one outlet for offgas and at least one heat exchanger.

2. The reactor according to claim 1 , wherein the at least one dome serves as a scrubber unit.

3. The reactor according to claim 1 , wherein a second of the compartments serves as a stripping unit.

4. The reactor according claim 1 , wherein the dimensions of the dome correspond to the dimensions of the compartment serving as the melamine synthesis unit such that the dome covers fully or at least partially said compartment.

5. The reactor according to claim 1 , wherein the dome has a diameter between 1 m and 5 m, or between 1 m and 3 m, or between 1 m and 2 m.

6. The reactor according to claim 1 , wherein the at least one dome has a height between 1 and 10 m, or between 3 and 8 m, or between 4 and 6 m.

7. The reactor according to claim 1 , wherein a second of the least two compartments serves as stripping unit and comprises at least one inlet for gaseous ammonia and at least one outlet for melamine melt.

8. The reactor according to claim 1 , wherein the at least one compartment serving as melamine synthesis unit comprises at least one half of the volume of the horizontal reactor and a second compartment serving as stripping unit comprises up to one half of the volume of the horizontal reactor.

9. The reactor according to claim 1 , wherein the height of the at least one baffle is at least one third of the reactor body height.

10. A process for obtaining melamine from urea at high pressure in a reactor according to claim 1 comprising the steps of:

feeding liquid urea into the at least one dome of the reactor,

heating the liquid urea in the at least one compartment of the reactor,

separating the offgases from thus obtained melamine melt by releasing the offgases through the at least one dome

transferring the melamine melt obtained in the at least one compartment over the at least one baffle into at least one second compartment of the reactor;

feeding gaseous ammonia into the at least one second compartment of the reactor, and

releasing the thus stripped melamine melt from the at least one second compartment.

11. The process according to claim 10 , wherein a temperature in the reactor is between 330 and 450° C. and a pressure is between 5 and 20 MPa.

12. The process according to claim 10 , wherein a temperature of the gaseous ammonia feed into the second compartment of the reactor is above 330° C.

Assignments (3)
MERGER Recorded Apr 2, 2015
From: UREA CASALE SA
To: CASALE SA
Reel/Frame 035319/0389 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 30, 2013
From: BOREALIS AGROLINZ MELAMINE GMBH
To: UREA CASALE SA
Reel/Frame 031857/0810 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 21, 2013
From: SCHADT, ARNE; SCHLESINGER, ROBERT
To: BOREALIS AGROLINZ MELAMINE GMBH
Reel/Frame 030057/0514 →
Priority Claims (1)
EP 10167186 · Jun 24, 2010 · regional
Continuity (1)
Related Publication 20130172555A1 · Jul 4, 2013