Method for modernizing the synthesis loop of an ammonia plant
View Patent ↗A method for modernizing an ammonia synthesis loop ( 1 ) with a first converter ( 10 ) and a second converter ( 11 ) in series, the first converter ( 10 ) comprises a cartridge with one or more catalyst beds, the second converter ( 11 ) comprises a catalyst bed in direct contact with said vessel, the method comprising the steps of removing the second converter, and boosting the first converter by replacing the cartridge with a high-efficiency cartridge comprising a plurality of adiabatic catalyst beds and inter-bed heat exchangers, or an isothermal catalyst bed, and by reducing the concentration of inerts in said first converter.
1. A method for modernizing the ammonia synthesis loop of an ammonia plant, wherein:
said loop comprises a converter system with at least a first converter and a second converter in series, the second converter receiving a process stream from the first converter,
said first converter comprises a cartridge with one or more catalyst beds,
said second converter comprises a pressure vessel and a catalyst bed enclosed in flow distributors associated directly to said vessel,
a purge rate containing inert gases is taken from the synthesis loop,
the method comprising the steps of:
removing said second converter from the loop;
revamping the first converter by at least the step of replacing said cartridge with a high-efficiency cartridge comprising a plurality of adiabatic catalyst beds and inter-bed heat exchangers, or
revamping the first converter by at least the step of replacing said cartridge with a new cartridge comprising an isothermal catalyst bed, and
increasing the purge rate of the loop.
2. The method according to claim 1 , where said high-efficiency cartridge comprising a plurality of axial/radial flow or radial-flow catalyst beds with intermediate cooling by a combination of quench and heat exchangers.
3. The method according to claim 2 , where said high-efficiency cartridge comprising three axial-radial flow beds with intermediate cooling with two intermediate heat exchangers between the beds.
4. The method according to claim 1 , where said new cartridge comprising an isothermal catalyst bed with a heat exchanger immersed in said bed.
5. The method according to claim 4 , where said heat exchanger immersed in the bed being a tube or plate heat exchanger.
6. The method according to claim 1 , wherein the purge rate containing inerts being increased by at least 30%.
7. The method according to claim 1 , wherein the purge rate containing inerts being increased to obtain a concentration of inerts in the first converter less than 10% molar.
8. The method according to claim 1 , wherein:
the first converter of the ammonia synthesis loop comprises a cartridge with two radial-flow catalyst beds and an interbed heat exchanger;
the second converter comprises one catalyst bed enclosed in flow panels mounted directly on the inside wall of the vessel of said second converter; and
the high efficiency cartridge is a three-bed axial-radial flow cartridge with two intermediate quench heat exchangers between the beds.