Patented concept to hugely increase the capacity of an existing ammonia plant.
Plant capacity can be increased up to 100% of the present plant production.
Energy saving higher than 0.5Gcal/MTNH3.
The philosophy originally developed for the Superevamp® is based on two main key points:
- Front-end debottlenecking with significant reduction of specific gas flow, by reduction of the S/C ratio and removal of N2, allowing to increase the net NG flow without significant increase in section pressure drop
- Inert-free synloop operation, which allow increasing the per-pass conversion and therefore the production rate with limited increase in the circulation flow
The reduction of the steam/carbon ratio, is made possible by the introduction of the pre-reformer, and allows maintaining the overall mass flow rate in reforming section, despite a plant capacity increase of more than (usually) 35÷40%.
Downstream the primary reformer, the existing secondary reformer is modified to ATR by replacing air feed with pure O2 feed. The removal of N2 from all the following sections generates a reduction in specific gas flow by more than 40% with respect to current operation, which together with the lower S/C makes it possible to significantly increase the feed flow without affecting the overall pressure drop.
Upstream the HTS a quench with water allows reducing of the temperature and achieving a proper S/CO ratio at the shift section inlet. The existing high temperature and low temperature shift converter are revamped with axial-radial internals in order to treat the increased gas flow rate.
To recover the increased amount of CO2, the CO2 removal section is revamped (addition of an upstream pre-wash section could be required); after methanation, final gas purification is performed in the a new LNW where all the inerts are removed from the process gas generating a virtually inert-free hydrogen stream which can be directly fed to the syngas compressor.
Inside the synthesis loop the main converter is revamped by installation of an additional ammonia converter to enhance the ammonia synthesis. No modifications are envisaged in refrigeration sections.
The plant capacity can be increased 100% compared to the current plant daily throughput.
Casale experience and know-how are of course at your disposal to design the most suitable Superevamp® scheme. Get in touch with us if you wish to explore how we can help you take your ammonia plant into the future – reliably – efficiently and in a sustainable way!
Technologies
- Ammonia converter revamping
- Ammonia washing unit
- AmoMax® Casale ammonia catalyst
- Autothermal Reformer
- Axial-radial shift converter
- Casale Cooling Module
- Casale static refrigeration package
- Casale-ARVOS process gas coolers
- Clean/Dirty CO2 separation
- CO2 removal section revamping
- Condensate treating towers
- Electric start-up heater
- Hot-wall Ammonia Converter revamping
- HP Hydrogen Recovery Unit
- Isothermal Ammonia Converter (IAC)
- Lithium-Bromide cooling circuit
- MP steam export to higher industrial steam header pressure
- Revamping with TPR®
- Secondary reformer burner