| |
| |
Co-Production of Hydrogen and Methanol
|
|
Steam reforming of a light hydrocarbon feed yields syngas that is then split into two streams: a first stream which can be fed to a unit to make methanol, and a second stream which can be fed along with steam to make a shifted syngas comprising H2 and CO2 that is separated by PSA to give high purity
|
| |
|
![]() |
| |
| |
CO-Rich Syngas Production Process
|
|
Expanding off a solid foundation in the hydrogen production area, Air Products has designed an energy-efficient process for producing CO-rich syngas. This reforming process uses intermediate injection of reactants to allow for low temperature steam without coking.
|
| |
|
![]() |
|
|
![]() |
|
|
![]() |
| |
| |
Liquid Phase Methanol (LPMEOH™)
|
|
Thanks to pioneering Liquid Phase Technologies from Air Products, syngas can be converted to methanol (MEOH) via the LPMEOH™ process in a way that reduces capital and operating costs, improves productivity and offers operating flexibility for changing conditions in your plant.
|
| |
|
![]() |
| |
| |
Making CO-Rich Syngas and High Purity H2
|
|
This is a method to produce simultaneously hydrogen and syngas that has a H2/CO ratio <2.5. It is accomplished by removing CO2 from the effluents of primary and secondary reformers and then increasing CO2 feed amounts to a secondary reformer.
|
| |
|
![]() |
|
|
![]() |
| |
| |
Vent Stream for O2 Combustion
|
|
A method has been developed for oxygen-enhanced combustion that increase productivity and fuel efficiency, while reducing flue gas volume and pollution emissions. The technology takes advantage of the oxygen-rich vent stream from nitrogen generation equipment which may also exist at a factory.
|
| |
|
![]() |
