Incremental hydrogen production from an existing steam/natural gas reformer
In some aspects, a method for incremental hydrogen production includes separating in a first Pressure Swing Absorption (PSA) system an existing reformer synthesis gas product stream into a first hydrogen stream and a first waste stream. The first waste stream is compressed to at least 40 bar to produce a compressed waste stream. Water is removed from the compressed waste stream to produce a dried waste stream. Carbon dioxide is removed from the dried waste stream to produce a remaining waste stream, and the removed carbon dioxide is at least 85% of carbon dioxide in the existing reformer synthesis gas product stream. A second PSA system separates the remaining waste stream into a second hydrogen stream and a second waste stream, and the second hydrogen stream comprises at least 11% of hydrogen from the existing reformer synthesis gas product stream.
1. A method for incremental hydrogen production, comprising:
separating in a first Pressure Swing Absorption (PSA) system an existing reformer synthesis gas product stream into a first hydrogen stream and a first waste stream;
compressing the first waste stream to at least 40 bar to produce a compressed waste stream;
removing water from the compressed waste stream to produce a dried waste stream;
removing carbon dioxide from the dried waste stream to produce a remaining waste stream, wherein the removed carbon dioxide is at least 85% of carbon dioxide in the existing reformer synthesis gas product stream;
separating in a second PSA system the remaining waste stream into a second hydrogen stream and a second waste stream, wherein the second hydrogen stream comprises at least 11% of hydrogen from the existing reformer synthesis gas product stream; and
passing the second waste stream to a reformer furnace as fuel gas.
2. A system for incremental hydrogen production, comprising:
a first Pressure Swing Absorption (PSA) system configured to separate an existing reformer synthesis gas product stream into a first hydrogen stream and a first waste stream;
a compressor configured to compress the first waste stream to at least 40 bar to produce a compressed waste stream;
a drier configured to remove water from the compressed waste stream to produce a dried waste stream;
a low-temperature separator configured to remove carbon dioxide from the dried waste stream to produce a remaining waste stream, wherein the removed carbon dioxide is at least 85% of carbon dioxide in the existing reformer synthesis gas product stream;
a second PSA system configured to separate the remaining waste stream into a second hydrogen stream and a second waste stream, wherein the second hydrogen stream comprises at least 11% of hydrogen from the existing reformer synthesis gas product stream; and
a conduit configured to pass the second waste stream to a reformer furnace as fuel gas.