Syngas (H2 + CO) is required to make a variety of products. Each of these syngas derivatives has a specific ratio of H2 to CO in the feed syngas that is optimal for its production. However, the H2:CO ratio produced is a function of the syngas process and the hydrocarbon feed. This ratio will not necessarily be optimal for downstream products. Therefore, some method for reducing the amount of hydrogen in the syngas is needed.

VaporSep®-H2 offers a simple method for separating H2 from syngas to adjust the H2:CO ratio. In a typical system, the feed gas is first cooled to remove condensable hydrocarbons, and then heated before entering the membrane. Hydrogen preferentially permeates through the membrane, producing a purified hydrogen “permeate” stream and a hydrogen-depleted “ratio-adjusted syngas” stream. This ratio adjustment may even produce high-purity CO for processes requiring it as a feed.
When syngas is used to produce chemicals such as methanol and ammonia, the synthesis loop must be purged continuously to avoid buildup of inert gases such as argon and methane. These purge streams are mainly syngas if the hydrogen in the purge stream can be purified, it has significant value for recycle to the process or for reuse in a nearby refinery or chemical plant.

VaporSep-H2 offers a simple method for separating H2 from synthesis purge streams. In a typical system, the feed gas is first cooled to remove condensable hydrocarbons, and then heated before entering the membrane. Hydrogen preferentially permeates through the membrane, producing a purified hydrogen “permeate” stream and a stream of concentrated inerts. The purified hydrogen is recompressed and recycled to the synthesis loop.
