Gas purification by adsorption of hydrogen sulfide
Hydrogen sulfide is removed from a hydrogen rich gas stream using adsorbents having a low loss of carbon dioxide adsorption capacity upon sulfur loading including high purity silica gels, titania or highly cross-linked, non-chemically reactive resins. The adsorbents may be used to adsorb both carbon dioxide and hydrogen sulfide, or may be used as a guard bed upstream of a separate carbon dioxide adsorbent.
1. Apparatus for use in purifying hydrogen by removal of impurities from a hydrogen feed gas, said apparatus comprising a flow path for said feed gas containing an adsorbent for hydrogen sulfide, said flow path having a feed direction, and said adsorbent for hydrogen sulfide comprises a silica gel having an SiO 2 content of at least 99.2% and has a sulfur deposition rate of less than 0.04 wt % S per day H 2 S exposure when continuously exposed to a 1% H 2 S dry gas at 20° C. for seven (7) days, and an adsorbent for carbon dioxide in said flow path downstream in said feed direction from said adsorbent for hydrogen sulfide.
2. Apparatus as claimed in claim 1 , further comprising a gasifier for steam reforming of a carbon source and a water gas shift reactor for producing said hydrogen feed gas connected in said flow path and located upstream with respect to said feed direction from said adsorbent for hydrogen sulfide.
3. Apparatus as claimed in claim 2 , further comprising an air separation unit (ASU) for producing separate flows of nitrogen and of oxygen respectively, said flow of oxygen being directed to said gasifier.
4. Apparatus as claimed in claim 3 , further comprising a power generating combustor connected to receive hydrogen purified by said adsorbent for hydrogen sulfide and said adsorbent for carbon dioxide and further connected to receive said flow of nitrogen to act as a diluent for combustion of said purified hydrogen in said combustor.
5. Apparatus as claimed in claim 3 , wherein said flow of nitrogen is connected to flow counter current to said feed direction as a regeneration gas flow through said adsorbent for hydrogen sulfide and further comprising a flow controller for selecting between feed gas flow through said adsorbent for hydrogen sulfide and regeneration gas flow therethrough.