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Canada (2 x 130,000 Nm3/h). More than 60 Uhde reformers have been constructed worldwide. , Dr. M. Michel, J. Zschommler (Uhde), Dr. M. Whysall and Dr. S. Vanheertum (UOP), “Large-scale hydrogen plants, Uhde and UOP’s experience,” AIChE 2003 Spring Meeting, New Orleans, March 30–April 3, 2003. , “Steam reformer based hydrogen plant optimization,”The International Conference HYFORUM 2000, Munich, Germany, September 2000. 9999 mole%. Impurities efficiently removed include: N2, CO, CH4, CO2, H2O, Ar, O2, C2– C8+, CH3OH, NH3, H2S and organic sulfur compounds.

71. Licensor: Costain Oil, Gas & Process Ltd. , using the Haldor Topsøe Convective Reformer (HTCR). 999+% without steam export. Description: The HTCR-based hydrogen plant can be tailor-made to suit the customer’s needs with respect to feedstock flexibility. In a typical plant, feedstock is first desulfurized. Subsequently, process steam is added, and the mixture is fed to the HTCR. Process gases are reacted in a water-shift reactor and purified by pressure swing absorption (PSA) unit to obtain product-grade hydrogen.

Proven extensively, the PFHEs are available from several vendors, which has a very positive effect on price and delivery time. A Dry natural gas Application: Natural gas liquefaction (LNG) process. Description: Liquefin process—Dry natural gas (A) enters the liquefaction train’s pre-cooling section (1) where it is cooled between –50°C and –80°C (–60°F and –110°F). The heat is exchanged with a mixed refrigerant in a bank of brazed aluminum plate-fin heat exchangers (PFHEs). The cooled feed stream is then sent outside the liquefaction train to fractionator (2) for condensate removal.

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Gas Processes Handbook by coll.


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