Steam methane reforming has evolved over time from refinery operated, basic reformer furnaces with relatively poor efficiencies to today’s over the fence highly heat integrated offerings from industrial gas companies. Early on, reductions in natural gas usage per H2 has driven the industry to conducting analysis of heat exchanger network design. Requirements on export steam purities have further tested the ability of suppliers to provide steam turbine quality steam for customers at an incremental cost. Steam to carbon ratios and elimination of waste heat from the plant have generated further changes to design conditions and flowsheets. The advancement of purification technologies and hydrogen recovery have generated constraints on the reforming process design and operability. Environmental regulations create opportunity for improvement, as well as a challenge to the economic design of the plant. Fundamentals are at the heart of providing the insight necessary for generating technoeconomic solutions. The application of heat integration, use of CFD models, imaging, internet of things, and detailed optimization and process monitoring software have driven innovation and built our fleet.
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