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Short construction schedule: Excluding the compressor and membrane/ PSA delivery, expected to be 4– 8 months based on unit capacity. Installations: Two commercial. References: “Noncryogenic N2-rejection process gets Hugoton field test,” Oil & Gas Journal, May 24, 1993. Gas Research Institute Topical Report GRI-93/0448, “Field Test Performance Evaluation of the Mehra Process for Nitrogen Rejection from Natural Gas,” February 1994. US Patent Nos. 4,623,371; 4,680,042; 4,832,718; 4,883,514; 5,224,350; 5,462,583; 5,551,972.

The desulfurized feed is mixed with process steam at an optimized steam/carbon ratio. The desulfurized feed is mixed with process steam at an optimized steam/carbon ratio, superheated to 500– 650°C and fed to the Lurgi Reformer. The feed/steam mixture passing the reformer tubes is converted at 800 –900°C by presence of a nickel catalyst to a reformed gas containing H2, CO2, CO, CH4 and undecomposed steam. The reformed gas is cooled to approximately 33°C in a reformed gas boiler. The Lurgi Reformer is a top-fired reformer with a low number of burners and low heat losses, almost uniform wall temperature over the entire heated tube length and low NOx formation by very accurate fuel and combustion air equipartition to the burners.

And S. W. Madsen, “Advanced reforming technologies for hydrogen production,” Hydrocarbon Engineering, December/January 1997/1998. Gøl, J. , “Options for hydrogen production,” HTI Quarterly, Summer 1995. CLICK HERE to e-mail for more information home proce ss cat egories proce ss index company index MEDAL membrane (hydrogen) Application: Hydrogen recovery and purification from refinery, petrochemical and ammonia plant gas streams. ��������������������������� ������������������������� Feed: Refinery streams include hydroprocessing unit purge streams, catalytic reformer offgas, fuel gas streams and steam reformer (feed preparation/product purification).

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