Gas steam reforming

Spath, P. and M. Mann, Life Cycle Assessment of Hydrogen Production via Natural Gas Steam Reforming, Technical Report, NREL, NREL/TP-570-27637,2000. 

Hydrogen availability is an important issue and refiners must be persuaded that gasification will prove to be as reliable a technology in the future as natural gas steam reforming is today. Many refineries produce sufficient pet coke to more than satisfy refinery hydrogen requirements. This would allow co-production of hydrogen and power or F-T liquids. 

In addition to natural gas, steam reformers can be used on light hydrocarbons such as butane and propane and on naphtha with a special catalyst. Steam reforming reactions are highly endothermic and need a significant heat source. Often the residual fuel exiting the fuel cell is burned to supply this requirement. Fuels are typically reformed at temperatures of 760 to 980°C (1,400 to 1,800°F). 

Mini Electricity Generation with SOFC. Development of 1 to 2 kW SOFC for application in distributed generation. The process for hydrogen production is natural gas steam reforming. 

In evaluation of the potential objects which are to define respective options to be taken into a consideration there are 99 objects. In this exercise we will focus our attention on the following hydrogen energy systems Fossil-Reforming-Intemal Combustion Engine System, Natural Gas Steam Reforming-Fuel Cell System, Nuclear Power-Electrolysis-Fuel Cell System, Solar Power-Electrolysis-Fuel Cell System, Wind Power-Electrolysis-Fuel Cell System, Biomass-Reforming-Gas Turbine System. 

The major units of the Aspen-HYSYS simulation for natural gas steam reforming based fuel cell system are presented in Figure 3. 

Synthesis Gas. There are three principal routes to synthesis gas steam reforming, partial oxidation, and coal gasifica-... 

Fortunately, efforts in addition to those of DOE are being implemented. The Tennessee Valley Authority is sponsoring the construction of an entrained flow gasifier to operate at elevated pressure and to provide synthesis gas to their small Ammonia Plant at Muscle Shoals, Alabama. Ironically, this ammonia plant was originally built using coke-fed water gas sets for synthesis gas production. It was converted to use natural gas steam reforming when cheap natural gas became available. The use of coal will provide valuable data on MBG production and purification. 

Natural gas steam reforming (with optional carbon capture and storage) ... 

Figure 3.3. Schematic representation of natural gas steam reforming...

This paper analyzes the sources of hydrogen for ammonia production, presents the feed and fuel requirements of the natural gas steam reforming process, estimates the relative economics of alternate feedstocks and briefly discusses the outlook for the ammonia industry. 

There are basically three processes in usage today for the production of hydrogen or ammonia synthesis gas Steam Reforming for the conversion of light hydrocarbons from natural gas to straight run naphthas Partial Oxidation for heavy hydrocarbons and coal and Electrolysis of Water. 

Natural Gas Steam Reforming Residuum Partial Oxidation Coal K-T Gasification New... 

By far the most widespread method of producing synthesis gas for methanol production today is via steam reforming of naphtha and lighter hydrocarbons. The process routes for both natural gas steam reforming and naphtha reforming are virtually identical, so we shall consider only natural gas reforming. Since the ICI LP methanol process was... 

Feedstock (process) Natural gas (steam reforming) Vacuum residue (partial oxidation) Coal (partial oxidation)... 

Spath, P., Mann, M. (2001). Life cycle assesment of hydrogen production via natural gas steam reforming. Revised USDoE contract report NREL/TP-570-27637, National Renewable Energy Lab., Golden, CO. 

M. Oertel, J. Schmitz. W. Weinrich. D. Jendryssek-Neuman, and R. Schulten. Hydrogen preparation by natural gas steam reforming with integrated hydrogen separation, Chem. Eng. Technol. 70 248 (1987). 

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