Hydrogen and Syngas Production and Purification Technologies 2009
DOI: 10.1002/9780470561256.ch2
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Catalytic Steam Reforming Technology for the Production of Hydrogen and Syngas

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Cited by 29 publications
(27 citation statements)
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References 271 publications
(173 reference statements)
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“…Methane is an established source of downstream chemical products in addition to its obvious use as a fuel. The key, initial stage is the splitting of methane into syngas (carbon monoxide and hydrogen gases) by steam reforming, providing an invaluable platform onto countless other chemicals that are of interest as solvents and other functional chemicals [ 118 , 119 ]. Alternatively gasification processes can be applied to biomass to directly produce syngas without the need for biological treatments or the intermediate methane [ 120 ].…”
Section: Methane and Syngasmentioning
confidence: 99%
“…Methane is an established source of downstream chemical products in addition to its obvious use as a fuel. The key, initial stage is the splitting of methane into syngas (carbon monoxide and hydrogen gases) by steam reforming, providing an invaluable platform onto countless other chemicals that are of interest as solvents and other functional chemicals [ 118 , 119 ]. Alternatively gasification processes can be applied to biomass to directly produce syngas without the need for biological treatments or the intermediate methane [ 120 ].…”
Section: Methane and Syngasmentioning
confidence: 99%
“…These two options, however, require expensive H2 which, in turn, is preferentially produced worldwide using non-renewable feedstock's, being the steam methane reforming the most 3 developed and commercialized technology [8]. In this regard, these routes should be viable in view of CO2 emissions abatement only when H2 is produced from renewable resources, such as water electrolysis.…”
Section: Introductionmentioning
confidence: 99%
“…On the other hand, from Equation (3) and (4), one can anticipate that the effect of (1 −˛) is the same as 2 . In other words, a new Thiele modulus could be defined as = k(1 −˛)/D e , so that the above equation described in literature for non-poisoned catalysts reverts into Equation (5) At this stage it is worth analysing the concentration profiles given by Equation (5), shown in Figure 2 for extreme˛values, that is 10% and 90% of the poisoned catalyst.…”
Section: Concentration Profilesmentioning
confidence: 89%
“…Table 1 shows some examples of catalyst deactivation in largescale industrial processes. Apart from those interesting cases reported by Hagen, [1] other noteworthy examples refer to the Nibased catalysts (typically supported on alumina) that are used in the steam reforming of natural gas that perform in excess of 5 years (>50 000 h) of continuous operation [2] or those employed for ethylbenzene dealkylation in the UOP Isomar process (4-5 years without regeneration). [3] Types of catalyst deactivation are diverse and include sintering, fouling and poisoning.…”
Section: Introductionmentioning
confidence: 99%