Techno-economic prospects of small-scale membrane reactors in a future hydrogen-fuelled transportation sector

Abstract

The membrane reactor is a novel technology for the production of hydrogen from natural gas. It promises economic small-scale hydrogen production, e.g. at refuelling stations and has the potential of inexpensive CO 2 separation. Four configurations of the membrane reactor have been modelled with Aspen plus to determine its thermodynamic and economic prospects. Overall energy efficiency is 84% HHV without H 2 compression (78% with compression up to 482 bar). The modelling results also indicate that by using a sweep gas, the membrane reactor can produce a reformer exit stream consisting mainly of CO 2 and H 2 O (490% mol) suited for CO 2 sequestration after water removal with an efficiency loss of only 1% pt. Reforming with a 2 MW membrane reactor (250 unit production volume) costs 14 $/GJ H 2 including compression, which is more expensive than conventional steam reforming+compression (12 $/GJ). It does, however, promise a cheap method of CO 2 separation, 14 $/t CO 2 captured, due to the high purity of the exit stream. The well-towheel chain of the membrane reactor has been compared to centralised steam reforming to assess the trade-off between production scale and the construction of a hydrogen and a CO 2 distribution infrastructure. If the scale of centralised hydrogen production is below 40 MW, the trade-off could be favourable for the membrane reactor with small-scale CO 2 capture (18 $/GJ including H 2 storage, dispensing and CO 2 sequestration for 40 MW SMR versus 19 $/GJ for MR). The membrane reactor might become competitive with conventional steam reforming provided that thin membranes can be combined with high stability and a cheap manufacturing method for the membrane tubes. Thin membranes, industrial utility prices and larger production volumes (i.e. technological learning) might reduce the levelised hydrogen cost of the membrane reactor at the refuelling station to less than 14 $/GJ including CO 2 sequestration cost, below that of large-scale H 2 production with CO 2 sequestration

Membranes in Energy Systems with CO 2 Capture

“…Their results demonstrated that the Pd metal cost is insignificant when the thickness reaches approximately 5 mm. This is in agreement with other studies [13], and a logical result that also applies for small scale hydrogen production [14]. Figure 7.2 shows schematically three sequential WGS reactors and separation processes [15] after reforming of natural gas in low pressure hydrogen production.…”

“…SR-MR and WGS-MR are also technologies for the production of hydrogen on a smaller scale, for example for local filling stations [14,16]. This will not be further discussed in this chapter.…”

A comparison of electricity and hydrogen production systems with CO2 capture and storage—Part B: Chain analysis of promising CCS options

“…Decentralised electricity and hydrogen production is generally not considered due to the relatively high costs of CCS at such scales. Advanced concepts using fuel cells and membranes, however, offer the potential for low-cost CO 2 capture at relatively small scales [28]. Decentralised electricity production with CCS is of particular interest for the Netherlands given the large share of decentralised CHP units (circa 5 GW e of total installed capacity near 20 GW e in 2003) [29].…”

Impact of hydrogen onboard storage technologies on the performance of hydrogen fuelled vehicles: A techno-economic well-to-wheel assessment

“…For centrally produced hydrogen two modes of transportation are assessed; gaseous pipeline and liquid truck transport (Table 3). For the pipeline a large distribution pipeline, pressure 60 bar 16 over 13 Electricity and natural gas prices supplied from the grid are based on prices for small industrial users in the EU which correspond to the scales used in the analysis in this paper [28].…”