Abstract

The use of biogas as feedstock for hydrogen production was widely proposed in the literature in the last years as a strategy to reduce anthropogenic carbon emissions. However, its lower heating value compared to natural gas hampers the revamping of existing reforming plants. The use of composite carbon molecular sieve membranes for biogas upgrading (CO2 removal from biogas) was investigated experimentally in this work. In particular, ideal perm-selectivities and permeabilities above the Robeson plot for CO2/CH4 mixtures have been obtained. These membranes show better performances compared to polymeric membranes, which are nowadays commercialized for CO2 separation in natural gas streams. Compared to polymeric membranes, carbon membranes do not show deactivation by plasticization when exposed to CO2, and thus can find industrial application. This work was extended with a techno-economic analysis where carbon membranes are installed in a steam methane reforming plant. Results have been first validated with data from literature and show that the use of biogas increases the costs of hydrogen production to a value of 0.25 €/Nm3 compared to the benchmark technology (0.21 €/Nm3). On the other hand, the use of biogas leads to a decrease in carbon emissions up to 95%, thus the use of biogas for hydrogen production is foreseen as a very interesting alternative to conventional technologies in view of the reduction in the carbon footprint in the novel technologies that are to be installed in the near future.

Highlights

  • Since the industrial revolution, the CO2 concentration in the atmosphere has experienced a continuous increase associated to the extensive use of fossil fuel resources for power generation, and many of the observed changes in the climate are consequence of these greenhouse gases emissions

  • The use of biogas as feedstock for hydrogen production was widely proposed in the literature in the last years as a strategy to reduce anthropogenic carbon emissions

  • Ideal perm-selectivities and permeabilities above the Robeson plot for CO2/CH4 mixtures have been obtained. These membranes show better performances compared to polymeric membranes, which are nowadays commercialized for CO2 separation in natural gas streams

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Summary

Introduction

The CO2 concentration in the atmosphere has experienced a continuous increase associated to the extensive use of fossil fuel resources for power generation, and many of the observed changes in the climate are consequence of these greenhouse gases emissions. The overall conversion efficiency of this biofuel into electricity is about 10–16% This efficiency is rather low as compared to the efficiency achieved with natural gas for electricity generation, which is normally in the range of 39% for large gas turbines and up to 58% in Combined Cycle Gas Turbine processes (CCGT) [7,8]. This is associated to the much lower energy content in the biogas, which could be around 20–60% of the lower heating value of a natural gas feedstock depending on the concentration of CH4

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