| dc.description.abstract | Emerging technologies in CO[subscript 2] air capture, high temperature electrolysis, microchannel
catalytic conversion, and Generation IV reactor plant systems have the potential to create
a shipboard liquid fuel production system that will ease the burdened cost of supplying
fuel to deployed naval ships and aircraft. Based upon historical data provided by the
US Navy (USN), the tanker ship must supply 6,400 BBL/Day of fuel (JP-5) to
accommodate the highest anticipated demand of a carrier strike group (CSG).
Previous investigation suggested implementing shipboard a liquid fuel production system
using commercially mature processes such as alkaline electrolysis, pressurized water
reactors (PWRs), and methanol synthesis; however, more detailed analysis shows that
such an approach is not practical. Although Fischer-Tropsch (FT) synthetic fuel
production technology has traditionally been designed to accommodate large economies
of scale, recent advances in modular, microchannel reactor (MCR) technology have to
potential to facilitate a shipboard solution. Recent advances in high temperature coelectrolysis
(HTCE) and high temperature steam electrolysis (HTSE) from solid oxide
electrolytic cells (SOECs) have been even more promising. In addition to dramatically
reducing the required equipment footprint, HTCE/HTSE produces the desired synthesis
gas (syngas) feed at 75% of the power level required by conventional alkaline electrolysis
(590 MW[subscript e] vs. 789 MW[subscript e]). After performing an assessment of various CO[subscript 2] feedstock sources, atmospheric CO[subscript 2] extraction using an air capture system appears the most promising option. However, it was determined that the current air capture system design
requires improvement. In order to be feasible for shipboard use, it must be able to capture
CO[subscript 2] in a system only ¼ of the present size; and the current design must be modified to
permit more effective operation in a humid, offshore environment. Although a PWR power plant is not the recommended option, it is feasible. Operating with a Rankine cycle, a PWR could power the recommended liquid fuel production plant with a 2,082 MW[superscript th] reactor and 33% cycle efficiency. The recommended option uses a molten salt-cooled advanced high temperature reactor (AHTR) coupled to a supercritical carbon dioxide (S-CO[subscript 2]) recompression cycle operating at 25.0 MPa and 670°C. This more advanced 1,456 MWth option has a 45% cycle efficiency, a 42% improvement over the PWR option. In terms of reactor power heat input to JP-5 combustion heat output, the AHTR is clearly superior to the PWR (31% vs. 22%).
In order to be a viable concept, additional research and development is necessary to
develop more compact CO[subscript 2] capture systems, resolve SOEC degradation issues, and
determine a suitable material for the molten salt/S-CO[subscript 2] heat exchanger interface. | en_US |
