Power
systems with
high shares of fluctuating renewable energies
require the management of power demand conforming to availability
as well as storage for periods of low generation. The production of
synthetic natural gas with power-to-gas (PtG) plants offers a solution
to both problems: flexibility in plant capacity and long-term energy
storage. Hence, we study the dynamic operability of a methanation
plant as a key part of the PtG process. At first, the effect of catalyst
dilution on maximum temperature and load range in the main reactor
is investigated. Subsequently, the dynamic and load change behavior
of the plant are studied by analyzing load ramps and operation according
to a pre-defined load profile. For a complete picture, experiments
and simulations are evaluated at the same time. Results show that
the dilution of a commercial catalyst with inert material is an effective
measure to reduce the maximum temperature in a methanation plant without
compromising product quality. This holds true for dynamic operation,
where the plant shows an excellent capability of following fast load
changes. Dividing the main reactor into three zones of different catalytic
activity is practical from an operator’s point of view and
applicable to existing plants to improve flexibility.