A cold
energy recovery facility includes a
liquid hydrogen tank configured to store
liquid hydrogen a first circuit configured to circulate a first working medium, a second circuit configured to circulate a second working medium having a
freezing point higher than the first working medium, a first
turboexpander provided in the first circuit, the first
turboexpander being configured to be driven by the first working medium in a gas state, a second
turboexpander provided in the second circuit, the second turboexpander being configured to be driven by the second working medium in a gas state, a first
heat exchanger configured to vaporize the
liquid hydrogen from the liquid
hydrogen tank by heat exchange with the first working medium, a second
heat exchanger configured to vaporize the first working medium in a
liquid state by heat exchange with the second working medium, and a third
heat exchanger configured to vaporize the second working medium in a
liquid state by heat exchange with a heat medium, wherein the first circuit and the first turboexpander form a part of a first
thermodynamic cycle that uses the liquid
hydrogen as a low-temperature heat source in the first heat exchanger, and the second circuit and the second turboexpander form a part of a second
thermodynamic cycle that uses the first working medium as a low-temperature heat source in the second heat exchanger.