A cold energy recovery facility comprising: 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; and wherein the cold energy recovery facility is characterized in that it further comprises a working medium heater provided downstream of the second heat exchanger and upstream of the first turboexpander in the first circuit, the working medium heater being configured to heat the first working medium flowing through the first circuit. 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; and wherein the cold energy recovery facility is characterized in that it further comprises a working medium heater provided downstream of the second heat exchanger and upstream of the first turboexpander in the first circuit, the working medium heater being configured to heat the first working medium flowing through the first circuit.