A method for forming a compressed gas and dispensing it to a compressed gas receiver, the method comprising the following steps: (a) providing a process fluid at a cryogenic temperature; (b) pressurizing the process fluid and feeding the pressurized process fluid at still a cryogenic temperature to a first heat exchanger; (c) providing a thermal fluid, such as for example D-Limonene, in a thermal fluid reservoir at a thermal fluid temperature above the cryogenic temperature of the pressurized process fluid; (d) forming the compressed gas from the pressurized process fluid, wherein forming the compressed gas includes heating the pressurized process fluid in the first heat exchanger by indirect heat exchange with the thermal fluid; (e) optionally, providing one or more compressed gas storage vessels and feeding compressed gas from the one or more compressed gas storage vessels to a dispenser; (f) feeding compressed gas formed in step (d) to the dispenser and/or the one or more compressed gas storage vessels, if present; (g) cooling compressed gas formed in step (d) and/or from the one or more compressed gas storage vessels, if present, by indirect heat exchange with the thermal fluid in a second heat exchanger and feeding the cooled compressed gas to the dispenser; and (h) dispensing the compressed gas via the dispenser to the compressed gas receiver; characterized in that (i) the first heat exchanger and the second heat exchanger are arranged in parallel with respect to the thermal fluid, and wherein a first pump feeds the thermal fluid of the thermal fluid reservoir through the first heat exchanger and a second pump feeds the thermal fluid of the thermal fluid reservoir through the second heat exchanger. (a) providing a process fluid at a cryogenic temperature; (b) pressurizing the process fluid and feeding the pressurized process fluid at still a cryogenic temperature to a first heat exchanger; (c) providing a thermal fluid, such as for example D-Limonene, in a thermal fluid reservoir at a thermal fluid temperature above the cryogenic temperature of the pressurized process fluid; (d) forming the compressed gas from the pressurized process fluid, wherein forming the compressed gas includes heating the pressurized process fluid in the first heat exchanger by indirect heat exchange with the thermal fluid; (e) optionally, providing one or more compressed gas storage vessels and feeding compressed gas from the one or more compressed gas storage vessels to a dispenser; (f) feeding compressed gas formed in step (d) to the dispenser and/or the one or more compressed gas storage vessels, if present; (g) cooling compressed gas formed in step (d) and/or from the one or more compressed gas storage vessels, if present, by indirect heat exchange with the thermal fluid in a second heat exchanger and feeding the cooled compressed gas to the dispenser; and (h) dispensing the compressed gas via the dispenser to the compressed gas receiver; characterized in that (i) the first heat exchanger and the second heat exchanger are arranged in parallel with respect to the thermal fluid, and wherein a first pump feeds the thermal fluid of the thermal fluid reservoir through the first heat exchanger and a second pump feeds the thermal fluid of the thermal fluid reservoir through the second heat exchanger.