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 . <EOS>