In cryogenic piping transportation systems, cryogenic liquids evaporate and produce vapor due to differences in internal and external temperatures, which is typically referred to as boil-off gas. This causes an increase in pressure inside the systems; consequently, the vaporized cryogenic liquids reduce the amount of transportation and can damage the pipelines. To decrease the amount of vaporized cryogenic liquids, a vacuum insulated pipe with an inner line and an outer jacket has been used widely. The inner line transports the cryogenic liquid, whereas the vacuum space between the inner and outer pipes provides insulation to minimize heat transfer and boil-off gas. The vacuum pressure in the vacuum space is referred to as the degree of vacuum, which affects the heat transfer characteristics significantly. Furthermore, selecting an appropriate degree of vacuum at the early stage of design for the vacuum insulated pipe is difficult. In this study, a heat transfer analysis is performed for a cryogenic vacuum insulated pipe comprising inner and outer pipes, vacuum space, and multilayer insulation thin films. The working fluid used is liquid nitrogen, and heat fluxes in the vacuum insulated pipe are evaluated based on the change in the degree of vacuum, such as 1, 10⁻¹, 10⁻², 10⁻³, and 10⁻⁴ Experiments are performed using a prototype of the vacuum insulated pipe, and the obtained results are compared with the results of the heat transfer analysis. In addition, the availability of the vacuum insulated pipe for liquid hydrogen transportation is reviewed.