Method for cooling a plant for superconductive cables
A method for cooling a plant for superconductive cables is provided, where the plant includes two thermally insulated end closures ( 1, 2 ) and at least one thermally insulated, tubular cryostat ( 3 ) arranged between the end closures, in which at least one superconductive cable is arranged. Liquid nitrogen contained in a cooling agent supply is pumped by means of a pump ( 9 ) through a first end closure and the cryostat to a second end closure. At least one vacuum insulated tank ( 7 ) is used for the cooling agent supply, where the tank ( 7 ) contains nitrogen at operating temperature and out of which the nitrogen is pumped. For making available a quantity of liquid nitrogen necessary for operating the plant, the supply of liquid nitrogen contained in the tank ( 7 ) is supplemented during operation or is switched over to another tank ( 10 ) containing liquid nitrogen.
1. Method for cooling a plant for superconductive cables, which has a first thermally insulated end closure and a second thermally insulated end closure and at least one thermally insulated tubular cryostat arranged between the end closures, in which at least one superconductive cable is arranged in the cryostat, and in which liquid nitrogen is pumped by a pump through the first thermally insulated end closure and the cryostat to the second thermally insulated end closure, said method comprising the steps of:
installing a first vacuum insulated tank proximal to the first thermally insulated end closure;
connecting the vacuum insulated tank via a thermally insulated pipeline to the first thermally insulated end closure;
connecting said pump to the thermally insulated pipeline;
installing a second tank and connecting said second tank to the first thermally insulated end closure;
filling operating temperature liquid nitrogen into said first and second tanks;
supplying said operating temperature liquid nitrogen to said plant from said first vacuum insulated tank, wherein said liquid nitrogen is pumped out of the first vacuum insulated tank to said first end closure through said thermally insulated pipeline, then flows into said at least one thermally insulated tubular cryostat and then to said second thermally insulated end closure,
refilling liquid nitrogen into the first vacuum insulated tank in time intervals during operation of said plant or supplementing the liquid nitrogen contained in the first vacuum insulated tank, by supplying liquid nitrogen from the second vacuum insulated tank containing liquid nitrogen, for making available a quantity of liquid nitrogen required for operating the plant,
wherein the liquid nitrogen that gradually warmed when flowing to the second thermally insulated end closure, is returned from the second thermally insulated end closure into said first vacuum insulated tank through a thermally insulated pipe, said returned liquid nitrogen evaporates within the first vacuum insulated tank producing cold gas,
employing said cold gas for cooling the plant components contained in the end closures, and
mounting, for maintaining a predeterminable pressure level in the plant, a pressure control valve in the thermally insulated pipe in front of an inlet of the first vacuum insulated tank.