The present disclosure describes a method for discharging a hydrogen storage system that is found in the annular space of a receiver tube, in particular for solar collectors, wherein the annular space is formed at least by an outer-lying tubular jacket and an inner-lying absorber tube of the receiver tube, and the outer-lying tubular jacket is joined by means of a wall to the absorber tube. The method is hereby characterized in that a first opening penetrating the tubular jacket or the wall is produced under a protective gas atmosphere, wherein protective gas enters through the first opening into the annular space, after which a process chamber with a connection for a vacuum pump is arranged in a gas-tight manner above the first opening, the receiver tube is evacuated through the first opening, and the first opening is subsequently sealed in a gas-tight manner.

The present disclosure describes a method for discharging a hydrogen storage system, which is found in the annular space of a receiver tube, in particular for solar collectors, wherein the annular space is formed between an outer-lying tubular jacket and an inner-lying absorber tube of the receiver tube, and the outer-lying tubular jacket is connected via a wall to the absorber tube in a gas-tight manner. The method is hereby characterized in that an opening penetrating the tubular jacket or the wall is produced, free hydrogen in the annular space is pumped out through the opening, and the opening is subsequently sealed. The disclosure further describes a device for implementing the method.

The invention relates to a method which comprises making a hole in a metallic support of an absorber tube, putting a vacuum pump in fluid communication with the chamber of the absorber tube by means of the hole, actuating the vacuum pump to generate a vacuum in the chamber until reaching a predetermined vacuum threshold, and introducing an inert gas inside the chamber and performing a plurality of sweeps with said inert gas, removing hydrogen from the chamber, allowing to thus reduce or remove the accumulation of hydrogen in said chamber, such that, as a result, at least part of the hydrogen absorption capacity of the getter material is recovered.

The invention relates to a method which comprises making a hole in a metallic support of an absorber tube, putting a vacuum pump in fluid communication with the chamber of the absorber tube by means of the hole, actuating the vacuum pump to generate a vacuum in the chamber until reaching a predetermined vacuum threshold, and introducing an inert gas inside the chamber and performing a plurality of sweeps with said inert gas, removing hydrogen from the chamber, allowing to thus reduce or remove the accumulation of hydrogen in said chamber, such that, as a result, at least part of the hydrogen absorption capacity of the getter material is recovered.

The invention relates to a method which comprises making a hole in a metallic support of an absorber tube, putting a vacuum pump in fluid communication with the chamber of the absorber tube by means of the hole, actuating the vacuum pump to generate a vacuum in the chamber until reaching a predetermined vacuum threshold, and introducing an inert gas inside the chamber and performing a plurality of sweeps with said inert gas, removing hydrogen from the chamber, allowing to thus reduce or remove the accumulation of hydrogen in said chamber, such that, as a result, at least part of the hydrogen absorption capacity of the getter material is recovered.

The invention relates to a method which comprises making a hole in a metallic support of an absorber tube, putting a vacuum pump in fluid communication with the chamber of the absorber tube by means of the hole, actuating the vacuum pump to generate a vacuum in the chamber until reaching a predetermined vacuum threshold, and introducing an inert gas inside the chamber and performing a plurality of sweeps with said inert gas, removing hydrogen from the chamber, allowing to thus reduce or remove the accumulation of hydrogen in said chamber, such that, as a result, at least part of the hydrogen absorption capacity of the getter material is recovered.

A system and method removes thermal decomposition components from biphenyl and/or diphenyl oxide-based heat transfer fluids. Light, volatile decomposition components including benzene, water, hydrogen and phenol leave the system for vapor recovery, chemical adsorption or thermal decomposition. Dimerized and polymerized heavy components such as biphenyl phenyl ether, terphenyl and related isomers are concentrated and recovered. The system can be a continuous, semi-continuous or batch operation. Solar electric plants employing the system can use solar field fluids and heating to operate the system during generator operation hours. A wash system operating at or near atmospheric pressure concentrates heavy thermal decomposition components while allowing removal of light, volatile decomposition components for separation from the majority of the thermal fluid components. Temperature-controlled condensation of the majority of the thermal fluid components allows collection of the thermal fluid, while allowing light, volatile decomposition components to be removed prior to vent processing.

A system and method removes thermal decomposition components from biphenyl and/or diphenyl oxide-based heat transfer fluids. Light, volatile decomposition components including benzene, water, hydrogen and phenol leave the system for vapor recovery, chemical adsorption or thermal decomposition. Dimerized and polymerized heavy components such as biphenyl phenyl ether, terphenyl and related isomers are concentrated and recovered. The system can be a continuous, semi-continuous or batch operation. Solar electric plants employing the system can use solar field fluids and heating to operate the system during generator operation hours. A wash system operating at or near atmospheric pressure concentrates heavy thermal decomposition components while allowing removal of light, volatile decomposition components for separation from the majority of the thermal fluid components. Temperature-controlled condensation of the majority of the thermal fluid components allows collection of the thermal fluid, while allowing light, volatile decomposition components to be removed prior to vent processing.

A system and method removes thermal decomposition components from biphenol and/or diphenyl oxide heat-transfer fluids. Light, volatile decomposition components including benzene, water, hydrogen and phenol leave the system for vapor recovery, chemical adsorption or thermal decomposition. Dimerized and polymerized heavy components such as biphenyl phenyl ether, terphenyl and related isomers are concentrated and recovered. The system can be a continuous, semi-continuous or batch operation. Solar electric plants employing the system can use solar field fluids and heating to operate the system during generator operation hours. A wash system operating at or near atmospheric pressure concentrates heavy thermal decomposition components while allowing removal of light, volatile decomposition components for separation from the majority of the thermal fluid components. Temperature-controlled condensation of the majority of the thermal fluid components allows collection of the thermal fluid, while allowing light, volatile decomposition components to be removed prior to vent processing.

A system and method removes thermal decomposition components from biphenol and/or diphenyl oxide heat-transfer fluids. Light, volatile decomposition components including benzene, water, hydrogen and phenol leave the system for vapor recovery, chemical adsorption or thermal decomposition. Dimerized and polymerized heavy components such as biphenyl phenyl ether, terphenyl and related isomers are concentrated and recovered. The system can be a continuous, semi-continuous or batch operation. Solar electric plants employing the system can use solar field fluids and heating to operate the system during generator operation hours. A wash system operating at or near atmospheric pressure concentrates heavy thermal decomposition components while allowing removal of light, volatile decomposition components for separation from the majority of the thermal fluid components. Temperature-controlled condensation of the majority of the thermal fluid components allows collection of the thermal fluid, while allowing light, volatile decomposition components to be removed prior to vent processing.