A variable-liftability device includes a pressurized hermetically sealed chamber accepting a gas of density lower than the density of the air; a mixer arranged at least partially inside the hermetically sealed chamber and configured to introduce air into the hermetically sealed chamber.

An airship and its long-term floating capacity maintenance method are disclosed. The airship includes an airship capsule and a pod at bottom. A renewable fuel cell and a water tank communicated with each other are arranged in the pod. The water tank is provided with a water inlet connected with a filling aircraft outside the airship. The airship capsule is provided with a solar cell. The interior of the airship capsule is provided with a hydrogen storage bag. The solar cell is electrically connected with the renewable fuel cell. The renewable fuel cell can use electric energy provided by the solar cell to electrolyze water provided by the filling aircraft into hydrogen and supplement the hydrogen to the hydrogen storage bag. The airship can supplement hydrogen to the airship capsule by electrolyzing water to reduce the phenomenon of insufficient gas in the airship capsule.

An airship and its long-term floating capacity maintenance method are disclosed. The airship includes an airship capsule and a pod at bottom. A renewable fuel cell and a water tank communicated with each other are arranged in the pod. The water tank is provided with a water inlet connected with a filling aircraft outside the airship. The airship capsule is provided with a solar cell. The interior of the airship capsule is provided with a hydrogen storage bag. The solar cell is electrically connected with the renewable fuel cell. The renewable fuel cell can use electric energy provided by the solar cell to electrolyze water provided by the filling aircraft into hydrogen and supplement the hydrogen to the hydrogen storage bag. The airship can supplement hydrogen to the airship capsule by electrolyzing water to reduce the phenomenon of insufficient gas in the airship capsule.

Described herein are features for a high altitude lighter-than-air (LTA) system and associated methods. The LTA may include one or more super-pressure balloons (SPB). One or more of the SPB's may include one or more interior volumes. One or more of the interior volumes may be configured to receive an LTA gas therein to supplement the free lift of the LTA system. There may be an adjustable valve or vent to release the LTA gas. One or more of the interior volumes may be configured to receive ambient air to provide a variable downward force. The SPB may use a compressor to pump in ambient air. The compressor or another valve may release ambient air to decrease the downward force. A zero-pressure balloon (ZPB) may be attached with the one or more SPB's. The ZPB may supplement lift for the system.

Described herein are features for a high altitude lighter-than-air (LTA) system and associated methods. The LTA may include one or more super-pressure balloons (SPB). One or more of the SPB's may include one or more interior volumes. One or more of the interior volumes may be configured to receive an LTA gas therein to supplement the free lift of the LTA system. There may be an adjustable valve or vent to release the LTA gas. One or more of the interior volumes may be configured to receive ambient air to provide a variable downward force. The SPB may use a compressor to pump in ambient air. The compressor or another valve may release ambient air to decrease the downward force. A zero-pressure balloon (ZPB) may be attached with the one or more SPB's. The ZPB may supplement lift for the system.

Gas Replacement System (GRS) produces lighter than air lift gas from ammonia to enable balloon launch and/or to extend the flight durations of balloons. The GRS produces lighter than air lift gas by dissociating all or part of an ammonia supply into a mixture of nitrogen and hydrogen. The GRS can be used to launch balloons from the ground and/or produce gas for airborne balloons to extend their flight duration. In one embodiment, a GRS includes a tank containing ammonia (e.g., liquid ammonia), a reactor, and a controller operable to direct a release of the ammonia from the tank to the reactor. The controller is also operable to direct the reactor to dissociate at least a portion of the ammonia into a lift gas and exhaust the lift gas from the reactor into the balloon for inflation, the lift gas comprising nitrogen and hydrogen.

Gas Replacement System (GRS) produces lighter than air lift gas from ammonia to enable balloon launch and/or to extend the flight durations of balloons. The GRS produces lighter than air lift gas by dissociating all or part of an ammonia supply into a mixture of nitrogen and hydrogen. The GRS can be used to launch balloons from the ground and/or produce gas for airborne balloons to extend their flight duration. In one embodiment, a GRS includes a tank containing ammonia (e.g., liquid ammonia), a reactor, and a controller operable to direct a release of the ammonia from the tank to the reactor. The controller is also operable to direct the reactor to dissociate at least a portion of the ammonia into a lift gas and exhaust the lift gas from the reactor into the balloon for inflation, the lift gas comprising nitrogen and hydrogen.

A balloon system including a balloon, a payload, and a safety module. A safety module, preferably including a tether and a parachute, and optionally including a cover and/or a drogue. A method of balloon system operation, preferably including operating the balloon system in flight and descending under a parachute.

A balloon system including a balloon, a payload, and a safety module. A safety module, preferably including a tether and a parachute, and optionally including a cover and/or a drogue. A method of balloon system operation, preferably including operating the balloon system in flight and descending under a parachute.

A system for generating hydrogen includes a vessel having a first chamber that is separated from a second chamber by a barrier. A trigger assembly integrated with the barrier allows a liquid to be combined with a reactant and a catalyst in the second chamber to form a chemical reaction to generate hydrogen gas. A pressure relief valve located on the vessel opens to allow the hydrogen gas to exit when a predetermined pressure is reached.