Ammonia and hydrogen electrochemical climate control systems

A climate control system comprising:

• a working fluid comprising ammonia (NH3) and hydrogen (H2);
• an evaporator that transforms liquid phase ammonia (NH3) in the working fluid to a vapor phase;
• an ejector configured to combine and create a pressurized stream of working fluid comprising vapor phase ammonia (NH3) received from the evaporator and a distinct stream of a gas phase hydrogen (H2);
• an electrochemical device that receives the pressurized stream of working fluid from the ejector to further increase pressure of the working fluid as the working fluid passes through the electrochemical device when an electrical potential is applied thereto;
• a condenser disposed downstream of the electrochemical device that cools the working fluid and transforms vapor phase ammonia (NH3) in the working fluid to a liquid phase;
• a separator disposed downstream of the condenser and upstream of the evaporator and the ejector, the separator being configured to separate liquid phase ammonia (NH3) from gas phase hydrogen (H2) so that separated liquid phase ammonia (NH3) is directed to the evaporator and transformed to vapor phase ammonia (NH3) that is fed to the ejector, while the separated gas phase hydrogen (H2) forms the distinct stream that is fed to the ejector;
• and
• a fluid conduit for circulating the working fluid and establishing fluid communication between the evaporator, the ejector, the electrochemical device, the condenser, and the separator.

A climate control system comprising:

• a working fluid comprising ammonia (NH3) and hydrogen (H2);
• an evaporator that transforms liquid ammonia (NH3) in the working fluid to a vapor phase;
• a first electrochemical device that receives the working fluid from the evaporator comprising vapor phase ammonia (NH3) and gas phase hydrogen (H2), wherein the first electrochemical device increases a pressure of the working fluid passing through the first electrochemical device when an electrical potential is applied thereto;
• a condenser disposed downstream of the first electrochemical device that cools the working fluid and transforms ammonia (NH3) in the working fluid from a gas phase to a liquid phase;
• a separator disposed downstream of the condenser, the separator being configured to separate liquid ammonia (NH3) from gas phase hydrogen (H2) so that separated liquid phase ammonia (NH3) is directed to the evaporator and transformed to vapor phase ammonia (NH3) that is fed to the first electrochemical device, while the separated gas phase hydrogen (H2) is directed to a second electrochemical device;
• the second electrochemical device configured to receive and decrease a pressure of gas phase hydrogen (H2) from the separator and generate electrical power that is transferred to the first electrochemical device;
• and
• a fluid conduit for circulating the working fluid and establishing fluid communication between the evaporator, the first electrochemical device, the condenser, the separator, and the second electrochemical device.