Abstract: A method of operating an absorption refrigeration system. The system has high- and low-pressure sections. The sections are connected by three lines and have an evaporator for subcooling the liquified refrigerant before it enters a connecting line. To enable uninterrupted transport of the weak refrigerant solution without increasing prime cost, the refrigerant vapor is fed from a subcooler into the expanded weak refrigerant solution at one or more points and a connecting line that conveys the weak refrigerant acts as an absorber. Expanded and evaporating refrigerant fluid flows through a subcooler in the high-pressure section. A condenser is in a line that conveys the weak refrigerant solution. The exit from the subcooler communicates through another line downstream of an expansion valve with a line that conveys the weak refrigerant solution and acts accordingly as an uncooled absorber.

Abstract: An absorption refrigeration system with a booster compressor in which at least one partial flow of a refrigerant vapor is extracted at an intermediate pressure appropriate for absorption.The method is performed by installing at least one additional absorption stage for the absorption of the extracted partial flow. Only the remaining refrigerant vapor has to be compressed to the total pressure difference.

Abstract: An absorption refrigerating machine for operation encountering differences of heat energy and refrigeration requirement over a period of time. A storage unit for storing of refrigerating medium-fluid is provided in the flow direction of the refrigeration medium after the condenser for liquefying of refrigerating-medium-vapor; a storage unit for storing of weak refrigeration medium-solution is provided in the flow direction of the solution in a bypass conduit after the solution heat exchanger and the automatic expansion or relief valve. The bypass conduit is connected with a continuous line or conduit by two distributor valves, and a storage unit for storage of rich refrigeration medium-solution is located in the flow direction of the solution after the absorber.

Abstract: A method of improving the energy consumption of absorption cooling plants, according to which the solution residue from the evaporator of an absorption cooling plant is employed for the rectification of the vapor of the cooling medium.