Low-temperature water heat sources flow inside heat tubes of low-temperature evaporators and liquid refrigerants flowing outside of those tubes are evaporated by accepting the waste heat of those low-temperature hot water heat sources. The evaporated refrigerant gas which goes to a low-temperature absorber to be absorbed into an absorption liquid flowing outside of the tubes heats liquid refrigerants of a high-temperature evaporator flowing inside the tubes of a low-temperature absorber.
Those liquid refrigerants go to a high-temperature evaporator to be evaporated. Refrigerant steam evaporated from the high-temperature evaporator goes to a high-temperature absorber to be absorbed into an absorption liquid flowing outside of the heat tubes installed to produce hot water and heat hot water warmed at a condenser to a final temperature. The absorption liquid flowing outside of those tubes is a thick absorption liquid coming from a generator.
A generator applies heat from outside (incineration heat, combustion heat and steam heat can be used as drive heat sources), concentrates the dilute absorption liquid (absorption liquid weakened after absorbing refrigerant steam at an absorber) coming from an absorber and generates refrigerant steam. The amount of refrigerant steam generated at this time is about twice as much as that evaporated at low- and high-temperature evaporators.
Refrigerant steam produced at the generator is condensed outside the heat tubes of a condenser and goes to a high-temperature evaporator, and then principally heats hot water flowing inside condenser tubes.
A part of the condensed refrigerant liquid coming down from a condenser to a high-temperature evaporator is heated at a low-temperature evaporator to be absorbed at a high-temperature absorber. The remaining liquid refrigerants go down to a low-temperature evaporator to be evaporated after absorbing the waste heat of low-temperature hot water heat sources. Low- and high-temperature solution heat exchangers are used for each absorption liquid line.