A method for increasing adjacent high-temperature heating-side get a multiterminal heating type I absorption heat pump which adds the high-temperature heating-side finally, which is based on the type I absorption heat pump using of an absorber and a condenser to heat the heated media of two or more stages;
- the method changes the type I absorption heat pump as below:
- (a) adding components and changing a plurality of pipelines of solution:
- (a1) adding components including a the new absorber, a the new absorption-evaporator, a the new throttle or a the liquid refrigerant pump, a the new solution pump, a the new solution heat exchanger and second solution heat exchanger;
- wherein an added pipe of concentrated solution from a concentrated solution generator passes through the second new solution heat exchanger and then connects the new absorber, wherein a pipe of dilute solution from the new absorber passes through the new solution heat exchanger and then connects the new absorption-evaporator, wherein the pipe of dilute solution from the new absorption-evaporator passes through the new solution pump, the new solution heat exchanger and the second new solution heat exchanger and then connects the concentrated solution generator;
- (a2) adding components including the new absorber, the new absorption-evaporator, the new throttle or the liquid refrigerant pump, the new solution pump, the new solution heat exchanger and second the new solution pump;
- wherein the added pipe of concentrated solution from the concentrated solution generator passes through the new solution heat exchanger and then connects the new absorption-evaporator, wherein the pipe of dilute solution from the new absorption-evaporator passes through the new solution pump and then connects the new absorber, wherein the pipe of dilute solution from the new absorber passes through the second new solution pump and the new solution heat exchanger and then connects the concentrated solution generator;
- (a3) adding components including the new absorber, the new absorption-evaporator, the new throttle or the liquid refrigerant pump, the new solution pump and the new solution heat exchanger;
- changing a pipe from a dilute solution provider passing through a solution pump, some of solution heat exchangers and then connecting the concentrated solution generator into connecting the new absorber, wherein the pipe of dilute solution from the new absorber passes through the new solution heat exchanger and then connects the new absorption-evaporator, wherein the pipe of dilute solution from the new absorption-evaporator passes through the new solution pump, the new solution heat exchanger and then connects the concentrated solution generator;
- (a4) adding components including the new absorber, the new absorption-evaporator, the new throttle or the liquid refrigerant pump, the new solution pump, the new solution heat exchanger and the second new solution heat exchanger;
- changing the pipe from the dilute solution provider passing through the solution pump, some solution heat exchangers and then connecting the concentrated solution generator into the pipe from the dilute solution provider passing through the solution pump, some solution heat exchangers and the second new solution heat exchanger and then connecting the new absorber, wherein the pipe of dilute solution from the new absorber passes through the new solution heat exchanger and then connects the new absorption-evaporator, wherein the pipe of dilute solution from the new absorption-evaporator passes through the new solution pump, the new solution heat exchanger and the second new solution heat exchanger and then connects the concentrated solution generator;
- (a5) adding components including the new absorber, the new absorption-evaporator, the new throttle or the liquid refrigerant pump, the new solution pump, the new solution heat exchanger and the second new solution pump;
- changing the pipe from the dilute solution provider passing through the solution pump, some solution heat exchangers and then connecting the concentrated solution generator into the pipe from the dilute solution provider passing through the solution pump, some solution heat exchangers and the new solution heat exchanger and then connecting the new absorption-evaporator, wherein the pipe of dilute solution from the new absorption-evaporator passes through the new solution pump and then connects the new absorber, wherein the pipe of dilute solution from the new absorber passes through the second new solution pump, the new solution heat exchanger and then connects the concentrated solution generator;
- (b) adding a pipe of cold agent steam from a refrigerant vapor provider to the new absorption-evaporator, the refrigerant vapor provider is a evaporator, a absorption-evaporator, a the low pressure generator or absorption-evaporator and a the low pressure generator;
- adding a pipe of cold agent liquid, from the condenser through the new throttle or from the evaporator through the new the liquid refrigerant pump to the new absorption-evaporator, then to the new absorber through pipes of refrigerant vapor;
- (c) adding pipes of heated media in the new absorber which connects with outside components;
- that makes the new absorber into an adjacent high-temperature heating-side of heat pump.