Fig. 1 Schematic presentation of a solar-assisted absorption chiller More

Fig. 2 The alteration of generator heat load with generator temperature ( T e v a p = 5 ∘ C ) More

Fig. 3 The alteration of circulation ratio with generator temperature ( T e v a p = 5 ∘ C ) More

Fig. 4 The alteration of COP with generator temperature ( T e v a p = 5 ∘ C ) More

Fig. 5 The alteration of total exergy destruction rate with generator temperature ( T e v a p = 5 ∘ C ) More

Fig. 6 The alteration of exergy efficiency with generator temperature ( T e v a p = 5 ∘ C ) More

Fig. 7 Energetic comparison of proposed solution mixture with LiBr/H 2 O ( T g e n = 96 ∘ C , T e v a p = 5 ∘ C , T a b s = T c o n d = 45 ∘ C ) More

Fig. 8 Exergetic comparison of proposed solution mixture with LiBr/H 2 O ( T g e n = 96 ∘ C , T e v a p = 5 ∘ C , T a b s = T c o n d = 45 ∘ C ) More

Fig. 9 The alteration of the maximum η ex,chill at the optimum generator temperatures ( T e v a p = 5 ∘ C ) More

Fig. 10 The alteration of COP, heat loads, and circulation ratio at the maximum η e x , c h i l l ( T e v a p = 5 ∘ C ) More

Fig. 11 The alteration of the auxiliary heater capacity, the extracted energy from the storage tank, and demanded solar collector area at the maximum η e x , c h i l l ( T e v a p = 5 ∘ C ) More

Fig. 12 The alteration of exergy destruction rate of each component at the maximum η e x , c h i l l ( T e v a p = 5 ∘ C ) More

Fig. 13 The alteration of exergy destruction rate of solar collector, storage tank, and auxillary heater at the maximum η ex , c h i l l ( T e v a p = 5 ∘ C ) More

Fig. 14 The alteration of COP and exergy efficiency of solar-driven system at the maximum η e x , c h i l l ( T e v a p = 5 ∘ C ) More