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M. Muttakin et al.
Hot water in
Hot water out
Chilled
water in
Chilled
water out
Cooling
water in
Cooling
water out
Bed 1
Bed 2
Condensate
return
Evaporator
Condenser
By-pass
opened
Fig. 8.8 Schematic of an adsorption chiller. Mode (b): Mass recovery. Water vapor flows from Bed
1 to Bed 2 due to the difference in pressure
Hot water in
Hot water out
Chilled
water in
Chilled
water out
Cooling
water in
Cooling
water out
Bed 1
Bed 2
Condensate
return
Evaporator
Condenser
Fig. 8.9 Schematic of an adsorption chiller. Mode (c): Heat recovery. Cooling water extracts heat
from Bed 1 and releases it to Bed 2 before flowing through the condenser
Thus one cycle is complete and in the next stage, the cycle is repeated, and the beds
perform an alternating role. Bed 1 starts adsorbing and is connected to the evaporator
and Bed 2 starts desorbing and gets connected to the condenser. The pressure of Bed
1 becomes essentially the same as that of evaporator and Bed 2 attains the same
pressure as of condenser. Hence in the mass recovery mode, the desorbed vapor of
Bed 2 is further passed to Bed 1 in order to achieve the mechanical equilibrium
between the two beds. The heat is extracted from the hot Bed 2 by the cooling water
and released to comparatively cooler Bed 1, during the heat recovery mode.
M. Muttakin et al.
Hot water in
Hot water out
Chilled
water in
Chilled
water out
Cooling
water in
Cooling
water out
Bed 1
Bed 2
Condensate
return
Evaporator
Condenser
By-pass
opened
Fig. 8.8 Schematic of an adsorption chiller. Mode (b): Mass recovery. Water vapor flows from Bed
1 to Bed 2 due to the difference in pressure
Hot water in
Hot water out
Chilled
water in
Chilled
water out
Cooling
water in
Cooling
water out
Bed 1
Bed 2
Condensate
return
Evaporator
Condenser
Fig. 8.9 Schematic of an adsorption chiller. Mode (c): Heat recovery. Cooling water extracts heat
from Bed 1 and releases it to Bed 2 before flowing through the condenser
Thus one cycle is complete and in the next stage, the cycle is repeated, and the beds
perform an alternating role. Bed 1 starts adsorbing and is connected to the evaporator
and Bed 2 starts desorbing and gets connected to the condenser. The pressure of Bed
1 becomes essentially the same as that of evaporator and Bed 2 attains the same
pressure as of condenser. Hence in the mass recovery mode, the desorbed vapor of
Bed 2 is further passed to Bed 1 in order to achieve the mechanical equilibrium
between the two beds. The heat is extracted from the hot Bed 2 by the cooling water
and released to comparatively cooler Bed 1, during the heat recovery mode.
