ERICSSON CYCLE PV AND TS DIAGRAM

We were discussing the Otto cycle and the Diesel cycle in our previous posts and we have seen there that these cycles are not totally reversible cycles but also these cycles are internally reversible cycles. Hence, thermal efficiency of an Otto cycle or Diesel cycle will be less than that of a Carnot cycle working between similar temperature limits.

Let us consider that we have one heat engine which is operating between heat source having at temperature T_H and heat sink having at temperature T_L. As we have already seen in our previous discussion that for a heat engine to be a complete reversible, difference between the working fluid temperature and heat source temperature or difference between working fluid temperature and heat sink temperature must never go beyond the differential amount of dT during any heat transfer process.

We can also say that heat addition or heat rejection process must be carried out isothermally and this criterion is fulfilled in Carnot cycle.

Now we will see here one more important cycle i.e. Ericsson cycle, where heat addition process and heat rejection process will be carried out isothermally. But we must note it here that Ericsson cycle will be different from Carnot cycle. Because there will be two constant pressure regeneration processes in Ericsson cycle instead of isentropic processes of Carnot cycle.

So, Let us see here Ericsson cycle

First we will see here the PV and TS diagram for Ericsson cycle, we will understand here the various processes involved and finally we will determine the thermal efficiency of the Ericsson cycle.

As we can see here from PV and TS diagram, there will be two reversible isothermal processes and two reversible constant pressure processes. Heat energy addition and rejection will be done at constant temperature process and also at constant pressure process.

Advantage of the Ericsson cycle over the Stirling cycles and Carnot cycles is its smaller pressure ratio for a specific ratio of maximum to minimum specific volume with higher mean effective pressure.

Process, 1-2: Isothermal expansion from state 1 to state 2. Heat energy will be added here from external source. Volume will be increased but pressure will be reduced during this process.

ΔU_1-2 = 0,

Q_1-2 = W_1-2 = RT₁ Log (V₂/V₁)

Process, 2-3: Constant pressure process, internal heat transfer from the working fluid to regenerator and therefore this process is also termed as constant pressure regeneration process.

ΔU_2-3 = C_V (T₃-T₂)

W_2-3 = P₂ (V₃-V₂),

Q_2-3 = (h₃-h₂)

Process, 3-4: Isothermal compression from state 3 to state 4. Heat energy will be rejected here to the external sink. Volume will be reduced but pressure will be increased during this process.

ΔU = 0,

Q_3-4 = W_3-4 = RT₃ Log (V₄/V₃)

Process, 4-1: Constant pressure process, internal heat transfer from the regenerator back to the working fluid.

ΔU_4-1 = C_V (T₁-T₄)

W_4-1 = P₁ (V₁-V₄),

Q_4-1 = (h₁-h₄)

During the process of regeneration, Heat will be transferred to the regenerator from the working fluid during one part of the cycle and heat will be transferred back to the working fluid during the second part of the cycle. Regenerator will be considered as reversible heat transfer device.

If we think the concept of regeneration where, area under 2-3 i.e. Q_2-3and area under 4-1 i.e. Q_4-1 are equal, Regenerative Ericsson cycle will become Carnot cycle because heat energy will be added from an external source at constant temperature and heat will be rejected too to an external sink at constant temperature and hence Regenerative Ericsson cycle will become Carnot cycle and therefore it will have similar efficiency as of Carnot cycle.

Therefore, efficiency of the Ericsson cycle will be written as