Data for a regenerative vapor power cycle using an open and a closed feedwater heater, similar in design to that shown in the figure below, are provided in the table below. Steam enters the turbine at $14$MPa,$560C,$ state $1,$ and expands isentropically in three stages to a condenser pressure of $45$ kPa $,$ state $4.$

Saturated liquid exiting the condenser at state $5$ is pumped isentropically to state $6$ and enters the open feedwater heater. Between the first and second turbine stages, some steam is extracted at $1$ MPa $,$ state $2,$ and diverted to the closed feedwater heater. The diverted steam leaves the closed feedwater heater as saturated liquid at $1$ MPa $,$ state $10,$ undergoes a throttling process to $0\mathrm{.}2$ MPa $,$ state $11,$ and enters the open feedwater heater.

Steam is also extracted between the second and third turbine stages at $0\mathrm{.}2$ MPa $,$ state $3,$ and diverted to the open feedwater heater. Saturated liquid at $0\mathrm{.}2$ MPa exiting the open feedwater heater at state $7$ is pumped isentropically to state $8$ and enters the closed feedwater heater. Feedwater exits the closed feedwater heater at $14$MPa,$170C,$ state $9,$ and then enters the steam generator.

State $p(kPa),T(C),h(k\frac{J}{k}g),s(k\frac{J}{k}g*K),x$

$\backslash$table$[[1,14000,560,3486,6\mathrm{.}593,$dots

Data for a regenerative vapor power cycle using an open and a closed feedwater heater, similar in design to that shown in the figure below, are provided in the table below. Steam enters the turbine at $14$MPa,$560C,$ state $1,$ and expands isentropically in three stages to a condenser pressure of $45$ kPa $,$ state $4.$

Saturated liquid exiting the condenser at state $5$ is pumped isentropically to state $6$ and enters the open feedwater heater. Between the first and second turbine stages, some steam is extracted at $1$ MPa $,$ state $2,$ and diverted to the closed feedwater heater. The diverted steam leaves the closed feedwater heater as saturated liquid at $1$ MPa $,$ state $10,$ undergoes a throttling process to $0\mathrm{.}2$ MPa $,$ state $11,$ and enters the open feedwater heater.

Steam is also extracted between the second and third turbine stages at $0\mathrm{.}2$ MPa, state $3,$ and diverted to the open feedwater heater. Saturated liquid at $0\mathrm{.}2$ MPa exiting the open feedwater heater at state $7$ is pumped isentropically to state $8$ and enters the closed feedwater heater. Feedwater exits the closed feedwater heater at $14$MPa,$170C,$ state $9,$ and then enters the steam generator.

State $p(kPa),T(C),h(k\frac{J}{k}g),s(k\frac{J}{k}g*K),x$

$\backslash$table$[[1,14000,560,3486,6\mathrm{.}593,$dots