00:01
In this question it is given that steam at a pressure of 6 megapascal and the temperature is 800 degrees centigrade enters in a steam turbine.
00:12
Heat loss from the turbine is 49 .7 kilojoules per kilogram and the isotropic efficiency is equals to 90 % or we can write 0 .9.
00:29
The exit pressure and temperature are 15 kilo pascal and 20 degrees centigrade respectively.
00:40
We are required to calculate the actual work and the reversible work between the inlet and the exit.
00:47
So let's see how to solve this question.
00:50
First of all, let's write the properties of the steam corresponding to state 1 from the table.
00:57
So we can write s -i is equal to 7 .3.
01:02
6 .6 kilojoules per kilogram kelvin and h i is equals to 4 ,132 .74 kilojoules per kilogram.
01:19
So these are the properties for state i and now at state e we can write s s is equals to s i so this will be equals to 7 .6566 kilojoules per kilogram kelvin.
01:45
Now let's apply the formula of entropy to calculate dryness fraction.
01:51
So we can write ses is equals to sfes plus xes into sfges.
02:09
Now substitute all the values from the the table and the calculated values so we can write 7 .6566 and this will be equals to 0 .7548 these values have been taken from the table plus x e comma s multiplied by 7 .2536 so when we further calculate we get dryness fraction e.
02:42
Comma s is equals to 0 .9515 and now let's apply the formula to calculate specific enthalpy for this state and this will be equals to hfes plus xes into hfges now substitute all the values so we will have hes is equals to 225 .91 plus 0 .9515 multiplied by 2 ,373 .14.
03:31
When we further calculate we get 2 ,484 kilojoules per kilogram.
03:40
Now let's apply the formula to calculate.
03:43
Turbine work.
03:45
So wt will be equals to h .i minus h .e.
03:52
Comma s.
03:54
Now substitute all the values so we will have 4 ,132 .74 minus 2 ,484.
04:03
When we further calculate, finally we get 1 ,648 .74 kilojoules per kilogram...