Question

To calculate the work required for adiabatically compressing a fluid from 100 kPa to 1 MPa in an open system, considering saturated liquid and saturated vapor states, and to analyze and compare the results for these two conditions.

          To calculate the work required for adiabatically compressing a fluid from 100 kPa to 1 MPa in an open system, considering saturated liquid and saturated vapor states, and to analyze and compare the results for these two conditions.
        
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University Physics with Modern Physics
University Physics with Modern Physics
Hugh D. Young 14th Edition
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To calculate the work required for adiabatically compressing a fluid from 100 kPa to 1 MPa in an open system, considering saturated liquid and saturated vapor states, and to analyze and compare the results for these two conditions.
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Transcript

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00:01 So, let's start with the concept which we are going to use here for this question.
00:08 So, here we are going to use the enthalpy method to calculate the work input.
00:14 So, let's start with the case first.
00:18 So, the concept you can see that is we are going to use the enthalpy method for the calculations.
00:27 So, in the case first, we have asked for steam exist as saturated liquid.
00:37 As saturated liquid.
00:40 For this case, if you see from the question, the pressure first have been given that we say the initial pressure 100 kpa.
00:49 Now for steam table, we will get the final heat, we will say let's say h1.
00:57 So, that will be equals to from steam table that is 417 .51 kj per kg.
01:06 While if you look to the final volume that is let's say v1.
01:10 So it will be equals to 0 .001043 m3 per kg.
01:20 While the enthalpy is let's say f of f which will be equals to h1 which we will get from the table as 1 .3028 kj per kgk.
01:34 Now according to the state second, we are given the pressure v2 is 1 mpa which would be equals to 1000 kpa.
01:50 Right? while the enthalpy will be same as the initial one that is s1.
01:56 So, from steam table corresponding to these values of s2 and p2, we have the h2 would be equals to 418 .7 kj per kg.
02:13 And similarly, the volume second would be equals to 0 .00104 m3 per kg.
02:24 So, from here as we have to calculate the work input...
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