CIclo de Rankine

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College of Engineering and Computer Science
Mechanical Engineering Department
Mechanical Engineering 370
Thermodynamics
	
	Fall 2010 Course Number: 14319 Instructor: Larry Caretto
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Unit Eleven Homework Solutions, November 30, 2010
1.	Consider a 210 MW steam power plant that operates on a simple ideal Rankine cycle. Steam enters the turbine at 10 MPa and 500oC and is cooled in the condenser to a pressure of 10 kPa. Show the cycle on a T-s diagram with respect to the saturation lines and determine (a) the quality of steam at the turbine exit, (b) the thermal efficiency of the cycle, and (c) the mass flow rate of the steam.
The cycle diagram shows the individual steps in the cycle. The increase in temperature in the pump is typically about 1oC so the isentropic pump step does not really show on the diagram. The constant pressure heating in the steam generator shows the path of an isobar on a T-s diagram. In the mixed region, where temperature and pressure are constant, the isobar is a horizontal line. The condenser, which is completely in the mixed region, has a constant temperature line to represent the constant pressure process in the condenser.
To compute the quality at the turbine exit, we recognize that this exit state is defined by the condenser pressure of 10 kPa and an isentropic process such that sout = sin = s(10 MPa, 500oC) = 6.5995 kJ/kg∙K. The outlet quality is thus found from the following equation.
	xout = 0.793.
In order to compute the efficiency, we need the enthalpy values at all the state points. Following a conventional Rankine cycle calculation, we find the properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(10 kPa) = 191.81 kJ/kg and v1 = 0.001010 m3/kg. The isentropic pump work, |wp| = v1(P2 – P1) where P2 is the same as the inlet pressure to the turbine, 10 MPa = 10,000 kPa. Thus,
We then find h2 = h1 + |wP1| = 191.81 kJ/kg + 10.09 kJ/kg = 201.90 kJ/kg.
h3 = h(10 MPa, 500oC) = 3375.1 kJ/kg.		s3 = s(10 MPa, 500oC) = 6.5995 kJ/kg∙K.
As noted above, state 4 is in the mixed region with P4 = 10 kPa and x4 = 0.793. We thus find the enthalpy from the quality as h4 = hf(P4 = 10 kPa) + x4 hfg(P4 = 10 kPa) = 191.81 + (0.793)(2392.1 kJ/kg) or h4 = 2089.7 kJ/kg.
The heat input to the steam generator, qh = h3 – h2 = 3375.1 kJ/kg – 201.90 kJ/kg = 3173.2 kJ/kg
The condenser heat rejection, ql = |h1 – h4| = |191.81 kJ/kg – 2089.7 kJ/kg| = 1897.9 kJ/kg.
The net work, w = qh - |qL| = 3173.2 kJ/kg| - 1897.9 kJ/kg = 1275.3 kJ/kg.
The efficiency = w / qH = (1275.3 kJ/k ) / (3173.2 kJ/kg) or  = 40.2%.
The mass flow,
 		
2.	Consider a solar-pond power plant that operates on a simple ideal Rankine cycle with refrigerant-134a as the working fluid. The refrigerant enters the turbine as a saturated vapor at 1.6 MPa and leaves at 0.7 MPa. The mass flow rate of the refrigerant is 6 kg/s. Show the cycle on a T-s diagram with respect to the saturation lines and determine (a) the thermal efficiency and (b) the power output of the plant.
The cycle diagram is shown on the next page. As usual, when the T-s diagram is drawn to scale, the pump does not appear on the diagram and the constant-pressure heating of the liquid in the steam generator is very close to the saturation line. This diagram is unusual because there is no superheating. In addition, the particular inlet and outlet pressures chosen for the turbine are in an area of the T-s diagram where the slope is nearly vertical. Thus, the isentropic turbine process, starting at the saturated vapor line lies very close to the saturated vapor line for the entire process. This is verified by the calculation of the exit quality from the turbine, x4. To compute this quality we note that the ideal cycle has an isentropic turbine so that s4 = s3 = sg(1.6 MPa) = 0.90784 kJ/kg∙K. At the condenser pressure of 0.7 MPa and an entropy of 0.90784 kJ/kg∙K, we find the quality as follows.
	xout = 0.979.
The value of 98.3% for quality confirms the turbine path in the diagram that is close to the saturated line for the entire process.
Next, we do the usual set of calculations for the Rankine cycle. In order to compute the efficiency, we need the enthalpy values at all the state points. Following a conventional Rankine cycle calculation, we find the properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(0.7 MPa) = 88.82 kJ/kg and v1 = 0.0008331 m3/kg. The isentropic pump work, |wp| = v1(P2 – P1) where P2 is the same as the inlet pressure to the turbine, 1.6 MPa = 1600 kPa. Thus,
We then find h2 = h1 + |wP1| = 86.78 kJ/kg + 0.75 kJ/kg = 89.57 kJ/kg.
h3 = hg(1.6 MPa) = 277.863 kJ/kg.		s3 = sg(1.6 MPa) = 0.90784 kJ/kg∙K.
As noted above, state 4 is in the mixed region with P4 = 700 kPa and x4 = 0.979. We thus find the enthalpy from the quality as h4 = hf(P4 = 700 kPa) + x4 hfg(P4 = 700 kPa) = 88.82 kJ/kg + (0.979)(176.212 kJ/kg) or h4 = 261.41 kJ/kg.
The heat intput to the steam generator, qh = h3 – h2 = 277.86 kJ/kg – 89.54 kJ/kg = 188.3 kJ/kg
The condenser heat rejection, ql = |h1 – h4| = |88.62 kJ/kg – 261.41 kJ/kg| = 172.6 kJ/kg.
The net work, w = qh - |qL| =188.3 kJ/kg| - 172.6 kJ/kg = 15.70 kJ/kg.
The efficiency = w / qH = (15.70 kJ/k ) / (188.3 kJ/kg) or  = 8.3%.
The power output = 
 		
3.	Consider a steam power plant that operates on a simple ideal Rankine cycle and has a net power output of 45 MW. Steam enters the turbine at 7 MPa and 500oC and is cooled in the condenser to a pressure of 10 kPa by running cooling water from a lake through the condenser at a rate of 2000 kg/s. Show the cycle on a T-s diagram with respect to the saturation lines, and determine (a) the thermal efficiency of the cycle, (b) the mass flow rate of the steam, and (c) the temperature rise of the cooling water.
The diagram for this cycle is similar to the diagram for the cycle in problem 9-16 and is not shown here.
In order to compute the efficiency, we need the enthalpy values at all the state points. Following a conventional Rankine cycle calculation, we find the properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(10 kPa) = 191.83 kJ/kg and v1 = 0.001010 m3/kg. The isentropic pump work, |wp| = v1(P2 – P1) where P2 is the same as the inlet pressure to the turbine, 7 MPa = 7,000 kPa. Thus,
We then find h2 = h1 + |wP1| = 191.81 kJ/kg + 7.06 kJ/kg = 198.87 kJ/kg.
h3 = h(7 MPa, 500oC) =3411.4 kJ/kg.		s3 = s(7 MPa, 500oC) = 6.8000 kJ/kg∙K.
h4 = h(P = Pcond = 10 kPa, s4 = s3). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
	xout = 0.8202.
With P4 = 10 kPa and x4 = 0.82027, we find the value of h4 = hf(P4 = 10 kPa) + x4 hfg(P4 = 10 kPa) = 191.81 + (0.8202)(2392.` kJ/kg) or h4 = 2153.7 kJ/kg.
The heat input to the steam generator, qh = h3 – h2 = 3411.4 kJ/kg – 198.87 kJ/kg = 3212.5 kJ/kg
The condenser heat rejection, ql = |h1 – h4| = |191.81 kJ/kg – 2153.7 kJ/kg| = 1961.8 kJ/kg.
The net work, w = qh - |qL| = 3212.5 kJ/kg| - 1961.8 kJ/kg = 1250.6 kJ/kg.
The efficiency = w / qH = (1250.6 kJ/kg) / (3212.5 kJ/kg) or  = 38.9%.
The mass flow,
 		
The heat rejection rate from the steam to the cooling water is the product of the mass flow rate and the value of |qL|: 
 
This heat is added to the cooling water. The cooling water flow is modeled as a steady flow with negligible kinetic and potential energies. There is no useful work. We model the enthalpy change of the cooling water by the equation h = cpT since we assume that the effect of pressure changes on the enthalpy of the relatively incompressible liquid water will be negligible. Applying the first law to the cooling water then gives the following relationship between the condenser heat rejection and the cooling water temperature rise, Tcw:
We can solve this equation for Tcw, andsubstitute in the given values including the heat capacity of liquid water to give cp,cw = 4.18 kJ/kg∙K (Table A-3(a) on page 914 of the text for liquid water at 25oC) to obtain the final answer for the temperature rise.
		Tcw = 8.44oC.
4.	A steam power plant operates on an ideal regenerative Rankine cycle. Steam enters the turbine at 6 MPa and 450oC and is condensed in the condenser at 20 kPa. Steam is extracted from the turbine at 0.4 MPa to heat the feedwater in an open feedwater heater. Water leaves the feedwater heater as a saturated liquid. Show the cycle on a T-s diagram and determine (a) the net work per kilogram of steam flowing through the boiler and (b) the thermal efficiency of the cycle.
	
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	The diagram of the components in the cycle is shown on the left. In terms of the numbered points on this diagram, the input data for the problem give P5 = 6 MPa, T5 = 450oC, Pcond = 20 kPa, and PFWH = 0.4 MPa.
For the ideal cycle in which there are no line losses in pressure or temperature and no pressure drops in heat transfer devices, we have P4 = P5,= 6 MPa, P2 = P3 = P6 = P7 = PFWH = 0.4 MPa, and P1 = P8 = Pcond = 20 kPa. The ideal cycle has isentropic work devices so s8 = s7 = s6 = s5; s2 = s1 and s4 = s3. Finally points 1 and 3 are saturated liquid.
As usual, we assume that the individual components are steady-flow devices with negligible kinetic and potential energies. There is no useful work in the steam generator, feedwater heater, or condenser. The turbine and pumps are reversible and adiabatic meaning that there is no heat transfer or entropy change. Thus the first law for each device only one inlet and one outlet is q = w + hout – hin. We begin by determining the enthalpy at each point in the cycle.
The properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(20 kPa) = 251.42 kJ/kg and v1 = 0.001017 m3/kg. The pumps are isentropic and we calculate the work of the first pump as follows: |wp1| = v1(P2 – P1). Thus,
We then find h2 = h1 + |wP1| = 251.42 kJ/kg + 0.39 kJ/kg = 251.80 kJ/kg.
The properties at state three are also those of a saturated liquid. Here the pressure is the feedwater heater pressure so that h3 = hf(400 kPa) = 604.66 kJ/kg and v3 = 0.001084 m3/kg. We use the vP calculation for isentropic pump work for the second pump.
We then find h4 = h3 + |wP2| = 604.66 kJ/kg + 6.07 kJ/kg = 610.73 kJ/kg.
h5 = h(6 MPa, 450oC) = 3302.9 kJ/kg.		s5 = s(6 MPa, 450oC) =6.7219 kJ/kg∙K.
h6 = h(P = PFWH = 400 kPa, s6 = s5). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
h6 = hf(P6 = 400 kPa) + x6 hfg(P6 = 400 kPa) = 604.66 kJ/kg + (0.9661)(2133.4 kJ/kg) or h6 = 2665.7 kJ/kg.
State 7 is the same as state 6 so we have h7 = 2665.7 kJ/kg.
h8 = h(P = Pcond = 20 kPa, s8 = s5). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
h8 = hf(P8 = 20 kPa) + x8 hfg(P8 = 20 kPa) = 251.42 kJ/kg + (0.8325)(2357.5 kJ/kg) or h8 = 2213.97 kJ/kg.
In this cycle there are three distinct mass flow rates at different points in the cycle. These are shown in the equations below. (Here, 
represents the mass flow into the feedwater heater.)
		
	
Taking a mass and energy balance around the feedwater heater gives the following relation for the mass flow ratio. We can substitute the enthalpy values found above to compute this ratio.
We can compute the heat input rate for the steam generator, using 
 as the mass flow rate in the steam generator.
The power output from the two turbine stages is given by the following equation, which accounts for the differences in mass flow rate in the two stages.
Finally, the total power input to the pumps is computed by accounting for the differences in mass flow rates.
We now have the necessary information to compute the cycle efficiency.
We can divide by the mass flow rate, 
to get the following equation for the efficiency in terms of the mass flow rate ratio that we found from our analysis of the feedwater heater.
In this form, the numerator of the efficiency equation is the net work per unit mass flowing through the steam generator.
Substituting the values found for the enthalpies in the cycle and the mass flow rate ratio gives the net work per unit mass flowing through the steam generator as follows:
		
From the equations for the efficiency and the net work, we see that we can use the computed value of work to simplify the efficiency calculation.
 = 37.8%
5.	Repeat problem 4 with the open feedwater heater replaced by a closed feedwater heater. Assume that the feedwater leaves the heater at the condensation temperature of the extracted steam and that the extracted steam leaves the heater as a saturated liquid and is pumped to the line carrying the feedwater.
	
	The diagram of the components in the cycle is shown on the left. In the closed feedwater heater, the feed water flows from point w to point 4, without mixing with the extracted steam. (The steam enters at point 8, transfers heat to the feed water without mixing, and leaves at point 3.
In terms of the numbered points on this diagram, the input data for the problem give P7 = 6 MPa, T7 = 450oC, Pcond = 20 kPa, and P8 = 0.4 MPa. We are also told that point 3 is a saturated liquid and T4 has the same temperature as this saturated liquid
For the ideal cycle in which there are no line losses in pressure or temperature and no pressure drops in heat transfer devices, we have P2 = P4 = P5 = P6 = P7 = 6 MPa, P3 = P8 = 0.4 MPa, and P1 = P10 = Pcond = 20 kPa. The ideal cycle has isentropic work devices so s10 = s9 = s8 = s7; s2 = s1 and s5 = s3. Finally points 1 and 3 are saturated liquid.
In this cycle there are three distinct mass flow rates at different points in the cycle. These are shown in the equations below. (Here, 
represents the mass flow into the feedwater heater.)
		
	
Taking a mass balance around the mixing chamber gives the following relation among the three mass flow rates.
As usual, we assume that the individual components are steady-flow devices with negligible kinetic and potential energies. There is no useful work in the steam generator, feedwater heater, or condenser. The turbine and pumps are reversible and adiabatic meaning that there is no heat transfer or entropy change. Thus the first law for each device with only one inlet and one outlet is q = w + hout – hin. We begin by determining the enthalpy at each point in the cycle.
The properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(20 kPa) = 251.42 kJ/kg and v1 = 0.001017 m3/kg. The pumps are isentropic and we calculate the work of the first pump as follows: |wp1| = v1(P2 – P1). Thus,
We then find h2 = h1 + |wP1| = 251.42 kJ/kg + 6.08 kJ/kg = 257.50 kJ/kg.
The properties at state three are also those of a saturated liquid. Here the pressure is the feedwater heater pressure so that h3 = hf(400 kPa) = 604.66 kJ/kg and v3 = 0.001084 m3/kg. We use the vP calculation for isentropic pump work for the second pump.
We then find h5 = h3 + |wP2| = 604.66 kJ/kg + 6.07 kJ/kg = 610.73 kJ/kg.
According to the problem information T4 has the same temperature as the saturated liquid at point three. From the saturation tables we find this temperature as 143.61oC. This is a compressed liquid and we can use the following data in the compressed liquid. We can use a double interpolation in the compressed liquid tables to find the enthalpy at this point. First we use two interpolations to find the enthalpy at the desired temperature of 143/61oC at the two pressures bounding the given pressure of 6 MPa in the tables.
We can now use these two values to find the desired enthalpy at 6 MPa.
The mixing chamber has no heat or work, but is has three different mass flowrates. Thus the first law and mass conservation equations for this device can be written as shown below and manipulated to get an equation for h6 in terms of mass flow rate ratios.
Thus, we can compute h6 if we know the mass flow rate ratio in the above equation. We can find this mass flow rate ratio from an analysis of the closed feedwater heater. Application of the first law for no heat and work (and recognizing that the two streams in this device do not mix) gives the following result.
We have already seen how to compute h1, h3, and h4, and we will determine h8 below. Thus we will be able to compute the mass flow rate ratio 
shown above from enthalpy values. To compute the ratio 
required to compute h6, we have to make the following computations.
We continue to find enthalpy values, using the conventional methods for the isentropic turbine work.
h7 = h(6 MPa, 450oC) = 3302.9 kJ/kg.		s7 = s(6 MPa, 450oC) =6.7219 kJ/kg∙K.
h8 = h(P = P8 = 400 kPa, s8 = s7). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
h8 = hf(P8 = 400 kPa) + x8 hfg(P8 = 400 kPa) = 604.66 kJ/kg + (0.9661)(2133.4 kJ/kg) or h8 = 2665.67 kJ/kg.
State 9 is the same as state 9 so we have h9 = 2665.67 kJ/kg.
h10 = h(P = Pcond = 20 kPa, s10 = s7). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
h10 = hf(P10 = 20 kPa) + x10 hfg(P10 = 20 kPa) = 251.42 kJ/kg + (0.8325)(2357.5 kJ/kg) or h10 = 2213.97 kJ/kg.
We now have all the enthalpy values required to compute the mass flow rate ratios
With the value just found for
, we can compute h6:
We can compute the heat input rate for the steam generator, using 
 as the mass flow rate in the steam generator.
The power output from the two turbine stages is given by the following equation, which accounts for the differences in mass flow rate in the two stages.
Finally, the total power input to the pumps is computed by accounting for the differences in mass flow rates.
We now have the necessary information to compute the cycle efficiency.
We can divide by the mass flow rate, 
to get the following equation for the efficiency in terms of the mass flow rate ratio that we found from our analysis of the feedwater heater.
In this form, the numerator of the efficiency equation is the net work per unit mass flowing through the steam generator.
Substituting the values found for the enthalpies in the cycle and the mass flow rate ratio gives the net work per unit mass flowing through the steam generator as follows:
		
From the equations for the efficiency and the net work, we see that we can use the computed value of work to simplify the efficiency calculation.
 = 37.7%
6	A steam power plant operates on an ideal reheat-regenerative Rankine cycle and has a net power output of 80 MW. Steam enters the high-pressure turbine at 10 MPa and 550oC and leaves at 0.8 MPa. Some of the steam is extracted at this pressure to heat the feedwater in an open feedwater heater. The rest of the steam is reheated to 500oC and is expanded in the low pressure turbine to the condenser pressure of 10 kPa. Show the cycle on a T-s diagram and determine (a) the mass flow rate of steam flowing through the boiler and (b) the thermal efficiency of the cycle.
	
 EMBED Word.Picture.8 ��
	The diagram of the components in the cycle is shown on the left. In terms of the numbered points on this diagram, the input data for the problem give P5 = 10 MPa, T5 = 550oC, Pcond = 10 kPa, and PFWH = 0.8 MPa, and T7 = 500oC.
For the ideal cycle in which there are no line losses in pressure or temperature and no pressure drops in heat transfer devices, we have P4 = P5,= 10 MPa, P2 = P3 = P6 = P7 = PFWH = 0.8 MPa, and P1 = P8 = Pcond = 20 kPa. The ideal cycle has isentropic work devices so s8 = s7, s6 = s5; s2 = s1 and s4 = s3. Finally points 1 and 3 are saturated liquid.
As usual, we assume that the individual components are steady-flow devices with negligible kinetic and potential energies. There is no useful work in the steam generator, feedwater heater, or condenser. The turbine and pumps are reversible and adiabatic meaning that there is no heat transfer or entropy change. Thus the first law for each device only one inlet and one outlet is q = w + hout – hin. We begin by determining the enthalpy at each point in the cycle.
The properties at state one as those of a saturated liquid at the condenser pressure: h1 = hf(10 kPa) = 191.81 kJ/kg and v1 = 0.001010 m3/kg. The pumps are isentropic and we calculate the work of the first pump as follows: |wp1| = v1(P2 – P1). Thus,
We then find h2 = h1 + |wP1| = 191.81 kJ/kg + 0.80 kJ/kg = 192.61 kJ/kg.
The properties at state three are also those of a saturated liquid. Here the pressure is the feedwater heater pressure so that h3 = hf(800 kPa) = 720.87 kJ/kg and v3 = 0.001115 m3/kg. We use the vP calculation for isentropic pump work for the second pump.
We then find h4 = h3 + |wP2| = 720.87 kJ/kg + 10.26 kJ/kg = 731.13 kJ/kg.
h5 = h(10 MPa, 550oC) = 3502.0 kJ/kg.		s5 = s(1 MPa, 550oC) =6.7585 kJ/kg∙K.
h6 = h(P = PFWH = 800 kPa, s6 = s5). This state is in the gas region so we have to find h6 by interpolation between the first two rows at 800 kPa. This gives h6 = 2812,8 kJ/kg.
h7 = h(0.8 MPa, 500oC) = 3481.3 kJ/kg.		s7 = s(0.8 MPa, 500oC) =7.8692 kJ/kg∙K.
h8 = h(P = Pcond = 10 kPa, s8 = s7). We see that this state is in the mixed region so we have to compute the quality to determine the enthalpy.
h8 = hf(P8 = 10 kPa) + x8 hfg(P8 = 10 kPa) = 191.81 kJ/kg + (0.9627)(2392.1 kJ/kg) or h8 = 2494.7 kJ/kg.
In this cycle there are three distinct mass flow rates at different points in the cycle. These are shown in the equations below. (Here, 
represents the mass flow into the feedwater heater.)
		
	
Taking a mass and energy balance around the feedwater heater gives the following relation for the mass flow ratio. We can substitute the enthalpy values found above to compute this ratio.
We can compute the heat input rate for the steam generator, using 
 as the mass flow rate for the initial the steam generator flow and mb for the reheat flow.
The power output from the two turbine stages is given by the following equation, which accounts for the differences in mass flow rate in the two stages.
Finally, the total power input to the pumps is computed by accounting for the differences in mass flow rates.
We now have the necessary information to compute the cycle efficiency.
We can divide by the mass flow rate, 
to get the following equation for the efficiency in terms of the mass flow rate ratio that we found from our analysis of the feedwater heater.
In this form, the numerator of the efficiency equation is the net work per unit mass flowing through the steam generator.
Substituting the values found for the enthalpies in the cycle and the mass flow rate ratio gives the net work per unit mass flowing through the steam generator as follows:
From this specific work, we can find the mass flow rate required for a power output of 80 MW.
		
From the equations for the efficiency and the net work, we see that we can use the computed value of work to simplify the efficiency calculation.
	 = 44.4%
An alternative approach for finding the efficiency is to determine the heat loss in the condenser. 
. Since this is the rejected heat, we can use the following approach for computing the efficiency.
Applying the results previously found to this equation gives...
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Mixing Chamber
1
7
8
10
High Pressure 
Turbine (T1)
Low Pressure 
Turbine (T2)
Condenser
Pump 
 (P1)
Steam 
Generator
Feedwater 
 Heater
Pump 
(P2)
2
3
5
9
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Chart3
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		537.1405090332						584.211920166
		584.211920166						584.211920166
		615.3873352051						584.211920166
		638.9596618652						584.211920166
		647.2824157715						584.211920166
		632.8575500488						584.211920166
		617.0636657715						584.211920166
		577.9946350098						584.211920166
		523.2960876465						584.211920166
		485.3729003906						584.211920166
		451.7770141602						584.211920166
		413.8124450684						597.4862731934
		389.3320068359						632.2977355957
		367.8860534668						681.8373474121
		343.3577636719						745.4446472168
		327.1732543945						773.15
		323.15
		312.670324707
		295.6454833984
		284.127355957
		273.598638916
1
2
3
4
1 - 2 Pump
2 - 3 Steam generator
3 - 4 Turbine
4 - 1 Condenser
Saturation
Condenser
Pump
Steam
Generator
Turbine
Entropy (kJ/kg-K)
Temperature (K)
Rankine Cycle Diagram
Names
		Names for Units						Error code look-up table
		SI_C		1				0		No error
		SI_K		2				1		Invalid input variable specification
		Engl_F		3				2		Invalid input variable specification
		Engl_R		4				3		Unknown error
		Names for Inputs						4		Input (1 or both) > maximum
		P		1				5		Input (1 or both) < minimum
		v		2				6		No convergence
		T		3				7		Input T & P are saturation values
		u		4				8		No convergence (liquid)
		s		5				9		Cannot do compressed liquid
		h		6				10		No convergence
		x		7
		Names for Substances
		Ammonia		2
		Refrigerant12		26
		Water		37
P-v chart
		1000		100000000		100000000		100000000		100000000		100000000		100000000		28420080
		2000		75000000		75000000		75000000		10000000		10000000		10000000		12349.3310546875
		2100		56927520		42984896		50000000		8580862		1553795.625		101347.734375		12349.3310546875
		5000		28813848		27076868		24181000		8580862		1553795.625		101347.734375		12349.3310546875
		10000		10000000		15515990		22079540		8580862		1553795.625		101347.734375		12349.3310546875
		20000		11651130		10000000		22079540		8580862		1553795.625		101347.734375		12349.3310546875
		50000		5849789.5		6753890.5		21759468		8580862		1553795.625		101347.734375		12349.3310546875
		100000		2931267.75		3472211		17892072		8580862		1553795.625		101347.734375		12349.3310546875
		200000		1174078.25		1760085.125		11665344		4603129		1553795.625		101347.734375		12349.3310546875
		500000		587304.375		709794.5625		10000000		2474430.75		1553795.625		101347.734375		12349.3310546875
		1000000		293718.875		355857.0625		5436423		1280137.125		1027871.0625		101347.734375		12349.3310546875
		2000000		117503.5859375		178168.40625		2852382		522268.8125		426722.125		101347.734375		12349.3310546875
		5000000		58754.46875		71324.9296875		1459898.75		262827.15625		215882.171875		101347.734375		12349.3310546875
		10000000		29377.904296875		35672.0546875		592044.0625		131835.765625		108563.9375		84993.75		12349.3310546875
		15000000		11751.322265625		17838.42578125		297367.8125		52835.4921875		43574.08984375		34265.6328125		12349.3310546875
		20000000		5875.6611328125		7135.9458007812		149020.125		26434.599609375		21811.716796875		17177.126953125		7440.3129882812
		22088050		2937.8305664062		3568.0688476562		59688.7109375		13221.51171875		18131.580078125		14282.4296875		2980.0952148438
		18584896				1784.0584716797		29857.796875		5289.6157226562		10912.0185546875		8599.60546875		1490.7087402344
		15316675						14932.2587890625		2644.9763183594		4366.2846679688		3442.4875488281		745.5195922852
		9181853						5973.7094726562		1322.5302734375		2183.3884277344		1721.6843261719
		3982750						2986.9892578125				1091.7557373047		860.9522705078
		1992371.25						1493.5281982422
		970882.9375
		368110.4375
		175678.734375
		83734.2578125
		31469.1171875
		15035.4345703125
		12349.3310546875
		7196.8666992188
		2725.5100097656
		1310.3555908203
		631.09375
		101347.734375
Saturation
T = 1000 C iostherm
T = 500 C isotherm
Critical Isotherm
T = 300 C isotherm
T = 200 C isotherm
T = 100 C isotherm
T = 50 C isotherm
Specific volume (m3/kg)
Pressure (Pascals)
P-v diagram for Water
Critical P-v
		1000		100000000		100000000		100000000		100000000		100000000
		2000		75000000		75000000		75000000		10000000		10000000
		2100		56927520		42984896		50000000		8580862		1553795.625
		5000		28813848		27076868		24181000		8580862		1553795.625
		10000		10000000		15515990		22079540		8580862		1553795.625
		20000		11651130		10000000		22079540		8580862		1553795.625
		50000		5849789.5		6753890.5		21759468		8580862		1553795.625
		100000		2931267.75		3472211		17892072		8580862		1553795.625
		200000		1174078.25		1760085.125		11665344		4603129		1553795.625
		500000		587304.375		709794.5625		10000000		2474430.75		1553795.625
		1000000		293718.875		355857.0625		5436423		1280137.125		1027871.0625
		2000000		117503.5859375		178168.40625		2852382		522268.8125		426722.125
		5000000		58754.46875		71324.9296875		1459898.75		262827.15625		215882.171875
		10000000		29377.904296875		35672.0546875		592044.0625		131835.765625		108563.9375
		15000000		11751.322265625		17838.42578125		297367.8125		52835.4921875		43574.08984375
		20000000		5875.6611328125		7135.9458007812		149020.12526434.599609375		21811.716796875
		22088050		2937.8305664062		3568.0688476562		59688.7109375		13221.51171875		18131.580078125
		18584896				1784.0584716797		29857.796875		5289.6157226562		10912.0185546875
		15316675						14932.2587890625		2644.9763183594		4366.2846679688
		9181853						5973.7094726562		1322.5302734375		2183.3884277344
		3982750						2986.9892578125				1091.7557373047
		1992371.25						1493.5281982422
		970882.9375
		368110.4375
		175678.734375
		83734.2578125
		31469.1171875
		15035.4345703125
		12349.3310546875
		7196.8666992188
		2725.5100097656
		1310.3555908203
		631.09375
		101347.734375
Saturation
T = 1000 C isotherm
T = 500 C isotherm
Critical Isotherm
T = 300 C isotherm
T = 200 C isotherm
Specific volume (m3/kg)
Pressure (Pascals)
P-v diagram for Water around Critical Region
Superheat P-v
		1000		100000000		100000000		100000000		100000000		100000000		100000000		28420080
		2000		75000000		75000000		75000000		10000000		10000000		10000000		12349.3310546875
		2100		56927520		42984896		50000000		8580862		1553795.625		101347.734375		12349.3310546875
		5000		28813848		27076868		24181000		8580862		1553795.625		101347.734375		12349.3310546875
		10000		10000000		15515990		22079540		8580862		1553795.625		101347.734375		12349.3310546875
		20000		11651130		10000000		22079540		8580862		1553795.625		101347.734375		12349.3310546875
		50000		5849789.5		6753890.5		21759468		8580862		1553795.625		101347.734375		12349.3310546875
		100000		2931267.75		3472211		17892072		8580862		1553795.625		101347.734375		12349.3310546875
		200000		1174078.25		1760085.125		11665344		4603129		1553795.625		101347.734375		12349.3310546875
		500000		587304.375		709794.5625		10000000		2474430.75		1553795.625		101347.734375		12349.3310546875
		1000000		293718.875		355857.0625		5436423		1280137.125		1027871.0625		101347.734375		12349.3310546875
		2000000		117503.5859375		178168.40625		2852382		522268.8125		426722.125		101347.734375		12349.3310546875
		5000000		58754.46875		71324.9296875		1459898.75		262827.15625		215882.171875		101347.734375		12349.3310546875
		10000000		29377.904296875		35672.0546875		592044.0625		131835.765625		108563.9375		84993.75		12349.3310546875
		15000000		11751.322265625		17838.42578125		297367.8125		52835.4921875		43574.08984375		34265.6328125		12349.3310546875
		20000000		5875.6611328125		7135.9458007812		149020.125		26434.599609375		21811.716796875		17177.126953125		7440.3129882812
		22088050		2937.8305664062		3568.0688476562		59688.7109375		13221.51171875		18131.580078125		14282.4296875		2980.0952148438
		18584896				1784.0584716797		29857.796875		5289.6157226562		10912.0185546875		8599.60546875		1490.7087402344
		15316675						14932.2587890625		2644.9763183594		4366.2846679688		3442.4875488281		745.5195922852
		9181853						5973.7094726562		1322.5302734375		2183.3884277344		1721.6843261719
		3982750						2986.9892578125				1091.7557373047		860.9522705078
		1992371.25						1493.5281982422
		970882.9375
		368110.4375
		175678.734375
		83734.2578125
		31469.1171875
		15035.4345703125
		12349.3310546875
		7196.8666992188
		2725.5100097656
		1310.3555908203
		631.09375
		101347.734375
Saturation
T = 1000 C iostherm
T = 500 C isotherm
Critical Isotherm
T = 300 C isotherm
T = 200 C isotherm
T = 100 C isotherm
T = 50 C isotherm
Specific volume (m3/kg)
Pressure (Pascals)
P-v diagram for Water in Superheat Region
h-s
		4284.5302734375		2312.3317871094		1664.5982666016		28.576499939		903.237121582		293.3174743652
		4377.76171875		2424.6103515625		1678.0816650391		72.4002532959		855.6442871094		251.4717712402
		4436.9624023438		2847.28515625		1710.7135009766		75.6462478638		852.4208984375		233.1692352295
		4482.609375		3128.8054199219		1851.4371337891		137.15675354		865.3916625977		209.471496582
		4557.4750976562		3301.0502929688		2045.6938476562		191.7832489014		911.5153198242		209.6671600342
		4610.5756835938		3373.1716308594		2126.9338378906		251.8970031738		988.3880004883		210.2611541748
		4605.7944335938		3412.7602539062		2360.9418945312		341.2192382812		1142.1334228516		211.2511444092
		4622.7202148438		3450.7180175781		2725.8115234375		417.9165039062		1603.3696289062		213.2311401367
		4631.3676757812		3469.7192382812		2965.1706542969		504.651763916		2372.0964355469		219.1711273193
		4636.6201171875		3481.1083984375		3012.0307617188		639.7344970703		2792.7209472656		229.0710906982
		4638.3813476562		3484.9013671875		3121.2189941406		762.4935302734		2825.7622070312		248.8710174561
		4639.2641601562		3486.7963867188		3173.8195800781		908.9182739258		2858.6884765625		308.2708129883
		4639.7944335938		3487.9338378906		3200.0070800781		1154.5045166016		2869.2219238281		407.2704772949
		4639.9711914062		3488.3125		3215.6479492188		1407.8640136719		2874.4025878906		605.2698364258
		4640.0600585938		3488.501953125		3220.8464355469		1609.5314941406		2877.4829101562		1199.2677001953
		4640.1127929688		3488.6157226562		3223.4428710938		1826.5794677734		2878.5053710938		2189.2644042969
				3488.6538085938		3224.9992675781		2069.646484375		2878.6774902344		2591.5949707031
				3488.6726074219		3225.5180664062		2483.5900878906		2879.0151367188		2592.6472167969
						3225.7775878906		2600.9157714844		2879.3212890625		2593.6005859375
						3225.9331054688		2738.6010742188		2879.4230957031		2593.91796875
						3225.9848632812		2801.0151367188		2879.4741210938		2594.0769042969
						3226.0107421875		2798.9753417969
								2776.4731445312
								2734.2629394531
								2700.2490234375
								2667.2453613281
								2626.6965332031
								2598.6828613281
								2591.5949707031
								2572.9384765625
								2542.1479492188
								2521.0725097656
								2501.6936035156
T = 1000 C
T = 500 C
Critical T
Saturation
T = 200 C
T = 50 C
Entropy (kJ/kg-K)
Enthalpy (kJ/kg)
h-s Diagram for Water
PowerPoint
		It appears that a Power Point chart will allow individual lines to be popped onto the chart with a single
		mouse click. However, those charts need to have a common set of values along the x axis
		Can we define a set of volumes which have a data point for each isotherm and the saturation line?
		Saturation Curve				T = 50 C isotherm				T = 100 C isotherm				T = 200 C isotherm				T = 300 C isotherm				Critical isotherm				T = 500 C isotherm				T = 1000 C isotherm
		V		P		V		P		V		P		V		P		V		P		V		P		V		P		V		P
		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals		m^3/kg		Pascals
		0.0010000879		1000		0.001		2.84E+07		0.001		100000000		0.001				0.0010000879				0.0010000879				0.001				0.001
		0.0010015428		2000		0.0010015428		2.47E+07		0.0010015428		9.60E+07		0.0010015428				0.0010015428				0.0010015428				0.0010015428				0.0010015428
		0.0010054707		5000		0.0010054707		1.53E+07		0.0010054707		8.58E+07		0.0010054707				0.0010054707				0.0010054707				0.0010054707				0.0010054707
		0.001010		10000		0.001010		4.17E+06		0.001010		7.37E+07		0.0010102882				0.0010102882				0.0010102882				0.0010102882				0.0010102882
		0.0010118484		12349.3310546875		0.0010118484		12349.3310546875		0.0010118484		6.98E+07		0.0010118484				0.0010118484				0.0010118484				0.0010118484				0.0010118484
		0.0010170657		20000		0.0010170657		12349.3310546875		0.0010170657		5.72E+07		0.0010170657				0.0010170657				0.0010170657				0.0010170657				0.0010170657
		0.0010298092		50000		0.0010298092		12349.3310546875		0.0010298092		2.82E+07		0.0010298092				0.0010298092				0.0010298092				0.0010298092				0.0010298092
		0.0010431278		100000		0.0010431278		12349.3310546875		0.0010434389		101347.734375		0.0010434389				0.0010431278				0.0010431278				0.0010431278				0.00104343890.001060641		200000		0.001060641		12349.3310546875		0.001060641		101347.734375		0.001060641		142959872		0.001060641				0.001060641				0.001060641				0.001060641
		0.0010928017		500000		0.0010928017		12349.3310546875		0.0010928017		101347.734375		0.0010928017		82797688		0.0010928017				0.0010928017				0.0010928017				0.0010928017
		0.0011273494		1000000		0.0011273494		12349.3310546875		0.0011273494		101347.734375		0.0011273494		33440160		0.0011273494				0.0011273494				0.0011273494				0.0011273494
		0.001156345		1553499.25		0.001156345		12349.3310546875		0.001156345		101347.734375		0.001156345		1687808		0.001156345				0.001156345				0.001156345				0.001156345
		0.001176456		2000000		0.001176456		12349.3310546875		0.001176456		101347.734375		0.001176456		1553795.625		0.001176456		136884864		0.001176456				0.001176456				0.001176456
		0.0012857464		5000000		0.0012857464		12349.3310546875		0.0012857464		101347.734375		0.0012857464		1553795.625		0.0012857464		50109520		0.0012857464		143219392		0.0012857464				0.0012857464
		0.0014040433		8580854		0.0014040433		12349.3310546875		0.0014040433		101347.734375		0.0014040433		1553795.625		0.0014040433		8580862		0.0014040433		85571272		0.0014040433				0.0014040433
		0.0014529194		10000000		0.0014529194		12349.3310546875		0.0014529194		101347.734375		0.0014529194		1553795.625		0.0014529194		8580862		0.0014529194		70797728		0.0014529194				0.0014529194
		0.0016574394		15000000		0.0016574394		12349.3310546875		0.0016574394		101347.734375		0.0016574394		1553795.625		0.0016574394		8580862		0.0016574394		37786512		0.0016574394		131899080		0.0016574394
		0.0020408698		20000000		0.0020408698		12349.3310546875		0.0020408698		101347.734375		0.0020408698		1553795.625		0.0020408698		8580862		0.0020408698		23733296		0.0020408698		88112000		0.0020408698
		0.003		22088050		0.003		12349.3310546875		0.003		101347.734375		0.003		1553795.625		0.003		8580862		0.003		22090496		0.003		59345884		0.003		201284080
		0.0070000002		18584896		0.0070000002		12349.3310546875		0.0070000002		101347.734375		0.0070000002		1553795.625		0.0070000002		8580862		0.0070000002		20455956		0.0070000002		34759672		0.0070000002		81059264
		0.0099999998		15316675		0.0099999998		12349.3310546875		0.0099999998		101347.734375		0.0099999998		1553795.625		0.0099999998		8580862		0.0099999998		17895004		0.0099999998		27076868		0.0099999998		56927520
		0.0199999996		9181853		0.0199999996		12349.3310546875		0.0199999996		101347.734375		0.0199999996		1553795.625		0.0199999996		8580862		0.0199999996		11666531		0.0199999996		15515990		0.0199999996		28813848
		0.0216745604		8580854		0.0216745604		12349.3310546875		0.0216745604		101347.734375		0.0216745604		1553795.625		0.0216745604		8580862		0.0216745604		10984456		0.0216745604		14473696		0.0216745604		26621214
		0.0500000007		3982750		0.0500000007		12349.3310546875		0.0500000007		101347.734375		0.0500000007		1553795.625		0.05		4603129		0.0500000007		5436813		0.0500000007		6753890.5		0.0500000007		11651130
		0.1000000015		1992371.25		0.1000000015		12349.3310546875		0.1000000015		101347.734375		0.1000000015		1553795.625		0.1		2474430.75		0.1000000015		2852562.5		0.1000000015		3472211		0.1000000015		5849789.5
		0.1273585111		1553795.625		0.1273585111		12349.3310546875		0.1273585111		101347.734375		0.1273585111		1553795.625		0.1273585111		1.97E+06		0.1273585111		2262524.5		0.1273585111		2742495.25		0.1273585111		4597424
		0.200000003		970882.9375		0.200000003		12349.3310546875		0.200000003		101347.734375		0.2		1027871.0625		0.2		1280137.125		0.200000003		1459985.375		0.200000003		1760085.125		0.200000003		2931267.75
		0.5		368110.4375		0.5		12349.3310546875		0.5		101347.734375		0.5		426722.125		0.5		522268.8125		0.5		592077.875		0.5		709794.5625		0.5		1174078.25
		1		175678.734375		1		12349.3310546875		1		101347.734375		1		215882.171875		1		262827.15625		1		297384.5625		1		355857.0625		1		587304.375
		1.6729232073		101347.734375		1.6729232073		12349.3310546875		1.6729232073		101347.734375		1.6729232073		1.30E+05		1.6729232073		1.58E+05		1.6729232073		178086.78125		1.6729232073		212946.4375		1.6729232073		351128.84375
		2		83734.2578125		2		12349.3310546875		2		84993.75		2		108563.9375		2		131835.765625		2		149028.46875		2		178168.40625		2		293718.875
		5		31469.1171875		5		12349.3310546875		5		34265.6328125		5		43574.08984375		5		52835.4921875		5		59692.0390625		5		71324.9296875		5		117503.5859375
		10		15035.4345703125		10		12349.3310546875		10		17177.126953125		10		21811.716796875		10		26434.599609375		10		29859.458984375		10		35672.0546875		10		58754.46875
		12.0319795609		12349.3310546875		12.0319795609		12349.3310546875		12.0319795609		14282.4296875		12.0319795609		1.81E+04		12.0319795609		2.20E+04		12.0319795609		24818.6328125		12.0319795609		29649.05078125		12.0319795609		48832.296875
		20		7196.8666992188		20		7440.3129882812		20		8599.60546875		20		10912.0185546875		20		13221.51171875		20		14933.0888671875		20		17838.42578125		20		29377.904296875
		50		2725.5100097656		50		2980.0952148438		50		3442.4875488281		50		4366.2846679688		50		5289.6157226562		50		5974.0419921875		50		7135.9458007812		50		11751.322265625
		100		1310.3555908203		100		1490.7087402344		100		1721.6843261719		100		2183.3884277344		100		2644.9763183594		100		2987.1555175781		100		3568.0688476562		100		5875.6879882812
		200		631.09375		200		745.5195922852		200		860.9522705078		200		1091.7557373047		200		1322.5302734375		200		1493.611328125		200		1784.0584716797		200		2937.8508300781
		
		
		V		m^3/kg		P-v Diagram		0.0010000879		0.0010015428		0.0010054707		0.0010102882		0.0010118484		0.0010170657		0.0010298092		0.0010431278		0.001060641		0.0010928017		0.0011273494		0.001156345		0.001176456		0.0012857464		0.0014040433		0.0014529194		0.0016574394		0.0020408698		0.003		0.0070000002		0.0099999998		0.0199999996		0.0216745604		0.0500000007		0.1000000015		0.1273585111		0.200000003		0.5		1		1.6729232073		2		5		10		12.0319795609		20		50		100		200
		P		Pascals		Saturation Curve		1000		2000		5000		10000		12349.3310546875		20000		50000		100000		200000		500000		1000000		1553499.25		2000000		5000000		8580854		10000000		15000000		20000000		22088050		18584896		15316675		9181853		8580854		3982750		1992371.25		1553795.625		970882.9375		368110.4375		175678.734375		101347.734375		83734.2578125		31469.1171875		15035.4345703125		12349.3310546875		7196.8666992188		2725.5100097656		1310.3555908203		631.09375
		P		Pascals		T = 50 C isotherm		28420080		24663056		15287168		4171264		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		12349.3310546875		7440.3129882812		2980.0952148438		1490.7087402344		745.5195922852
		P		Pascals		T = 100 C isotherm		100000000		96038824		85838760		73668768		69807704		57181504		28214736		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		101347.734375		84993.75		34265.6328125		17177.126953125		14282.4296875		8599.60546875		3442.4875488281		1721.6843261719		860.9522705078
		P		Pascals		T = 200 C isotherm																		142959872		82797688		33440160		1687808		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1553795.625		1027871.0625426722.125		215882.171875		129644.40625		108563.9375		43574.08984375		21811.716796875		18131.580078125		10912.0185546875		4366.2846679688		2183.3884277344		1091.7557373047
		P		Pascals		T = 300 C isotherm																										136884864		50109520		8580862		8580862		8580862		8580862		8580862		8580862		8580862		8580862		8580862		4603129		2474430.75		1971914.375		1280137.125		522268.8125		262827.15625		157512.640625		131835.765625		52835.4921875		26434.599609375		21972.6484375		13221.51171875		5289.6157226562		2644.9763183594		1322.5302734375
		P		Pascals		Critical isotherm																												143219392		85571272		70797728		37786512		23733296		22090496		20455956		17895004		11666531		10984456		5436813		2852562.5		2262524.5		1459985.375		592077.875		297384.5625		178086.78125		149028.46875		59692.0390625		29859.458984375		24818.6328125		14933.0888671875		5974.0419921875		2987.1555175781		1493.611328125
		P		Pascals		T = 500 C isotherm																																		131899080		88112000		59345884		34759672		27076868		15515990		14473696		6753890.5		3472211		2742495.25		1760085.125		709794.5625		355857.0625		212946.4375		178168.40625		71324.9296875		35672.0546875		29649.05078125		17838.42578125		7135.9458007812		3568.0688476562		1784.0584716797
		P		Pascals		T = 1000 C isotherm																																						201284080		81059264		56927520		28813848		26621214		11651130		5849789.5		4597424		2931267.75		1174078.25		587304.375		351128.84375		293718.875		117503.5859375		58754.46875		48832.296875		29377.904296875		11751.322265625		5875.6879882812		2937.8508300781
T-s
		280.1273254395		318.9599975586		318.9599975586		319.324407959		773.15
		290.6508239746		318.9599975586		319.324407959		327.2010559082		318.9599975586
		291.4254821777						347.4516052246
		306.0278381348						368.8721984863
		318.9599975586						391.4805969238
		333.2144836426						415.2580322266
		354.4805358887						440.1489624023
		372.7752441406						466.0597595215
		393.3832458496						492.8244384766
		425.0064147949						520.1244567871
		453.0573486328						547.3703674316
		485.5660766602						573.5540222168
		537.1405090332						584.211920166
		584.211920166						584.211920166
		615.3873352051						584.211920166
		638.9596618652						584.211920166
		647.2824157715						584.211920166
		632.8575500488						584.211920166
		617.0636657715						584.211920166
		577.9946350098						584.211920166
		523.2960876465						584.211920166
		485.3729003906						584.211920166
		451.7770141602						584.211920166
		413.8124450684						597.4862731934
		389.3320068359						632.2977355957
		367.8860534668						681.8373474121
		343.3577636719						745.4446472168
		327.1732543945						773.15
		323.15
		312.670324707
		295.6454833984
		284.127355957
		273.598638916
Saturation
Condenser
Pump
Steam
Generator
Turbine
Entropy (kJ/kg-K)
Temperature (K)
Temperature-Entropy Rankine Cycle Diagram
P-v Data
						Saturation Properties																				T = 50 C isotherm																				P = 10 MPa isobar
						P		V		T		u		s		h		x		Error Code						P		V		T		u		s		h		x		Error Code						P		V		T		u		s		h		x		Error Code
						Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg
		280.1273254395		1000		1000		0.0010070801		6.9773254395		28.5752506256		0.1032763645		28.576499939		0		0		0		1.00E+08		100000000		0.0009730784		50		196.0089569092		0.6573936939		293.3174743652		0		0		0		2.50E-01		10,000,000		0.000996615		16.9412231445		70.1728591919		0.25		80.1395111084		0		0		290.0912231445
		290.6508239746		2000		2000		0.0009994507		17.5008239746		72.3982467651		0.2568418086		72.4002532959		0		0		0		5.00E+07		50000000		0.0009914358		50		201.8995056152		0.6798597574		251.4717712402		0		0		0		0.5		10,000,000		0.0010015413		34.9356994629		144.8605957031		0.5		154.8761138916		0		0		308.0856994629
		291.4254821777		2100		2100		0.0010032654		18.2754821777		75.6439971924		0.2679961026		75.6462478638		0		0		0		0.001		28420080		0.001		50		204.7491607666		0.6897144914		233.1692352295		0		0		0				10,000,000		0.001006		46.174		191.474		0.649		201.534		0		0		319
		306.0278381348		5000		5000		0.0010051727		32.8778381348		137.1510009766		0.473926276		137.15675354		0		0		0		0.0010118484		12349.3310546875		0.0010118484		50		209.4589996338		0.7038320303		209.471496582		0		0		0		0.75		10,000,000		0.0010096759		54.0510559082		224.1673736572		0.75		234.2629699707		0		0		327.2010559082
		318.9599975586		10000		10000		0.0010099411		45.8099975586		191.7732543945		0.6487446427		191.7832489014		0		0		0		0.002		12349.3310546875		0.0020000001		50		209.6424560547		0.7044374943		209.6671600342		0.000082134		0		0		1		10,000,000		0.0010208768		74.3016052246		308.3638305664		1		318.5721435547		0		0		347.4516052246
		333.2144836426		20000		20000		0.0010170937		60.0644836426		251.8767547607		0.8330942392		251.8970031738		0		0		0		0.005		12349.3310546875		0.0049999999		50		210.1994018555		0.7062756419		210.2611541748		0.0003314905		0		0		1.25		10,000,000		0.0010353095		95.7221984863		397.735168457		1.25		408.0879821777		0		0		368.8721984863
		354.4805358887		50000		50000		0.0010297298		81.3305358887		341.167755127		1.092867136		341.2192382812		0		0		0		0.01		12349.3310546875		0.0099999998		50		211.1276550293		0.7093392611		211.2511444092		0.0007470847		0		0		1.5		10,000,000		0.0010534121		118.3305969238		492.5739135742		1.5		503.1069335938		0		0		391.4805969238
		372.7752441406		100000		100000		0.0010430813		99.6252441406		417.8122558594		1.3036909103		417.9165039062		0		0		0		0.02		12349.3310546875		0.0199999996		50		212.984161377		0.7154663801		213.2311401367		0.001578273		0		0		1.75		10,000,000		0.0010758436		142.1080322266		593.1676635742		1.75		603.9260864258		0		0		415.2580322266
		393.3832458496		200000		200000		0.0010606647		120.2332458496		504.4395141602		1.5298799276		504.651763916		0		0		0		0.05		12349.3310546875		0.0500000007		50		218.5536499023		0.7338479161		219.1711273193		0.0040718382		0		0		2		10,000,000		0.0011034898		166.9989624023		699.7941894531		2		710.8295898438		0		0		440.1489624023
		425.0064147949		500000		500000		0.0010927916		151.8564147949		639.1873779297		1.8593251705		639.7344970703		0		0		0		0.1		12349.3310546875		0.1000000015		50		227.836151123		0.7644836903		229.0710906982		0.0082277795		0		0		2.25		10,000,000		0.001137581		192.9097595215		812.7094726562		2.25		824.0852050781		0		0		466.0597595215
		453.0573486328		1000000		1000000		0.0011273474		179.9073486328		761.366027832		2.1377363205		762.4935302734		0		0		0		0.2		12349.3310546875		0.200000003		50		246.4011383057		0.8257553577		248.8710174561		0.0165396631		0		0		2.5		10,000,000		0.0011799716		219.6744384766		932.1307373047		2.5		943.9296875		0		0		492.8244384766
		485.5660766602		2000000		2000000		0.0011764541		212.4160766602		906.565246582		2.4473495483		908.9182739258		0		0		0		0.5		12349.3310546875		0.5		50		302.0961608887		1.009570241		308.2708129883		0.0414753146		0		0		2.75		10,000,000		0.0012336485		246.9744567871		1058.2062988281		2.75		1070.5427246094		0		0		520.1244567871
		537.1405090332		5000000		5000000		0.0012857467		263.9905090332		1148.0754394531		2.9204797745		1154.5045166016		0		0		0		1		12349.3310546875		1		50		394.9211120605		1.3159284592		407.2704772949		0.0830347314		0		0		3		10,000,000		0.0013036457		274.2203674316		1190.9523925781		3		1203.9880371094		0		0		547.3703674316
		584.211920166		10000000		10000000		0.0014529191		311.061920166		1393.3342285156		3.3599638939		1407.8640136719		0		0		0		2		12349.3310546875		2		50		580.571105957		1.9286448956		605.2698364258		0.166153565		0		0		3.25		10,000,000		0.0013989889		300.4040222168		1330.1518554688		3.25		1344.1418457031		0		0		573.5540222168
		615.3873352051		15000000		15000000		0.0016574394		342.2373352051		1584.6700439453		3.68305754661609.5314941406		0		0		0		5		12349.3310546875		5		50		1137.5211181641		3.7667942047		1199.2677001953		0.4155100584		0		0				10,000,000		0.0014529191		311.061920166		1393.3342285156		3.3599638939		1407.8640136719		0		0		584.211920166
		638.9596618652		20000000		20000000		0.0020408698		365.8096618652		1785.7620849609		4.0141925812		1826.5794677734		0		0		0		10		12349.3310546875		10		50		2065.7709960938		6.8303766251		2189.2644042969		0.831104219		0		0		3.5		10,000,000		0.0024829351		311.061920166		1464.8448486328		3.5		1489.6748046875		0.0621499643		0		584.211920166
		647.2824157715		0.003		22088050		0.003		374.1324157715		2003.7415771484		4.3838248253		2069.646484375		0		0		0		12.0319795609		12349.3310546875		12.0319795609		50		2443.0080566406		8.0754041672		2591.5949707031		1		0		0		3.75		10,000,000		0.0043217749		311.061920166		1592.5095214844		3.75		1635.7277832031		0.173103407		0		584.211920166
		632.8575500488		0.007		18584896		0.0070000002		359.7075500488		2353.4938964844		5.0571789742		2483.5900878906		1		0		0		20		7440.3129882812		20		50		2443.8410644531		8.3118257523		2592.6472167969		0		0		0		4		10,000,000		0.0061606145		311.061920166		1720.1739501953		4		1781.7807617188		0.2840568423		0		584.211920166
		617.0636657715		0.01		15316675		0.0099999998		343.9136657715		2447.7495117188		5.2888450623		2600.9157714844		1		0		0		50		2980.0952148438		50		50		2444.595703125		8.7364244461		2593.6005859375		0		0		0		4.25		10,000,000		0.0079994546		311.061920166		1847.8386230469		4.25		1927.8337402344		0.3950102925		0		584.211920166
		577.9946350098		0.02		9181853		0.0199999996		304.8446350098		2554.9638671875		5.6646595001		2738.6010742188		1		0		0		100		1490.7087402344		100		50		2444.8471679688		9.0568933487		2593.91796875		0		0		0		4.5		10,000,000		0.0098382942		311.061920166		1975.5032958984		4.5		2073.88671875		0.5059637427		0		584.211920166
		523.2960876465		0.05		3982750		0.0500000007		250.1460876465		2601.8774414062		6.0710382462		2801.0151367188		1		0		0		200		745.5195922852		200		50		2444.9729003906		9.3770751953		2594.0769042969		0		0		0		4.75		10,000,000		0.0116771339		311.061920166		2103.1677246094		4.75		2219.9396972656		0.6169171929		0		584.211920166
		485.3729003906		0.1		1992371.25		0.1000000015		212.2229003906		2599.7380371094		6.3413991928		2798.9753417969		1		0		0																						5		10,000,000		0.0135159744		311.061920166		2230.8325195312		5		2365.9926757812		0.7278706431		0		584.211920166
		451.7770141602		0.2		970882.9375		0.200000003		178.6270141602		2582.2966308594		6.5957322121		2776.4731445312		1		0		0				T = 100 C isotherm																		5.25		10,000,000		0.015354814		311.061920166		2358.4970703125		5.25		2512.0456542969		0.8388240933		0		584.211920166
		413.8124450684		0.5		368110.4375		0.5		140.6624450684		2550.2075195312		6.9227585793		2734.2629394531		1		0		0				P		V		T		u		s		h		x		Error Code		0		5.5		10,000,000		0.0171936527		311.061920166		2486.1616210938		5.5		2658.0986328125		0.9497775435		0		584.211920166
		389.3320068359		1		175678.734375		1		116.1820068359		2524.5703125		7.1695685387		2700.2490234375		1		0		0				Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg						0				10,000,000		0.0180259943		311.061920166		2543.9482421875		5.613161087		2724.2087402344		1		0		584.211920166
		367.8860534668		2		83734.2578125		2		94.7360534668		2499.7768554688		7.418302536		2667.2453613281		1		0		0		0.001		100000000		0.0010000423		100		394.6253356934		1.2365700006		494.6303405762		0		0		0		5.75		10,000,000		0.0197829455		324.3362731934		2607.1867675781		5.75		2805.0163574219		0		0		597.4862731934
		343.3577636719		5		31469.1171875		5		70.2077636719		2469.3510742188		7.7513313293		2626.6965332031		1		0		0		0.0010384951		10000000		0.0010384951		100		415.7702331543		1.2986160517		426.1547546387		0		0		0		6		10,000,000		0.0232329369		359.1477355957		2726.1086425781		6		2958.4377441406		0		0		632.2977355957
		327.1732543945		10		15035.4345703125		10		54.0232543945		2448.3286132812		8.0067329407		2598.6828613281		1		0		0		0.0010434389		101347.734375		0.0010434389		100		419.3838806152		1.3079042435		419.4895019531		0		0		0		6.25		10,000,000		0.0270207487		408.6873474121		2852.1923828125		6.25		3122.4001464844		0		0		681.8373474121
		323.15		12.0319795609		12349.3310546875		12.0319795609		50		2443.0080566406		8.0754041672		2591.5949707031		1		0		0		0.002		101347.734375		0.0020000001		100		420.5777587891		1.3113635778		420.7803039551		0.0005721471		0		0		6.5		10,000,000		0.0311331674		472.2946472168		2989.2016601562		6.5		3300.533203125		0		0		745.4446472168
		312.670324707		20		7196.8666992188		20		39.520324707		2429.0002441406		8.2651395798		2572.9384765625		1		0		0		0.005		101347.734375		0.0049999999		100		424.3219909668		1.3222125769		424.8286132812		0.0023665344		0		0		500		10,000,000		0.0327864923		500		3045.3068847656		6.5956840515		3373.1716308594		0		0		773.15
		295.6454833984		50		2725.5100097656		50		22.4954833984		2405.8723144531		8.6111927032		2542.1479492188		1		0		0		0.01		101347.734375		0.0099999998		100		430.5624389648		1.3402942419		431.5758056641		0.0053571798		0		0		6.75		10,000,000		0.0355423354		548.2873535156		3140.7282714844		6.75		3496.1516113281		0		0		821.4373535156
		284.127355957		100		1310.3555908203		100		10.977355957		2390.037109375		8.8761510849		2521.0725097656		1		0		0		0.02		101347.734375		0.0199999996		100		443.0433044434		1.376457572		445.0701599121		0.0113384714		0		0		7		10,000,000		0.0402458273		635.4683837891		3309.7236328125		7		3712.1818847656		0		0		908.6183837891
		273.598638916		200		631.09375		200		0.448638916		2375.4748535156		9.1436481476		2501.6936035156		1		0				0.05		101347.734375		0.0500000007		100		480.4859313965		1.4849476814		485.5532226562		0.0292823464		0		0		7.25		10,000,000		0.0452664569		733.2961425781		3498.6831054688		7.25		3951.3474121094		0		0		1006.4461425781
		373.15		1.6729232073		101347.734375		1.6729232073		100		2506.0358886719		7.3539810181		2675.5830078125		1		0				0.1		101347.734375		0.1000000015		100		542.8903198242		1.6657643318		553.0250244141		0.0591888018		0		0		7.5		10,000,000		0.0506356359		841.4736328125		3709.9086914062		7.5		4216.2646484375		0		0		1114.6236328125
		473.1408752441		0.001156345		1553499.25		0.001156345		199.9908752441		850.5833740234		2.3304858208		852.3796386719		0		0				0.2		101347.734375		0.200000003		100		667.6990356445		2.027397871		687.9685058594		0.1190017164		0		0		7.75		10,000,000		0.0563831553		959.7253417969		3945.65625		7.75		4509.4858398438		0		0		1232.8753417969
		573.1499694824		0.0014040433		8580854		0.0014040433		299.9999694824		1332.3638916016		3.2538225651		1344.4116210938		0		0				0.5		101347.734375		0.5		100		1042.1253662109		3.1122980118		1092.7990722656		0.2984404564		0		0		8		10,000,000		0.0625349581		1087.8165283203		4208.1323242188		8		4833.4775390625		0		0		1360.9665283203
		573.1499694824		0.0216745604		8580854		0.0216745604		299.9999694824		2562.5004882812		5.7035746574		2748.4870605469		1		0				1		101347.734375		1		100		1666.1689453125		4.9204654694		1767.5167236328		0.597505033		0		0		8.25		10,000,000		0.0691199005		1225.7839355469		4499.611328125		8.25		5190.8100585938		0		0		1498.9339355469
		473.15		0.1273585111		1553795.625		0.1273585111		200		2594.83203125		6.4313855171		2792.7209472656		1		0				1.6729232073		101347.734375		1.6729232073		100		2506.0358886719		7.3539810181		2675.5830078125		1		0		0		8.5		10,000,000		0.076124765		1299.8499755859		4660.6987304688		8.5		5387.1455078125		0		0		1572.9999755859
																								2		84993.75		2		100		2507.6774902344		7.4396276474		2677.6650390625		0		0		0		8.75		10,000,000		0.0832633525		1299.8499755859		4662.5708007812		8.75		5388.9750976562		0		0		1572.9999755859
																								5		34265.6328125		5		100		2512.6850585938		7.8723583221		2684.0131835938		0		0		0		9		10,000,000		0.0904747173		1299.8499755859		4664.1689453125		9		5390.5361328125		0		0		1572.9999755859
																								10		17177.126953125		10		1002514.3439941406		8.195514679		2686.115234375		0		0		0
																								12.0319795609		14282.4296875		12.0319795609		100		2514.6237792969		8.2814369202		2686.4697265625		0		0		0
																								20		8599.60546875		20		100		2515.1716308594		8.517036438		2687.1638183594		0		0		0
																								50		3442.4875488281		50		100		2515.6677246094		8.9408884048		2687.7922363281		0		0		0				P = 10 kPa isotherm
																								100		1721.6843261719		100		100		2515.8327636719		9.2611074448		2688.0012207031		0		0		0				P		V		T		u		s		h		x		Error Code
																								200		860.9522705078		200		100		2515.9155273438		9.58116436		2688.1059570312		0		0						Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg
																																												2.50E-01		10,000		0.001001192		16.8183288574		70.1391983032		0.25		70.1492996216		0		0		289.9683288574
																										T = 200 C isotherm																0		0.5		10,000		0.0010058597		34.6771850586		144.8419036865		0.5		144.8521728516		0		0		307.8271850586
																										P		V		T		u		s		h		x		Error Code		0				10,000		0.0010099411		45.8099975586		191.7732543945		0.6487446427		191.7832489014		0		0		318.9599975586
																										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg						0		0.75		10,000		0.1990846395		45.8099975586		222.0889282227		0.75		224.0796508789		0.0134996772		0		318.9599975586
																								0.001		100000000		0.0010827142		200		794.9663696289		2.2061827183		903.237121582		0		0		0		1		10,000		0.688131988		45.8099975586		296.9384460449		1		303.8196411133		0.0468304455		0		318.9599975586
																								0.001147975		10000000		0.001147975		200		844.164855957		2.3170874119		855.6442871094		0		0		0		1.25		10,000		1.1771793365		45.8099975586		371.7879638672		1.25		383.5596618652		0.0801612139		0		318.9599975586
																								0.001156345		1553795.625		0.001156345		200		850.6242675781		2.3305718899		852.4208984375		0		0		0		1.5		10,000		1.6662267447		45.8099975586		446.637512207		1.5		463.2996520996		0.1134919822		0		318.9599975586
																								0.002		1553795.625		0.0020000001		200		862.2841796875		2.3579854965		865.3916625977		0.0066849492		0		0		1.75		10,000		2.1552741528		45.8099975586		521.4869995117		1.75		543.0396118164		0.1468227506		0		318.9599975586
																								0.005		1553795.625		0.0049999999		200		903.7464599609		2.4554674625		911.5153198242		0.0304563306		0		0		2		10,000		2.6443214417		45.8099975586		596.3365478516		2		622.7796020508		0.1801535189		0		318.9599975586
																								0.01		1553795.625		0.0099999998		200		972.8500976562		2.6179375648		988.3880004883		0.0700753033		0		0		2.25		10,000		3.133368969		45.8099975586		671.1860351562		2.25		702.5196533203		0.2134842873		0		318.9599975586
																								0.02		1553795.625		0.0199999996		200		1111.0576171875		2.9428777695		1142.1334228516		0.1493132412		0		0		2.5		10,000		3.6224162579		45.8099975586		746.0355834961		2.5		782.2596435547		0.2468150556		0		318.9599975586
																								0.05		1553795.625		0.0500000007		200		1525.6799316406		3.9176976681		1603.3696289062		0.3870270848		0		0		2.75		10,000		4.1114635468		45.8099975586		820.8851318359		2.75		861.9996337891		0.280145824		0		318.9599975586
																								0.1		1553795.625		0.1000000015		200		2216.7170410156		5.5423979759		2372.0964355469		0.7832167745		0		0		3		10,000		4.6005110741		45.8099975586		895.7346191406		3		941.7396240234		0.3134765923		0		318.9599975586
																								0.1273585111		1553795.625		0.1273585111		200		2594.83203125		6.4313855171		2792.7209472656		1		0		0		3.25		10,000		5.0895586014		45.8099975586		970.5841064453		3.25		1021.4796142578		0.3468073606		0		318.9599975586
																								0.2		1027871.0625		0.200000003		200		2620.1879882812		6.6776914597		2825.7622070312		0		0		0		3.5		10,000		5.5786056519		45.8099975586		1045.4337158203		3.5		1101.2196044922		0.380138129		0		318.9599975586
																								0.5		426722.125		0.5		200		2645.3273925781		7.1376600266		2858.6884765625		0		0		0		3.75		10,000		6.0676531792		45.8099975586		1120.283203125		3.75		1180.9595947266		0.4134688973		0		318.9599975586
																								1		215882.171875		1		200		2653.33984375		7.4692230225		2869.2219238281		0		0		0		4		10,000		6.5567007065		45.8099975586		1195.1326904297		4		1260.6995849609		0.4467996657		0		318.9599975586
																								2		108563.9375		2		200		2657.2746582031		7.7948174477		2874.4025878906		0		0		0		4.25		10,000		7.045747757		45.8099975586		1269.9822998047		4.25		1340.4395751953		0.480130434		0		318.9599975586
																								5		43574.08984375		5		200		2659.6125488281		8.2210712433		2877.4829101562		0		0		0		4.5		10,000		7.5347952843		45.8099975586		1344.8317871094		4.5		1420.1795654297		0.5134612322		0		318.9599975586
																								10		21811.716796875		10		200		2660.3879394531		8.5420827866		2878.5053710938		0		0		0		4.75		10,000		8.0238428116		45.8099975586		1419.6812744141		4.75		1499.9196777344		0.5467919707		0		318.9599975586
																								12.0319795609		18131.580078125		12.0319795609		200		2660.5187988281		8.6276435852		2878.6774902344		0		0		0		5		10,000		8.5128898621		45.8099975586		1494.5308837891		5		1579.6596679688		0.5801227689		0		318.9599975586
																								20		10912.0185546875		20		200		2660.7749023438		8.8625354767		2879.0151367188		0		0		0		5.25		10,000		9.0019369125		45.8099975586		1569.3803710938		5.25		1659.3996582031		0.6134535074		0		318.9599975586
																								50		4366.2846679688		50		200		2661.0070800781		9.2857475281		2879.3212890625		0		0		0		5.5		10,000		9.4909849167		45.8099975586		1644.2298583984		5.5		1739.1396484375		0.6467843056		0		318.9599975586
																								100		2183.3884277344		100		200		2661.0842285156		9.6057529449		2879.4230957031		0		0				5.75		10,000		9.9800319672		45.8099975586		1719.0793457031		5.75		1818.8796386719		0.6801150441		0		318.9599975586
																								200		1091.7557373047		200		200		2661.1228027344		9.925702095		2879.4741210938		0		0				6		10,000		10.4690790176		45.8099975586		1793.9288330078		6		1898.6196289062		0.7134458423		0		318.9599975586
																																										0		6.25		10,000		10.9581270218		45.8099975586		1868.7783203125		6.25		1978.3596191406		0.7467765808		0		318.9599975586
																										T = 300 C isotherm																0		6.5		10,000		11.4471740723		45.8099975586		1943.6280517578		6.5		2058.099609375		0.780107379		0		318.9599975586
																										P		V		T		u		s		h		x		Error Code		0		6.75		10,000		11.9362211227		45.8099975586		2018.4775390625		6.75		2137.8395996094		0.8134381175		0		318.9599975586
																										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg						0		7		10,000		12.4252691269		45.8099975586		2093.3269042969		7		2217.5795898438		0.8467689157		0		318.9599975586
																								0.0012130128		100000000		0.0012130128		300		1207.0416259766		3.0206084251		1328.3431396484		0		0		0		7.25		10,000		12.9143161774		45.8099975586		2168.1765136719		7.25		2297.3195800781		0.8800996542		0		318.9599975586
																								0.0013975828		10000000		0.0013975828		300		1328.5965576172		3.2471649647		1342.5731201172		0		0		0		7.5		10,000		13.4033641815		45.8099975586		2243.0258789062		7.5		2377.0595703125		0.9134304523		0		318.9599975586
																								0.0014040433		8580862		0.0014040433		300		1332.3656005859		3.2538256645		1344.4138183594		0		0		0		7.75		10,000		13.892411232		45.8099975586		2317.8754882812		7.75		2456.7995605469		0.9467611909		0		318.9599975586
																								0.002		8580862		0.0020000001		300		1368.5317382812		3.3258485794		1385.6938476562		0.0294001773		0		0		8		10,000		14.3814582825		45.8099975586		2392.7250976562		8		2536.5395507812		0.980091989		0		318.9599975586
																								0.005		85808620.0049999999		300		1550.5894775391		3.6884069443		1593.494140625		0.1773983687		0		0				10,000		14.6735601425		45.8099975586		2437.431640625		8.1493215561		2584.1672363281		1		0		318.9599975586
																								0.01		8580862		0.0099999998		300		1854.0190429688		4.2926707268		1939.8280029297		0.4240620136		0		0		8.25		10,000		15.4857397079		63.221496582		2462.2907714844		8.25		2617.1481933594		0		0		336.371496582
																								0.02		8580862		0.0199999996		300		2460.8779296875		5.5011982918		2632.4956054688		0.9173893332		0		0		8.5		10,000		17.6837177277		110.5215454102		2530.1928710938		8.5		2707.0300292969		0		0		383.6715454102
																								0.0216745604		8580862		0.0216745604		300		2562.5002441406		5.7035737038		2748.4870605469		1		0		0		8.75		10,000		20.1618289948		164.0323486328		2607.8837890625		8.75		2809.501953125		0		0		437.1823486328
																								0.05		4603129		0.0500000007		300		2708.7028808594		6.2662382126		2938.8596191406		0		0		0		9		10,000		22.9424095154		224.1755981445		2696.748046875		9		2926.1721191406		0		0		497.3255981445
																								0.1		2474430.75		0.1000000015		300		2761.6677246094		6.6486468315		3009.1108398438		0		0		0
																								0.2		1280137.125		0.200000003		300		2787.1359863281		6.9981245995		3043.1635742188		0		0		0		Pump
																								0.5		522268.8125		0.5		300		2802.0283203125		7.4381194115		3063.1628417969		0		0		0				P		V		T		u		s		h		x		Error Code
																								1		262827.15625		1		300		2806.9221191406		7.7636060715		3069.7492675781		0		0		0				Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg
																								2		131835.765625		2		300		2809.3552246094		8.086274147		3073.0268554688		0		0		0		Inlet		10,000		0.0010099411		45.8099975586		191.7732543945		0.6487446427		191.7832489014		0		0		318.9599975586
																								5		52835.4921875		5		300		2810.810546875		8.5108089447		3074.9880371094		0		0		0		Outlet		10,000,000		0.0010060103		46.174407959		191.4741363525		0.6487446427		201.5341491699		0		0		319.324407959
																								10		26434.599609375		10		300		2811.294921875		8.8312540054		3075.6411132812		0		0		0
																								20		13221.51171875		20		300		2811.537109375		9.1514234543		3075.9672851562		0		0		0		Turbine
																								50		5289.6157226562		50		300		2811.6821289062		9.5744667053		3076.1630859375		0		0		0				P		V		T		u		s		h		x		Error Code
																								100		2644.9763183594		100		300		2811.73046875		9.8944158554		3076.2282714844		0		0						Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg
																								200		1322.5302734375		200		300		2811.7546386719		10.2143383026		3076.2607421875		0		0				Inlet		10,000,000		0.0327864923		500		3045.3068847656		6.5956840515		3373.1716308594		0		0		773.15
																																												Outlet		10,000		11.6343507767		45.8099975586		1972.2756347656		6.5956840515		2088.6188964844		0.7928642631		0		318.9599975586
																										T = 374.1 isotherm
																										P		V		T		u		s		h		x		Error Code		0		Condenser
																										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg						0				P		V		T		u		s		h		x		Error Code
																								0.0013661224		100000000		0.0013661224		374.1000061035		1527.9857177734		3.5718967915		1664.5982666016		0		0		0				Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg
																								0.0014375476		75000000		0.0014375476		374.1000061035		1570.2646484375		3.6467859745		1678.0816650391		0		0		0		Inlet		10,000.000		11.634		45.810		1,972.276		6.596		2,088.619		0.793		0		318.9599975586
																								0.0015543412		50000000		0.0015543412		374.1000061035		1632.9963378906		3.754750967		1710.7135009766		0		0		0		Outlet		10,000		0		46		192		1		192		0		0		318.9599975586
																								0.002		24181000		0.0020000001		374.1000061035		1803.0750732422		4.0397267342		1851.4371337891		0		0		0
																								0.002843854		22079540		0.002843854		374.1000061035		1982.9028320312		4.3468565941		2045.6938476562		0		0		0
																								0.0033218244		22079540		0.0033218244		374.1000061035		2053.5893554688		4.4723720551		2126.9338378906		1		0		0
																								0.005		21759468		0.0049999999		374.1000061035		2252.1447753906		4.8361368179		2360.9418945312		0		0		0
																								0.01		17892072		0.0099999998		374.1000061035		2546.8908691406		5.4458150864		2725.8115234375		0		0		0
																								0.02		11665344		0.0199999996		374.1000061035		2731.8640136719		5.9544596672		2965.1706542969		0		0		0
																								0.0244644266		10000000		0.0244644266		374.1000061035		2767.3862304688		6.0837836266		3012.0307617188		0		0		0
																								0.05		5436423		0.0500000007		374.1000061035		2849.3977050781		6.4973158836		3121.2189941406		0		0		0
																								0.1		2852382		0.1000000015		374.1000061035		2888.5812988281		6.8569455147		3173.8195800781		0		0		0
																								0.2		1459898.75		0.200000003		374.1000061035		2908.02734375		7.19647789		3200.0070800781		0		0		0
																								0.5		592044.0625		0.5		374.1000061035		2919.6259765625		7.6310372353		3215.6479492188		0		0		0
																								1		297367.8125		1		374.1000061035		2923.4787597656		7.9548063278		3220.8464355469		0		0		0
																								2		149020.125		2		374.1000061035		2925.4025878906		8.2766342163		3223.4428710938		0		0		0
																								5		59688.7109375		5		374.1000061035		2926.5556640625		8.7006702423		3224.9992675781		0		0		0
																								10		29857.796875		10		374.1000061035		2926.9399414062		9.0209503174		3225.5180664062		0		0		0
																								20		14932.2587890625		20		374.1000061035		2927.1323242188		9.3410377502		3225.7775878906		0		0		0
																								50		5973.7094726562		50		374.1000061035		2927.2475585938		9.7640314102		3225.9331054688		0		0		0
																								100		2986.9892578125		100		374.1000061035		2927.2856445312		10.0839633942		3225.9848632812		0		0
																								200		1493.5281982422		200		374.1000061035		2927.3049316406		10.403878212		3226.0107421875		0		0
		
																										T = 500 C isotherm
																										P		V		T		u		s		h		x		Error Code		0
																										Pascals		m^3/kg		deg C		kJ/kg		kJ/kg-K		kJ/kg						0
																								0.0018902613		100000000		0.0018902613		500		2123.3056640625		4.4842619896		2312.3317871094		0		0		0
																								0.0023095764		75000000		0.0023095764		500		2251.3928222656		4.6963043213		2424.6103515625		0		0		0
																								0.005		42984896		0.0049999999		500		2632.3608398438		5.3767843246		2847.28515625		0		0		0
																								0.01		27076868		0.0099999998		500		2858.0368652344		5.8871569633		3128.8054199219		0		0		0
																								0.02		15515990		0.0199999996		500		2990.73046875		6.3206896782		3301.0502929688		0		0		0
																								0.0327864923		10000000		0.0327864923		500		3045.3068847656		6.5956840515		3373.1716308594		0		0		0
																								0.05		6753890.5		0.0500000007		500		3075.0656738281		6.8159928322		3412.7602539062		0		0		0
																								0.1		3472211		0.1000000015		500		3103.4970703125		7.1602678299		3450.7180175781		0		0		0
																								0.2		1760085.125		0.200000003		500		3117.7021484375		7.4923286438		3469.7192382812		0		0		0
																								0.5		709794.5625		0.5		500		3126.2111816406		7.9224872589		3481.1083984375		0		0		0
																								1		355857.0625		1		500		3129.0441894531		8.2448043823		3484.9013671875		0		0		0
																								2		178168.40625		2		500		3130.4597167969		8.5659103394		3486.7963867188		0		0		0
																								5		71324.9296875		5		500		3131.3090820312		8.9895133972		3487.9338378906		0		0		0
																								10		35672.0546875		10		500