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Refrigerant-134a is used as the working fluid in a simple ideal Rankine cycle which operates the boiler at \(2000 \mathrm{kPa}\) and the condenser at \(24^{\circ} \mathrm{C}\). The mixture at the exit of the turbine has a quality of 93 percent. Determine the turbine inlet temperature, the cycle thermal efficiency, and the back-work ratio of this cycle.

Short Answer

Expert verified
Answer: To determine the turbine inlet temperature, cycle thermal efficiency, and back-work ratio, follow these steps: 1. Draw a T-s diagram and identify the state points of the cycle. 2. Use the property tables for Refrigerant-134a to determine the enthalpy and entropy at each state using the given conditions. 3. Find the turbine inlet temperature (State 2) using the saturation temperature at the given boiler pressure. 4. Calculate the heat added and work extracted during the cycle. 5. Calculate the cycle thermal efficiency using the ratio of net work output to heat input. 6. Calculate the back-work ratio using the ratio of pump work to turbine work. The exact values for the turbine inlet temperature, cycle thermal efficiency, and back-work ratio will depend on the specific values obtained from the Refrigerant-134a property tables.

Step by step solution

01

Identify the state points and diagram the cycle

First, draw a T-s diagram for the Rankine cycle and label the state points. The cycle consists of 4 states: 1. At the boiler inlet (liquid phase) 2. At the boiler exit/turbine inlet (saturated vapor phase) 3. At the turbine exit/condenser inlet (mixture of vapor and liquid) 4. At the condenser exit/pump inlet (liquid phase)
02

Find the enthalpy and entropy at each state

We will use the property tables for Refrigerant-134a to determine the enthalpy and entropy at each state. We are given the boiler pressure and condenser temperature, which will help us find the properties. At state 1 (P1 = \(2000 \mathrm{kPa}\), Saturated Liquid): \(h_1 = h_{f}\ @(P_1) \) \(s_1 = s_{f}\ @(P_1)\) At state 2 (P2 = \(2000 \mathrm{kPa}\), Saturated Vapor): \(h_2 = h_{g}\ @(P_2)\) \(s_2 = s_{g}\ @(P_2)\) At state 3 (T3 = \(24^{\circ} \mathrm{C}\), Quality, x = 0.93): \(h_3 = h_{mixture}\ @(T_3, x) = h_{f}\ @(T_3) + x\cdot (h_{g}\ @(T_3) - h_{f}\ @(T_3))\) \(s_3 = s_{mixture}\ @(T_3, x) = s_{f}\ @(T_3) + x\cdot (s_{g}\ @(T_3) - s_{f}\ @(T_3))\) At state 4 (P4 = \(2400 \mathrm{kPa}\), Saturated Liquid): \(h_4 = h_{f}\ @(P_4)\) \(s_4 = s_{f}\ @(P_4)\)
03

Find the Turbine Inlet Temperature

The temperature at turbine inlet (State 2) is the boiler exit temperature. \(T_2 = T_{saturation}\ @(P_2)\)
04

Calculate the heat added and work extracted

Heat added in the boiler (Q_in): \(Q_{in} = h_2 - h_1\) Turbine Work (W_turbine): \(W_{turbine} = h_2 - h_3\) Pump Work (W_pump): \(W_{pump} = h_4 - h_1\)
05

Calculate the Cycle Thermal Efficiency

The cycle thermal efficiency is given by the ratio of net work output to heat input: \(\eta_{thermal} = \frac{W_{net}}{Q_{in}} = \frac{(W_{turbine} - W_{pump})}{Q_{in}}\)
06

Calculate the Back-Work Ratio

The back-work ratio is given by the ratio of pump work to turbine work: \(Back-work\ Ratio = \frac{W_{pump}}{W_{turbine}}\) Using the R-134a property tables and the formulas above, the values for the turbine inlet temperature, cycle thermal efficiency, and back-work ratio can be calculated.

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Most popular questions from this chapter

A simple ideal Rankine cycle with water as the working fluid operates between the pressure limits of 2500 psia in the boiler and 5 psia in the condenser. What is the minimum temperature required at the turbine inlet such that the quality of the steam leaving the turbine is not below 80 percent. When operated at this temperature, what is the thermal efficiency of this cycle?

Starting with Eq. \(10-20\), show that the exergy destruction associated with a simple ideal Rankine cycle can be expressed as \(x_{\text {dest }}=q_{\text {in }}\left(\eta_{\text {th,Camot }}-\eta_{\text {th }}\right),\) where \(\eta_{\text {th }}\) is efficiency of the Rankine cycle and \(\eta_{\mathrm{th}, \mathrm{Camot}}\) is the efficiency of the Carnot cycle operating between the same temperature limits.

A simple ideal Rankine cycle which uses water as the working fluid operates its condenser at \(40^{\circ} \mathrm{C}\) and its boiler at \(300^{\circ} \mathrm{C}\). Calculate the work produced by the turbine, the heat supplied in the boiler, and the thermal efficiency of this cycle when the steam enters the turbine without any superheating.

Using EES (or other) software, investigate the effect of reheat pressure on the performance of an ideal Rankine cycle. The maximum and minimum pressures in the cycle are \(15 \mathrm{MPa}\) and \(10 \mathrm{kPa}\) respectively, and steam enters both stages of the turbine at \(500^{\circ} \mathrm{C}\). The reheat pressure is varied from 12.5 to 0.5 MPa. Determine the thermal efficiency of the cycle and plot it against the reheat pressure, and discuss the results.

An ideal Rankine steam cycle modified with two closed feedwater heaters is shown below. The power cycle receives \(75 \mathrm{kg} / \mathrm{s}\) of steam at the high pressure inlet to the turbine. The feedwater heater exit states for the boiler feedwater and the condensed steam are the normally assumed ideal states. The fraction of mass entering the high pressure turbine at state 5 that is extracted for the feedwater heater operating at \(1400 \mathrm{kPa}\) is \(y=0.1446 .\) Use the data provided in the tables given below to (a) Sketch the \(T\) -s diagram for the ideal cycle. (b) Determine the fraction of mass, \(z\), that is extracted for the closed feedwater heater operating at the \(245 \mathrm{kPa}\) extraction pressure. (c) Determine the required cooling water flow rate, in \(\mathrm{kg} / \mathrm{s}\), to keep the cooling water temperature rise in the condenser to \(10^{\circ} \mathrm{C}\). Assume \(c_{p}=4.18 \mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\) for cooling water (d) Determine the net power output and the thermal efficiency of the plant.

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