Download e-book for kindle: Advanced Thermodynamics for Engineers by Jr. Wark Kenneth

By Jr. Wark Kenneth

ISBN-10: 0070682925

ISBN-13: 9780070682924

This article is meant to supply an advent to complex thermodynamics for mechanical and aerospace engineering scholars, protecting issues corresponding to: availability research; thermodynamic houses; chemical reactions; and a statistical point of view of entropy.

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Try it! ) Also, by going back to Properties, one can examine the effect of using another equation of state, for example the Soave form of the Redlich–Kwong (SRK) equation. While the process just simulated would work for the liquefaction of propane, it would not be acceptable since the propane vapor leaving the separator is released to the atmosphere, which is an economic problem, since it is a valuable resource, and an environmental problem, being explosive and a greenhouse gas. A simple way to deal with this is to recycle the propane vapor back into the process by mixing it with the feed and returning it to the compressor.

Repeat the propane liquefaction with recycle calculation in the text but using the Soave–Redlich– Kwong equation of state instead of the Peng–Robinson equation. Compare the compressor work required and the amount of liquefied propane produced with the values obtained using the Peng–Robinson equation. Do you consider the differences significant? 4. Repeat the propane liquefaction with recycle calculation using the Soave–Redlich–Kwong equation of state using an increased compressor outlet pressure of 20 bar.

This simulation is then run. We see by clicking on the Control panel, which produces the results in Fig. 2-24, that the calculation converged on the third iteration. Figure 2-24 The stream results seen in Results Summary>Streams are given in the window of Fig. 2-25. 62 kg/hr of propane for each 60 kg/hr of propane initially fed into the process. 5 kg/hr. 45◦ C. 24 Chapter 2 Two Simple Simulations Figure 2-25 Now going to the Results Summary>Models and then to the Compr tab (Fig. 199 kW for an initial feed flow of 60 kg/hr of propane to produce 60 kg/hr of liquid propane.

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Advanced Thermodynamics for Engineers by Jr. Wark Kenneth


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