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A problem were given some information about helium at 68 degrees fahrenheit and 14 .7 psi.
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It's a large tank flow steadily through converging nozzle to receiver pipe.
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The cross -section area at the throat to the converging converging passage is 0 .05 feet cubed.
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We're asked to determine the mass flow rate through the duct if the receiver pressure is first 10 psis and second 5 psis.
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Okay, let's start with a.
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Okay, that will be the following equation.
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And we're going to use textbook table for helium, for helium info, and we'll get the following.
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This will be 1 .66 over 1 .66 minus 1 .6.
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And this will equal 7 .17 psi .8.
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Now we're going to compare the receiver pressure is greater than my critical pressure.
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That means we can use the receiver pressure as the throat pressure, and then we can evaluate the mock number.
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And i'll have p over pt, and that'll be k minus 1 over k.
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And this will equal, after we plug our values again, take that times 14 .7 over 10 to the 1 .66 minus 1 over 1 .66 minus 1 .6 minus 1.
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And this will equal 7 .0 .78.
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And then the temperature in the throat equal t over 1 plus k minus 1 over 2 times mok squared.
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And this will equal 528 divided by 1 plus 1 .66 minus 1 ,000, and we'll take that over 2 and then we'll multiply that by 0 .78 squared.
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This will be degrees rankin and then this will equal 453.
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Okay and we can collect get the velocity at the throat and this will equal 0 .708 times the square root of 1 .6 times 1 .242 times 10 to the fourth times 453.
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And this will be in, oopsie, feet per second.
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And this will equal to 164 feet per second.
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And i'm going to clean this one up a little, sort of squash it together.
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1 .66 times 1 .242 times 102 .10.
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N to the fourth times 453 feet squared.
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Okay.
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And then the density will be equal to 1 plus times m a squared to the 1k minus 1.
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And let's do this here.
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So pt will be equal to 3.
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This will equal p over rt.
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And that'll be times 1 over 1 plus k minus 1 over 2, ma squared 1 times k minus 1...