A centrifugal ar compressor has a rotor inrer diameter of \(D_{1}=2.0\) in.., a rotor oater diameter of \(D_{2}=6.5\) in, a rotor depth of 10 in. and a rotor rotational speed of 3600 rpm. The fluid relative velocities \((W)\) are purely radial. The compressor delivers an air mass flow rate of \(1.0 \mathrm{lom} / \mathrm{s}\) with \(T_{1}=70^{\circ} \mathrm{F}, p_{1}=4.7 \mathrm{psia}, T_{2}=\) \(240^{\circ} \mathrm{F},\) and \(p_{2}=33.1\) psia. Find the power transferied by the rotor to the air and the inlet relative velocity \(W\)

Short Answer

Expert verified
The first step is to calculate the mass flow in frequently used units (lbm/sec). Following this, the energy equation needs to be applied involving the velocities and the work done on the fluid by the rotor. After computing the required values, we are able to calculate Power.

Step by step solution

01

Calculate the mass flow rate

Given that the air mass flow rate is 1.0 lbf/s (where lbf represents pound-force), it must be converted to lbm/sec (where lbm represents pound-mass). Using the conversion factor, \(1 \, \text{lbf} = 32.174 \, \text{lbm} \, \text{ft/sec}^2\), the mass flow rate becomes \(1.0 \, \text{lbf/s} \times \frac{1}{32.174 \, \text{lbm} \, \text{ft/sec}^2} = 0.0311 \, \text{lbm/sec}\).
02

Apply the energy equation

Knowing the mass flow rate, the energy equation can be applied next. The energy equation here is \( \text{Power} = \dot{m}(h_2 - h_1 + \frac{W_1^2}{2}-\frac{W_2^2}{2})\), where, \( \dot{m}\) is the mass flow rate. The enthalpy (h) at states 1 and 2 could be looked up in the property tables for air. To calculate W, we consider W to be purely radial and hence, \(W = u =R \cdot \omega\) (with ω the angular velocity and R the radius). The radius \(R= \frac{D}{2}\) can be considered as halfway between the inner and outer diameters of the rotor. Hence \( R = \frac{D_1 + D_2}{4} = \frac{2+6.5}{4} = 2.125\) in. Convert \( R\) to feet, this gives \( R = 2.125/12 = 0.177\) ft. The rotational speed \( \omega\) in rad/sec is then \( \omega = \frac{2\pi \times 3600}{60} = 377\) rad/sec. Hence, \(W = u = 377 \times 0.177 = 66.7\) ft/sec. With the \(W_1\) and \( W_2\) (considered to be equal) and \( h_1\) and \( h_2\) known, the Power can be calculated with the energy equation.
03

Find the power transferred

After substituting the values in the energy equation, calculate the power transferred. However, to calculate the power, the change in enthalpy is needed. In order to compute the enthalpy change, the air specifics should be considered (specific heat capacity and the temperature difference). Once enthalpy, \( \Delta h = c_p (T_2 - T_1)\), is calculated, substitute everything into the equation for Power.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A model fan with wheel diameter 32 in. is tested at a speed of \(1750 \mathrm{rpm}\). The test fluid is air with density \(0.075 \mathrm{lbm} / \mathrm{ft}\). At its \(\mathrm{BEP}\), the fan produces \(8000 \mathrm{ft}^{3} / \mathrm{min}\) at total pressure rise of 8 in. \(\mathrm{H}_{2} \mathrm{O}\). A geometrically similar fan is to handle \(200,000 \mathrm{ft}^{3} / \mathrm{min}\) of flue gas with density \(0.050 \mathrm{lbm} / \mathrm{ft}^{3}\) and 30 in. \(\mathrm{H}_{2} \mathrm{O}\) total pressure rise. Determine the required size and speed of the flue gas fan. Note any assumptions and/or limitations.

A certain axial-flow pump has a specific speed of \(N_{x}=5.0\) If the pump is expected to deliver 3000 gpm when operating against a 15 -ft head, at what speed (rpm) should the pump be run? Draw a sketch of the p.ump impeller (front and side views).

Water to run a Pelton wheel is supplied by a penstcck of length \(\ell\) and diameter \(D\) with a friction factor \(f\). If the only losses associated with the flow in the penstock are due to pipe friction. show that the maximum power output of the turbine occurs when the nozzle diameter, \(D_{1},\) is given by \(D_{1}=D /(2 f \ell / D)^{1 / 4}\)

A prototype fan has a \(20-f\) diameter, an inlet pressure of 14.40 psia, an inlet temperature of \(70^{\circ} \mathrm{F},\) and a speed of 90 rpm. \(\mathrm{A}\) \(\frac{1}{10}-\operatorname{scal} \mathrm{e}\) model of the fan has the same inlet pressure and emperature. an inlet power of \(1.24 \mathrm{hp}\), a flow rate of \(220 \mathrm{ft}^{3} / \mathrm{min}\), and a speed of \(1800 \mathrm{rpm} .\) Find the corresponding input power and flow rate of the prototype fan. Neglect Reynolds number effects.

Water at \(40^{\circ} \mathrm{C}\) is pumped from an open tank through \(200 \mathrm{m}\) of \(5 \mathrm{C}\) -mm-diameter smooth horizontal pipe as shown in Fig. \(P 12.17\) and discharges into the atmosphere with a velocity of \(3 \mathrm{m} / \mathrm{s}\). Minor losses are neglaible. (a) If the efficiency of the pump is \(70 \%\), how much power is being supplied to the pump? (b) What is the NPSH at the pump inlet? Neglect losses in the short section of pipe connecting the pump to the tank. Assume standard atmospheric pressure.

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free