Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN: 9781259696527
Author: J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher: McGraw-Hill Education
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- 5arrow_forwardGiven information is attached. A. Neglect friction and calculate the velocity at point 2. (Velocity in m/s) B. If the pipe diameter at point 2 is 7.00 cm, what is the diameter at point 1? (Diameter in cm)arrow_forwardA pipeline conveys benzene from one point to the other. A gauge attached to line reads 150kPa. It is desired to check the gauge reading with benzene –over-mercury U-tube manometer.Determine the expected height difference of the mercury in the manometer; if on one endthe manometer is open to the atmosphere and on the other end where the gauge pressure isconnected there is a 3 cm height of benzene above the mercury meniscus. (benzene densityis 876 kg/m3 and mercury 13600 kg/m3)arrow_forward
- 10.33 ft³/min of a liquid with density (SG=1.84) is pumped 45 feet uphill. At the inlet, the pipe inner diameter is 3 in and the liquid pressure is 18 psia. At the outlet, the pipe inner diameter is 2 in and the liquid pressure is 40 psia. The friction loss in the pipe is 11.0 ft lbf/lbm- Determine the work required (hp) to pump the liquid. (Hint: gc will be helpful in this problem.)arrow_forwardالعنوان > TIONTICWUTK A liquid with sp. gr. = 1.12 flows through a pipe with velocity 1 m/s. The diameter of the pipe is 4 in. Calculate: (i) The mass flowrate (kg/s), and (Ibm/min) (ii) The volumetric flowrate (m³/s), and (ft³/min) Ans.: (1) 9.08 Kg 1198.5 lb/min (it) 0.0081 m³/s. 17.15ft³/min Solve Ans: ۱/۱ で CICarrow_forward
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