Problem 10-1: A mercury-filled (S = 13.57) manometer is used in a 5.1 cm water line to measure the pressure drop across a flow meter. If the manometer deflection is 10.16 cm Hg, determine the pressure drop in N m2

12. Examine Figure 1. Given that a=7.5 in. and b=12 in., what is the height of the water in the ight hand vessel? Density ofthe CCI4 is 1.6 g/cm³. Manometer oil,p = 0.7g/cm3 Open to atmosphere Vapor 6.6 psig Liquid 10 in. Figure CS CamScanner ile tarandı

Problem 1: Determine the pressure at A if the gauge pressure at B is 87 kPa. The specific weights (weight per unit volume) of each fluid are Ywater = 9790 N/m³, Ymercury = 133100 N/m³, Yoil = 8720 N/m³. Water flow A 4 cm SAE 30 oil Mercury I 5 cm B- 6 cm 11 cm

QUESTION 1 of From pump 1.0 m a. Using a vertical bar chart, plot the pressure drop (i.e. P₁-P₂) for these eight nominal pipe sizes: 3/4", 1", 1- 1/4", 1-1/2", 2", 2-1/2", 3", 4", 6", and 8" 1.5 m Given the following conditions: Carbon tetrachloride at 20 °C is flowing through the piping system at a volumetric flow rate of 0.2 m³/min Total length of piping = 50 m Piping to be used is schedule 40 carbon steel pipe with an absolute roughness = 0.05 mm All 45° and 90° elbows have 'threaded regular' geometry Use the nominal pipe dimensions (3/4", 1", etc) for the x-axis labels but be sure to use the actual internal pipe diameters (given in document titled 'Table D1 in Janna textbook') in your calculations. HINT: Using a logarithmic scale on the y-axis scale will allow you to better compare the entire range of values. b. Re-do plot from part a, but now include the total cost (in USD) of the piping (you can ignore the costs associated with the fittings) on a secondary y-axis. For the piping…