
Spherical particles of density 2000 kg m3 and diameters between 20 to 100 um are fed...
2. Comparing sedimentation and flotation um spherical floc particles with a density of 1.15 g/cm3 pm spherical floc particles with a density of 1.15 g/cm Calculate the settling velocity of 12 in summer (T-20°C) and in winter (T 4°C). Calculate the rise velocity of the same floc particle after the attachment of a single air bubble of 40 um diameter for the same two temperatures. The density of air is 1.27 kg/m3 at 4°C and 1.19 kg/m3 at 20°C Comment...
A horizontal pipe carries a smoothly flowing liquid of density of 1230 kg/m3. At Locations 1 and 2 along the pipe, the diameters are d1=6.15 cm and d2=2.13 cm, respectively. The flow speed at Location 1 is 2.97 m/s. What is the pressure difference ΔP (Pa) between Location 2 and Location 1 (including its sign)? Ignore viscosity.
A horizontal pipe carries a smoothly flowing liquid with density 1.23x10^3 kg/m3. At locations 1 and 2 along the pipe the diameters are 5.89 cm and 3.85 cm, respectively. Is the flow speed at location 2 higher or lower than at location 1? Part2 The flow speed at location 1 is 2.79 m/s. What is the pressure difference between location 2 and location 1 (including its sign)? Ignore viscosity. Answer in Pa
FIGURE 1 shows a branching pipe system through which is flowing water of density 1000 kg m-3 and viscosity 1.0 x 103 Pa s. 2. AVI Diameter at A 600 mnm Diameter at B500 mm Diameter at C 300 mm FIG. 1 If the volumetric flowrate at point A is 586 m3 h1 and the flow velocity at point C is 0.61 m s-1 determine: the mass flowrate at pointB a. b. the Reynolds number of the flow at point...
A horizontal pipe carries a smoothly flowing liquid of density of 1310 kg/m3. At Locations 1 and 2 along the pipe, the diameters are d5.19 cm and 2 3.75 cm, respectively. Is the flow speed at Location 2 higher or lower than the flow speed at Location 1? O higher di Location 2 d2 Location 1 cannot tell from the data O lower The flow speed at Location 1 is 2.33 m/s. What is the pressure difference Δ between Location...
Air at 100 kPa and density of 1.2 kg/m3 flows upward through a 5-cm diameter inclined duct at a rate of 50 L/s. The duct diameter is then reduced to 4 cm through a reducer. The pressure change across the reducer is measured by a water manometer. The elevation difference between the two points on the pipe where the two arms of the manometer are attached is 0.1 m. Determine the differential height between the fluid levels of the two...
Water (density = 1000 kg/m3, viscosity = 1.15 x 10-3 N-s/m2) is delivered from a large reservoir upstream (Section"1") through two mortar lined steel circular pipes arranged in series to another large reservoir downstream (Section "2") as shown in Figure E4.7 The upstream pipe is 80 m long and 0.15 m in diameter, whereas the downstream pipe is 50 m long and 0.1 m in diameter. Both pipes have sharp-edged entrance and exit. Consider both major and minor losses. Determine...
Consider an oil of density p 800 kg/m3, viscosity u 0.01 Pa.s (10 times the viscosity of water), heat capacity of Cp 2 k]/(kg K) and thermal conductivity of Koll -0.15 W/(mk). This oil flows at mass flowrate of 30 kg/minute through a copper pipe of d- 2 cm inner diameter, with wall thickness of t-1 mm. At the relevant conditions, copper has thermal conductivity of ke 400 W/(m.K). The copper pipe loses heat to the surroundings of Tsurr 20°C...
Water (density 998 kg/mº, dynamic viscosity 0.001 Pa s) is pumped between two reservoirs at a volumetric flow rate of 0.006 m/s through a 120-m long pipe of 5 cm diameter. The roughness ratio of the pipe is a/d = 0.001. There are some fittings and valves in the pipe system, as shown in Figure Q1. The loss coefficients of the valves and fittings can be found in Table Q1. The Darcy friction factor can be found in the Moody...
FMA360 1 AY 2018 ASSIGNMENT 1 0.003 m3/s of water at 20°C is required to be transported between two locations 400 m apart. Assuming there is no fittings, find the appropriate drawn tubing to be used if the head loss must not exceed 25m There are 3 different diameters for you to choose from, 3.0 cm, 4.0 cm, 5.0 cm. Use the attached Moody diagram for your calculations Temperature Pressure Density Dynamic viscosity Kinematic viscosity Pa kg/m kg/ms 101325 999.19...