In figure below, p₁ = 70 kPa, p₂ = 5 kPa, and the orifice has the following properties: Diameter, Dₒ = 6.0 cm, C꜀ = 1.00, Cᵥ = 0.95, and the head of the liquid (s = 2.50), h = 1.80 m. Find (a) the actual orifice discharge. (b) the new value of p₁ in kPa (p₂ is kept unchanged) to double the discharge in (1-a). (c) the theoretical velocity in m/s using the new value of discharge in (1-b).
In figure below, p₁ = 70 kPa, p₂ = 5 kPa, and the orifice has the following properties: Diameter, Dₒ = 6.0 cm, C꜀ = 1.00, Cᵥ = 0.95, and the head of the liquid (s = 2.50), h = 1.80 m. Find (a) the actual orifice discharge. (b) the new value of p₁ in kPa (p₂ is kept unchanged) to double the discharge in (1-a). (c) the theoretical velocity in m/s using the new value of discharge in (1-b).
Solid Waste Engineering
3rd Edition
ISBN:9781305635203
Author:Worrell, William A.
Publisher:Worrell, William A.
Chapter4: Mechanical Processes
Section: Chapter Questions
Problem 4.22P: Why is it so difficult to process MSW?
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In figure below, p₁ = 70 kPa, p₂ = 5 kPa, and the orifice has the following properties: Diameter, Dₒ = 6.0 cm, C꜀ = 1.00, Cᵥ = 0.95, and the head of the liquid (s = 2.50), h = 1.80 m. Find (a) the actual orifice discharge. (b) the new value of p₁ in kPa (p₂ is kept unchanged) to double the discharge in (1-a). (c) the theoretical velocity in m/s using the new value of discharge in (1-b).
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