* Your assessment is very important for improving the workof artificial intelligence, which forms the content of this project
Download ChE 345 Chemical Engineering Fluid Mechanics
Survey
Document related concepts
Transcript
BERNOULLI EQUATION Bernoulli’s presenter: Fan Chao Way Nur Suhaili Mohd Yatim Nurirdayu Jantan Nurul Maisyarah Samsudin POTENTIAL ENERGY • Due to its elevation, the potential energy of the element relative to some reference level • PE = wz w= weight of element z= elevation KINETIC ENERGY • Due to its velocity, the kinetic energy of the element is: • KE=wv2/2g FLOW ENERGY • Pressure energy or flow work • Represent the amount of work to move the element of fluid across the certain certain section against pressure. • FE = wp/γ • The force on the element is pA, where p is the pressure at the section and A is the area of the section. • In moving the element across the section, the forces moves, the force moves a distance L equal to the length of element. • Work = pAL =pv • Where the v is the volume of the element. • The weight of the element w is • W = γV • • • • Where γ is the specific weight of the fluid. The volume of the element is V = w/ γ So work =pv = pw/ γ 6.7 INTERPRETATION OF BERNOULLI’S EQUATION Each term in Bernoulli's equation is one form of the energy possessed by the fluid per unit weight of fluid flowing in the system. Unit in each term Energy per unit weight In SI system : N.m N In customary system : Ib.ft Ib In fluid flow analysis, the term are typically expressed as “head” referring to a height above a reference level. Specifically, p/γ= pressure head z = elevation head V2/2g= velocity head Total head = p/γ(pressure head) +z (elevation head) + V2/2g(velocity head) Point 1-2 : magnitude may change in value • No energy lost/added, total head remains constant level. • Continuity equation: A1v1 = A2 v2 v2 = v1(A1/A2) • v2< v1 • A1<A2, v2< v1, so v22/2g<v12/2g • Pressure head ↑ because velocity head ↓ 6.8 RESTRICTION ON BERNOULLI’S EQUATION 1.Valid only for incompressible fluids because the specific weight of the fluid is assumed to be the same at the 2 sections of interest. 2.No mechanical devices between the 2 sections of interest that would add energy to or remove energy from the system, because the equation states that the total energy in the fluid is constant. 3.No heat transferred into or out of the fluids. 4.No energy lost due to friction.