Week 4 lecture 5 Flashcards

1
Q

Equation for kinetic energy

A

0.5 m v^2

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2
Q

Equation for potential energy

A

mgz

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3
Q

Energy stored in the system, manifestations of it are temperature and phase.

A

Internal energy

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4
Q

Equation for the change in energy of the system

A

(U + mgz + 0.5mv^2) - (U +mgz +0.5mv^2)

Assumption: we are dealing with a closed system of mass m

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5
Q

Equations for delta U

A

1) U2 - U1
2) Q-W

U = Q-W is the first law of thermodynamics for closed systems

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6
Q

Equation for enthalpy

A

H = U +PV

Used for open systems

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7
Q

Equation for the energy exchange with the surroundings with mass flow

A

0 = Q - W + ΣUi + migzi + 0.5mivi^2- ΣUj + mjgzj +0.5mjvj^2

ΣUi + migzi + 0.5mivi^2 = sum for all inflows
ΣUj + mjgzj +0.5mjvj^2 = sum for all outflows

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8
Q

Two elements of work

A
  1. Shaft work
  2. Flow work
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9
Q

Equation for work using the two elements of work

A

Work = Shaft work + Flow work

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10
Q

Equation for enthalpy change

Neglecting potential and kinetic energy

A

Q - Ws = deltaH

Ws = shaft work

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11
Q

Equation for flow work

A

Wf = ΣPjVj - ΣPiVi

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12
Q

All the other work exchanged between the process and surroundings excluding flow work

A

Shaft work

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13
Q

The work which will be needed in order to maintain a continuous flow through a control volume

A

Flow work

https://www.hkdivedi.com/2016/07/flow-work-or-flow-energy-in.html

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14
Q

In a nozzle or diffuser, the only work is _____

A

flow work

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15
Q

What shaft work in a nozzle/diffuser is equal to

A

Ws = O

The change is potential energy is also negligible

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16
Q

Energy balance over nozzle/diffuser

A

0 = Q + m[(h1-h2) + 0.5(V1^2 - V2^2)]

Normally for nozzles and diffusers the heat transfer rate is also relative to the enthalpy and kinetic energy thus the energy balance becomes:
0 = (h1-h2) + 0.5(v1^2 - v2^2)

17
Q

Mass flowing through state, steady flow devices is:

A

Constant

18
Q

The steady state, steady flow first law of turbines

A

0 = Q - Ws + m(h1-h2)

kinetic and potential energy changes have been neglected
When heat transfer between the turbine and surroundings is often small enough relative to the power and thalpy terms that is can also be neglected
Ws = m(h1-h2)

19
Q

Devices in which work is done on the substance, typically to increase the pressure and/or elevation

A

Compressors and pumps

20
Q

Steady rate, steady flow first law equation for compressors and pumps

A

0 = Q - Ws + m(h1-h2)

Ignoring heat transfer to the surroundings
Ws = m(h1-h2)

21
Q

Well insulated devices that allow energy exchange between hot and cold fluids without mixing the fluids

A

Heat exchangers

22
Q

The only work in a heat exchanger

A

Flow work

23
Q

What shaft work in a heat exchanger equals

A

Ws = 0

24
Q

Steady rate, steady flow first law equation for heat exchangers

A

0 = Q + Σmihi - Σmjhj

25
Q

Used to create a significant reduction in pressure by introducing a restriction into a line through which a gas or liquid flows

A

Throttling devices

26
Q

Steady rate, steady flow first law equation for throttling devices

A

0= (h1-h2)+1/2(v1^2-v2^2)

Assumptions:
- process is adiabatic
- potential energy is neglected
Neglecting kinetic energy: h1=h2