Lecture 5 Flashcards

1
Q

SFEE

A

steady flow energy equation

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2
Q

enthalpy

A

internal energy + work done

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3
Q

why are we able to simplify the SFEE to

Q - W = m (h2 -h1) (all with respect to time

A

as enthalpy is often by 1000 times the largest terms so can ignore kinectic and potential terms especially for gases

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4
Q

simplify the SFEE to bernoullis equation

A

internal energy does not change and heat is not added
use density rather than specific volume (v = 1/density)
treat density as constant
no work input

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5
Q

for closed systemm

A

Q -W =m(u2 -u1)

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6
Q

for steady flow thermal systems

A

SFEE with enthalpy terms

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7
Q

for steady flow fluid systems with work

A

SFEE densities and internal energy removed

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8
Q

steady flow fluid systems

A

bernoullis equation

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9
Q

what does a turbine do

A

extracts KE from flow and turns it into motion

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10
Q

draw a diagram of a turbine

A

take in high temperature and pressure fluid

out goes low temperature and pressure fluid

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11
Q

compressor takes

A

low temperature low pressure fluid and compresses it doing work on the fluid

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12
Q

in a powerstation what is the name of compresses that pressurise the water

A

feed pumps

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13
Q

work is needed to drive a compressor or tubine

A

work is needed to drive a compressor work is extracted from a turbine

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14
Q

SFEE simplification for turbines and compressors

A

adiabatic Q = 0

gases and steam kinetic and potential energy terms are negligible

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15
Q

SFEE eqation for turbine and compressor

A

-W = mass flow rate (h2 - h1)

or workrate = mass flow rate (h1-h2)

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16
Q

SFEE wind and water turbines

A

kinetic energy term and enthalpy term

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17
Q

Maximum work out

A

always from reversible process

18
Q

isentropic is

A

maximum work possible but never achieved in areal system

19
Q

for ideal gas undergoing isentropic adiabatic process

A

n = gamma = cp/cv
ideal work is
mass flow rate * cp * (T1-T2x)
cp as open system

20
Q

for steam undergoing isentropic adiabatic process

A

entropy at the start = entropy at the end
entropy at start know for p and t
can calculate final as entropy will be the same

21
Q

draw diagram of turbine isentropic and real case including equations

A
W = m (h1 - h2s)
W = eff *m(h1-h2s)
22
Q

for an ideal gas going through turbine how do calculate the change in temperature

A

T1 - T2 = eff * (T1-T2s)

W = mass flow rate cp(T1 -T2s)

23
Q

in a turbine in comparison to the isentropic temperature what should the final temperature be

A

exit temperature is higher

24
Q

For steam turbine efficiency

A

W = m (h1-h2)
h2 = h1 - eff * (h1 -h2s)
find T2 by finding temp with that enthalpy

25
should W be positive for a turbine
yes as turbine extracts work | it is work done by the system
26
should W be positive or negative for a compressor
negative as compressor doing work on the system
27
for a compressor you have to put more
work in than the isentropic amount
28
feedpump is a
compresses liquid water in a powerstation | water incompressible therefore volume cannot change
29
for an isentropic feed pump
ds = 0 and q = 0 so dh =v dp at constant volume dh = v(p2 - p1) = -w
30
graph diagram of a feedpump
see powerpoint
31
nozzle takes
a low velocity flow at high pressure and temperature and it undergoes an expansion increasing KE
32
nozzle takes
a low velocity flow at high pressure and temperature and it undergoes an expansion increasing KE enthalpy of fluid decreases
33
nozzle
undergoes an expansion
34
diffuser
expansion
35
diffuser takes
high velocity flow and slows it down increases the enthalpy of the fluid pressure will increases
36
nozzle and diffuser simplification of SFEE
everything including work term goes apart from speed and enthalpy
37
isentropic nozzle drawing
see powerpoint
38
if nozzle is not 100% efficient what would happen to exit flow
it would be slower but hotter
39
often assume which end of nozzle and diffuser
that velocity is zero wide end of diffuser or nozzle
40
real devices difference
heat transfer through devices | irreversible pressure loss in fluid flow (mostly due to turbulent losses)