Download Unit Operation and Process Heat Transfer

Survey
yes no Was this document useful for you?
   Thank you for your participation!

* Your assessment is very important for improving the workof artificial intelligence, which forms the content of this project

Document related concepts
no text concepts found
Transcript
Unit Operation and Process
Heat Transfer
Widelia Ika Putri, S.T.P., M.Sc.
LOGO
[email protected]
Pasteurization of milk, juice, etc.
Refrigeration of fruits and
vegetables.
Meat freezing.
Thermal sterilization in canned
food.
Evaporation
Distillation
Drying
March 2012
[email protected]
Heat transfer
 A dynamic process in which heat is
transferred spontaneously from one body
to another a lower temperature body.
 The rate of heat transfer depends upon
the differences between the bodies, the
greater the difference in temperature, the
greater the rate of heat transfer.
 Temperature difference between the
source of heat and the receiver of heat is
therefore the driving force in heat
transfer.
 An increase in the temperature difference
increases the driving force and therefore
increases the rate of heat transfer.
March 2012
[email protected]
Heat transfer
Conduction
Convection
Radiation
March 2012
[email protected]
Rate of transfer = driving force /
resistance
Rate of heat transfer = temperature
difference / heat flow resistance of
medium.
March 2012
[email protected]
Ohm’s Law
The rate of transport (the quantity
transported per unit time) is
proportional to the driving force and
inversely proportional to the
resistance of the medium to the
transport.
March 2012
[email protected]
q = dQ/dt = the rate of heat transfer
F = driving force
R = resistance of the medium to heat
transfer
k = conductance of the medium to
heat transfer
 Heat flux (J) = the rate of transport
proportional to the area A available to
the transport (the rate of transport
per unit area) => q/A
March 2012
[email protected]
Steady State Conductive Heat Transfer
Steady state => all the properties
that define the ‘state’ of the system
(temperature, pressure, chemical
composition, etc.) remain constant
with time.
Fourier’s 1st Law
March 2012
[email protected]
Q = heat transferred (J)
T = temperature (K)
t = time (s)
k = thermal conductivity of the
medium (J/s.m.K)(W/m.K)
z = distance in the direction of the
transport (m)
March 2012
[email protected]
Thermal conductivity
• A property of the material (the
material’s ability to transfer heat).
Thermal diffusivity
• The ratio of thermal conductivity to the
“volumetric heat capacity” of material
(the ratio of the material’s ability to
transfer heat to its capacity to store
heat).
March 2012
[email protected]
Soal
1. Hitung kecepatan transfer panas dari
bahan 3x4 m, tebal 0,2m, di satu sisi
0oC dan di sisi lainnya 35oC. Jika
bahan tersebut adalah: a. alumunium;
b. kuningan; c. besi; d. tembaga; e.
karet
March 2012
[email protected]
Sweat (1986)
k = 0.25Xc + 0.155Xp + 0.16Xf +
0.135Xa + 0.58Xw
X = mass fraction
c = carbohydrate
p = protein
f = fat
a = ash
w = water
March 2012
[email protected]
Soal
1. Hitung thermal conductivity dari
bahan berikut ini:
food
Water
(%)
Protein
(%)
Fat
(%)
Carbohydrate
(%)
Apel
84.1
0.3
0.4
14.9
Brokoli
89.9
3.3
0.2
5.5
Tepung
gandum
12.0
9.2
1.0
73.8
Susu sapi
87.0
3.5
3.9
4.9
Ayam
panggang
66.0
20.2
12.6
0
Ikan cod
82.6
16.5
0.4
0
Almond
4.7
18.6
54.1
19.6
March 2012
[email protected]
Steady State Conduction through a
Single Slab
March 2012
[email protected]
Steady State Conduction through a
Multilayer Slab
March 2012
[email protected]
Soal
1. Dinding dari ruang penyimpan
tersusun dari 3 lapisan, dari yang
terdalam:
• Stainless steel, tebal 2mm
• Thermal insulation, tebal 80mm (k =
0.03 J/s.m.C)
• Beton, tebal 150mm
Bila sisi terdalam adalah -18oC dan
sisi terluar 20oC, hitung flux panas
yang melalui dinding?
March 2012
[email protected]
Steady State Conduction through a
Cylinder Slab
March 2012
www.themegallery.com
Soal
1. Pipa baja berdiameter 5cm
membawa uap air pada 150oC. Pipa
disekat dengan lapisan penyekat
silinder ketebalan 3cm
(k=0.03W/mK). Hitung kecepatan
panas hilang per meter panjang pipa,
jika suhu lapisan terluar adalah 35oC?
Company Logo
[email protected]
Steady State Convective Heat Transfer
Convection
Natural
Convection
Forced
Convection
The movement
is caused by
heat transfer
itself.
The movement
is caused by
factor
independent of
the transfer.
March 2012
[email protected]
A stationary layer (film) of fluid which
in contact with the solid’s surface ->
thickness δ
Temperature in the bulk -> T2;
temperature in the boundary layer ->
T1
A coefficient convective of heat
transfer ->
March 2012
[email protected]
h -> depends on the properties of the
fluid (specific heat, viscosity, density,
and thermal conductivity), the
turbulence (average velocity), and
the geometry of the system -> these
parameters are dimensionless group
used in heat transfer.
March 2012
[email protected]
vertical
sphere
Natural
convection
March 2012
[email protected]
Soal
1. Papan gabus tebal 10 cm pada satu
sisi bersuhu -12oC dan sisi lain 21oC.
Berapa kecepatan transfer panas
melalui 1m2 dinding?
2. Sebuah cold storage memiliki
dinding yang tersusun dari: 11 cm
batu bata pd bag. terluar, kmdn 7,5
cm beton, dan 10 cm gabus. Suhu
rata2 di bag. dalam -18oC dan di
bagian luar dinding 18oC. Hitung
kecepatan transfer panas melalui
1m2 dinding?
March 2012
[email protected]
Soal
1. Hitung kecepatan panas yang hilang
dari dinding vertical suatu oven
dengan konveksi alami. Suhu dinding
50oC dan di udara ambient 20oC.
Tinggi dinding 1.2m dan lebar 3m?
March 2012
[email protected]
turbulent
viscous
Forced
convection
sphere
March 2012
[email protected]
Soal
1. Jus jeruk, didinginkan, mengalir
dengan kecepatan 4m3/jam melalui
pipa berdiameter 0.05m. Sifat dari jus
jeruk pada suhu pengolahan adalah:
ρ= 1060kg/m3; µ= 3.10-3Pa.s; cp=
3900J/kg.K; k= 0.54 W/m.K. Hitung
koeffisien panas konveksi antara jus
jeruk yang mengalir di dalam pipa
dengan dinding pipa?
March 2012
[email protected]
2. Gandum pipilan dikeringkan dengan
udara panas dalam aliran turbulent di
fluidized bed dryer. Kecepatan udara
0.5m/s dengan suhu 93oC. Pipilan
gandum diasumsikan berbentuk bulat
dengan diameter 1mm. Hitung
koeffisien transfer panas konveksi?
March 2012
[email protected]
Radiation
Radiation covers a vast array of
phenomena that involve energy
transport in the form of waves, in the
wavelength range of 10-7 to 10-4 m.
Radiation => cooling the emitting
body and heating the receiving body.
> 0oK => all substances emit
electromagnetic radiation.
Heat transfer by radiation does not
require the presence of material
medium.
March 2012
[email protected]
Black body => a body that absorb the
incident radiation totally; the
absorbtivity of black body is unity and
its reflectivity and transmissivity are
both zero.
March 2012
[email protected]
Emmisivity (ε) => the ratio of
emissive power of a real body to that
of a black body at the same
temperature; always less than unity.
March 2012
[email protected]
Soal
1. Hitung net heat transfer dengan
radiasi dari sebongkah roti di oven
pada suhu 177oC, jika emissivitasnya
0,85 dgn total luas area 0.0645 m2
dan suhu 100oC?
March 2012
www.themegallery.com
Heat Exchanger
Device for the exchange of heat between
two fluids separated by partition.
The partition is a heat conducting solid
wall, usually made of metal.
Extensively used in the food industry for
heating (e.g. pasteurizer), cooling (chilled
water generator), and heat induced phase
change (freezing, evaporation).
Company Logo
www.themegallery.com
Flow Pattern
1
Parallel flow
2
Countercurrent flow
3
Cross flow
Company Logo
www.themegallery.com
Company Logo
www.themegallery.com
Jacketed Pan
Kumparan pemanas
Plate Heat Exchanger
Company Logo
LOGO