Title: Bernoullis Theorem for Fans
1Bernoullis Theorem for Fans
- PE Review Session VIB section 1
2Fan and Bin
3
2
1
3static pressure
velocity head
total pressure
4Power
5FtotalFpipeFexpansionFfloorFgrain
- Fpipef (L/D) (V2/2g) for values in pipe
- Fexpansion (V12 V22) / 2g
- V1 is velocity in pipe
- V2 is velocity in bin
- V1 gtgt V2 so equation reduces to
- V12/2g
6Ffloor
- Equation 2.38 p. 29 (4th edition) for no grain on
floor - Equation 2.39 p. 30 (4th edition) for grain on
floor - Ofpercent floor opening expressed as decimal
- epvoidage fraction of material expressed as
decimal (use 0.4 for grains if no better info)
7ASAE Standards graph for Ffloor
8Fgrain
- Equation 2.36 p. 29 (Cf 1.5)
- A and b from standards or Table 2.5 p. 30
- Or use Shedds curves (Standards)
- X axis is pressure drop/depth of grain
- Y axis is superficial velocity (m3/(m2s)
- Multiply pressure drop by 1.5 for correction
factor - Multiply by specific weight of air to get F in m
or f
9Shedds Curve (english)
10Shedds curves (metric)
11Example
- Air is to be forced through a grain drying bin
similar to that shown before. The air flows
through 5 m of 0.5 m diameter galvanized iron
conduit, exhausts into a plenum below the grain,
passes through a perforated metal floor (10
openings) and is finally forced through a 1 m
depth of wheat having a void fraction of 0.4.
The area of the bin floor is 20 m2. Find the
static and total pressure when Q4 m3/s
12FF(pipe)F(exp)F(floor)F(grain)
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19Fexp
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21Ffloor Equ. 2.39
22 23 24(No Transcript)
25Fgrain
26 27 28Using Shedds Curves
29- Ftotal 3.2 21.2 2.3 130
- 157 m
30Problem 2.4 (page 45)
- Air (21C) at the rate of 0.1 m3/(m2 s) is to be
moved vertically through a crib of shelled corn
1.6 m deep. The area of the floor is 12 m2 with
an opening percentage of 10 and the connecting
galvanized iron pipe is 0.3 m in diameter and 12
m long. What is the power requirement, assuming
the fan efficiency to be 70?
31Moisture and Psychrometrics
- Core Ag Eng Principles Session IIB
32Moisture in biological products can be expressed
on a wet basis or dry basis
- wet basis
- dry basis (page 273)
33Standard bushels
- ASAE Standards
- Corn weighs 56 lb/bu at 15 moisture wet-basis
- Soybeans weigh 60 lb/bu at 13.5 moisture
wet-basis
34Use this information to determine how much water
needs to be removed to dry grain
- We have 2000 bu of soybeans at 25 moisture (wb).
How much water must be removed to store the
beans at 13.5?
35- Remember grain is made up of dry matter H2O
- The amount of H2O changes, but the amount of dry
matter in bu is constant.
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38- So water removed
- H2O _at_ 25 - H2O _at_ 13.5
39Your turn
- How much water needs to be removed to dry shelled
corn from 23 (wb) to 15 (wb) if we have 1000 bu?
40Psychrometrics
- If you know two properties of an air/water vapor
mixture you know all values because two
properties establish a unique point on the psych
chart - Vertical lines are dry-bulb temperature
41Psychrometrics
- Horizontal lines are humidity ratio (right axis)
or dew point temp (left axis) - Slanted lines are wet-bulb temp and enthalpy
- Specific volume are the other slanted lines
42Your turn
- List the enthalpy, humidity ratio, specific
volume and dew point temperature for a dry bulb
temperature of 70F and a wet-bulb temp of 60F
43- Enthalpy 26 BTU/lbda
- Humidity ratio0.0088 lbH2O/lbda
- Specific volume 13.55 ft3/lbda
- Dew point temp 54 F
44Psychrometric Processes
- Sensible heating horizontally to the right
- Sensible cooling horizontally to the left
- Note that RH changes without changing the
humidity ratio
45Psychrometric Processes
- Evaporative cooling grain drying (p 266)
46Example
- A grain dryer requires 300 m3/min of 46C air.
The atmospheric air is at 24C and 68 RH. How
much power must be supplied to heat the air?
47Solution
- _at_ 24C, 68 RH Enthalpy 56 kJ/kgda
- _at_ 46C Enthalpy 78 kJ/kgda
- V 0.922 m3/kgda
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49Equilibrium Moisture Curves
- When a biological product is in a moist
environment it will exchange water with the
atmosphere in a predictable way depending on
the temperature/RH of the moist air surrounding
the biological product. - This information is contained in the EMC for each
product
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51Equilibrium Moisture Curves
- Establish second point on the evaporative cooling
line i.e. cant remove enough water from the
product to saturate the air under all conditions
sometimes the exhaust air is at a lower RH
because the product wont release any more water
52Establishing Exhaust Air RH
- Select EMC for product of interest
- On Y axis draw horizontal line at the desired
final moisture content (wb) of product - Find the four T/RH points from EMCs
53Establishing Exhaust Air RH
- Draw these points on your psych chart
- Sketch in a RH curve
- Where this RH curve intersects your drying
process line represents the state of the exhaust
air
54Sample EMC
55We are drying corn to 15 wb with natural
ventilation using outside air at 25C and 70 RH.
What will be the Tdb and RH of the exhaust air?
56Drying Calculations
57Example problem
- How long will it take to dry 2000 bu of soybeans
from 20 mc (wb) to 13 mc (wb) with a fan which
delivers 5140-9000 cfm at ½ H2O static pressure.
The bin is 26 in diameter and outside air (60
F, 30 RH) is being blown over the soybeans.
58Steps to work drying problem
- Determine how much water needs to be removed
(from moisture content before and after total
amount of product to be dried) - Determine how much water each pound of dry air
can remove (from psychr chart outside air is
it heated, etc., and EMC) - Calculate how many cubic feet of air is needed
- Determine fan operating CFM
- From CFM, determine time needed to dry product
59Step 1
- How much water must be removed?
- 2000 bu
- 20 to 13
- Now what?
60Step 1
- Std bu 60 lb _at_ 0.135
- mw 0.135(60 lb) 8.1 lb H2O
- md mt mw 60 8.1 51.9 lbdm
- _at_ 13
61Step 1
62Step 2
- How much water can each pound of dry air remove?
- How do we approach this step?
63Step 2
- Find exit conditions from EMC.
- Plot on psych chart.
0C 32F 64 10C 50F 67 30C 86F 72
64Step 2
_at_ 52F 68 RH
65Change in humidity ratio
66- Each pound of dry air can remove
67- We need to remove 10500 lbH2O.
- Each lbda removes 0.0023 lbH2O.
68Step 3
- Determine the cubic feet of air we need to remove
necessary water
69Step 3 Calculations
70Step 4
- Determine the fan operating speed
- How do we approach this?
71Step 4
Airflow (cfm/ft2) 50 30 15 10
Pressure drop (H2O/ft) 0.5 0.23 0.09 0.05
x depth x CF
72Step 4
Fgrain
½
PS
Q
6300 cfm
73- From cfm of fan and cubic feet of air, determine
the time needed to dry the soybeans.
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75Example 2
- Ambient air at 32C and 20 RH is heated to 118 C
in a fruit residue dryer. The flow of ambient
air into the propane heater is at 5.95 m3/sec.
The drying is to be carried out from 85 to 22
wb. The air leaves the drier at 40.5C. - Determine the airflow rate of the heated air.
76Example 2
- With heated air, is conserved (not Q)
77Example 2
- 2. Determine the relative humidity of the air
leaving the drier.
78Example 2
32 40.5 118
78 RH
79Example 2
- 3. Determine the amount of propane fuel required
per hour.
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81Example 2
82Example 2
- 4. Determine the amount of fruit residue dried
per hour.
83Example 2
- _at_ 85, 0.15 of every kg is dry matter
84Example 2
85Example 2
86Your Turn
- A grain bin 26 in diameter has a
- perforated floor over a plenum chamber. Shelled
field corn will be dried from an initial mc of
24 to 14 (wb). Batch drying (1800 std.
bu/batch) will be used - with outside air (55F, RH 70) that has been
heated 10F before being passed through the corn.
To dry the corn in 1 week -
87- 1. What is the necessary fan delivery rate (cfm)?
88- 2. What is the approximate total pressure drop
(in inches of water) required to obtain the
needed air flow?
89- 3. The estimated fan HP based on fan efficiency
of 65
90- 4. If the drying air is heated by electrical
resistance elements and the power costs is
0.065/KWH, calculate the cost of heating energy
per standard bushel.