Pressure drop model presentation april 19th
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Transcript of Pressure drop model presentation april 19th
Pressure Drop Model and Experimental Variability
Plate and Frame Filter Press
Erin DurkeeYen Nguyen
Dalton Russell
CHE 4002-401 Chemical Engineering Laboratory I: Project III
Oklahoma State UniversityCoach Clint Aichele
Coach Mike ResetaritsCoach Russ Rhinehart
Flow behaves like a transitional flow. Pressure drop model for the combined set of both laminar and
turbulent portions
Where:
a = 0.0484
b = 10.01
c = 0.0009
d = 5.47
p = 3.41
CONCLUSION
∆ 𝑃𝑐𝑜𝑚𝑏𝑖𝑛𝑒𝑑=(𝑎+𝑏𝑁 )∗𝑄+(𝑐+
𝑑𝑁 𝑝 )∗𝑄𝑝
Apparatus Overall Diagram
EXPERIMENTAL EQUIPMENT
Suspension Tank
Hand Wheel with Spindle
Overall System
Pumpoutlet Thermometer Pumpoutlet Pressure Gauge
EXPERIMENTAL EQUIPMENT
Bypass Stop Valve Pipe Diaphragm Valve Filterinlet Pressure Gauge
Filteroutlet Flow MeterFilter Plate Arrangement
EHS & LP Environmental – water is the only component used
Health – no health hazards
Safety – wear standard lab clothing and safety glasses – slipping hazard due to water
Loss Prevention – use minimal amount of resources necessary
THEORY Pressure drops through two different zones in the filter press:• the in-pipe zone :
• laminar• turbulent • transitional
• porous medium of the filter paper: • laminar • turbulent• transitional ∆ 𝑃=∆ 𝑃𝑝𝑖𝑝𝑒+∆ 𝑃𝑝𝑜𝑟𝑜𝑢𝑠
(A sketch to illustrate the two different zones.)
THEORY Darcy-Weisbach equation:
Where: • f: Darcy friction factor• L and D: length and inside diameter of the pipeline• ρ: density of water• Q: flow rate of water through the unit
THEORY: In-pipe zone:
Porous medium zone:
Where:• c, d are turbulent flow unknown constants• N: the number of filter papers used, or the number of
split flows during the filtering process
Theory : Laminar Flow Data from the Moody diagram (Munson):
Plug back into the Darcy-Weisbach equation:
Poiseuille’s law:
THEORY: In-pipe zone:
Porous medium zone:
Where: • a, b are laminar flow unknown constants
THEORY Laminar only:
Turbulent only:
Combined Flow:
∆ 𝑃 𝑙𝑎𝑚𝑖𝑛𝑎𝑟=(𝑎+ 𝑏𝑁 )∗𝑄
∆ 𝑃𝑐𝑜𝑚𝑏𝑖𝑛𝑒𝑑=(𝑎+𝑏𝑁 )∗𝑄+(𝑐+
𝑑𝑁 𝑝 )∗𝑄𝑝
∆ 𝑃 𝑡𝑢𝑟𝑏𝑢𝑙𝑒𝑛𝑡=(𝑐+𝑑𝑁2 )∗𝑄2
DATA PROCESSING Flow rate:
Where:• V1, V2 : initial and final readings of volume in gallons
• t1, t2 : initial and final readings of time in minutes
• 6.309*10-5 : unit conversion for the flow rate (Q) from gal/min to m3/s
𝑄=( 6.309∗10−5 )∗𝑉 2−𝑉 1
𝑡2−𝑡 1
DATA PROCESSING Data model:
Where:• : specific weight of water • (z3-z2) : change in elevation
• KL=7: minor loss coefficient for the water meter equipment
• Re ≤ 2100: ; Re ≥ 4000:
𝑃2=𝛾 (𝑧 3− 𝑧2+[ 𝑓 𝐿𝐷 +𝐾 𝐿 ] 8𝑄2
𝑔𝜋 2𝐷4 )Sketch to illustrate the points (2) and (3)
EXPERIMENTAL PLANDAY 1 – PRELIMINARY TRIALS
N plates
6 psig
Record Flow Rate in 1 min
Calculate P2
Repeat with new filter papers
*N = 8, 12, and 16
Number of Plates:
Inlet Pressure (P1): 9 psig 12 psig
EXPERIMENTAL PLANDAY 2 – VARIABILITY AND MODEL TESTING
14 plates
Proper Orientation
Record Flow Rate in 1 min
Calculate P2
Number of Plates:
Inlet Pressure Range (P1): 3 – 12 psig
Random Orientation
EXPECTATION The value of the outlet pressure P2 should be less than 0 psig.
• a, b, c, d, and p are not negative • Laminar flow coefficients: if a ≠ 0, then c = 0 • Turbulent flow coefficients: if b ≠ 0, then d = 0
The graph of pressure drop ∆P vs. flow rate Q should be:• increasing linear line if laminar flow only• positive increasing quadratic curve if turbulent only
POLYMATH - NONLINEAR REGRESSION
POLYMATH REPORT
Laminar Turbulent Combined
RESULTS The combined
flow model best described the data:
Where:
a = 0.0484 c =
0.0009
b = 10.01d
= 5.47
p = 3.41 ∆ 𝑃𝑐𝑜𝑚𝑏𝑖𝑛𝑒𝑑=(𝑎+
𝑏𝑁 )∗𝑄+(𝑐+
𝑑𝑁 𝑝 )∗𝑄𝑝
3.8 4 4.2 4.4 4.6 4.8 5 5.2 5.4 5.6 5.8 6 6.2 6.4 6.64.505.005.506.006.507.007.508.008.509.009.50
10.0010.5011.0011.5012.0012.5013.00
Pressure drop vs. Flow rate when N=8
Data Model
Laminar Model
Turbulent Model
Combined Model
Flow Rate Q (gal/min)
P1-P2 (psig)
VARIABILITY OF MEDIUM
Proper Orientation Random Orientation
4.5 5 5.5 6 6.5 7 7.5 8 8.5 93.003.504.004.505.005.506.006.507.007.508.008.509.009.50
10.0010.5011.00
Pressure drop vs. Flow rate when N=14
Process Model
Data Model
Flow rate Q (gal/min)
P1-P
2 (p
sig)
4.2 4.7 5.2 5.7 6.2 6.7 7.2 7.7 8.2 8.73.003.504.004.505.005.506.006.507.007.508.008.509.009.50
10.0010.5011.00
Pressure drop vs. Flow rate when N=14
Data Model
Process Model
Flow rate Q (gal/min)
P1-P
2 (p
sig)
STATISTICAL TEST
Preliminary Trials
Two-tailed t-test: Passed
R-lag-1 test: Did not pass
large negative
Proper Orientation
Two-tailed t-test: Passed
R-lag-1 test: Did not pass
large positive
Random Orientation
Two-tailed t-test: Did not pass
R-lag-1 test: Did not pass
large positive
RESIDUAL PLOTS
Preliminary Trials Proper Orientation
1 2 3 4 5 6 7 8 9 10
-0.50
-0.30
-0.10
0.10
0.30
0.50
0.70
0.90
Plot of Residuals when N=14
Trials
Res
idua
ls
PROPAGATION OF UNCERTAINTY Data model:
ε(p1) (psig) ε(z3) (m) ε(z2) (m) ε(L) (m) ε(D) (m) ε(V2) (m3) ε(V1) (m3) ε(t2) (min) ε(t1) (min)
4.00 0.0010 0.0010 0.0010 0.0010 0.0004 0.0004 0.0083 0.0083
1 -1.42E+00 1.42E+00 -5.63E-02 7.65E+01 -1.79E+05 1.79E+05 2.72E+03 -2.72E+03
1 -1.42E+00 1.42E+00 -5.88E-02 8.03E+01 -1.84E+05 1.84E+05 2.85E+03 -2.85E+03
1 -1.42E+00 1.42E+00 -6.13E-02 8.41E+01 -1.88E+05 1.88E+05 2.99E+03 -2.99E+03
1 -1.42E+00 1.42E+00 -8.61E-02 1.23E+02 -2.26E+05 2.26E+05 4.36E+03 -4.36E+03
1 -1.42E+00 1.42E+00 -9.21E-02 1.32E+02 -2.34E+05 2.34E+05 4.70E+03 -4.70E+03
εΔP, 0.95
81.02
83.14
85.27
105.09
109.65
PROPAGATION OF UNCERTAINTY
Result • Average 95% probable errors: ε∆P , 0.95 = 136.89• Two sigma limit : 2σ = 0.88
DISCUSSION
Model works well in the range of:• N=8 up to 14 plates• Low to medium-high flow rate
At a very high flow rate (when control valve shows PI1 ≈ 2 bar):• Accurate inlet pressure readings P1 were hard to obtain
• Residuals between data model and processing model increase• Data started showing outliers, model does not fit data well
REFERENCES1. Munson, Bruce R., Ted H. Okiishi, Wade W. Huebsch, and Alric P.
Rothmayer. Fundamentals of Fluid Mechanics, 7th edition. Jefferson City: John Wiley & Sons, Inc, 2013. 400-410, 416-431. Print.
2. Rhinehart, R. R. (2016). Lessons on Data Analysis and Model and Procedure Validation. Oklahoma State University.
3. Venugopal, Vidhya. Standard Operating Procedures: Experiments in Plate and Frame Filter Press. Oklahoma State University.
Pressure Drop Model and Experimental
VariabilityPlate and Frame Filter Press
Erin Durkee
Yen Nguyen
Dalton Russell
Conclusion:
QUESTIONS?
∆ 𝑃𝑐𝑜𝑚𝑏𝑖𝑛𝑒𝑑=(0.0484 +10.01𝑁 )∗𝑄+(0.0009+
5.47𝑁3.41 )∗𝑄3.41
Units:• ∆Pcombined (psig)• Q (gal/min)