Post on 25-Feb-2016
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Team Leader: Megan O’ConnellMatt Burkell
Steve DigerardoDavid Herdzik
Paulina KlimkiewiczJake Leone
P13027: Portable Ventilator
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Technical Review OverviewEngineering SpecsProposed redesignBattery and Power CalculationsPower: ElectricalElectric Board LayoutMCU LogicPressure SensorThermal AnalysisHousing ModificationsProject ComparisonProject ScheduleQuestions?22 of 52
Engineering SpecificationsPortable Emergency Ventilator
Engineering Specifications - Revision 1 - 03/19/13
Specification Number Source Function Specification (Metric) Unit of Measure Marginal Value Ideal Value Comments / Status
S1 PRP System Volume Control Liters 0.2 ± 0.2
S2 PRP System Breathing Rate BPM, Breaths per Minute 4 -15
S3 PRP System Pick Flow Liter/Min 15 - 60
S4 PRP System Air Assist Senitivity cm H20 0.5 ± 0.5
S5 PRP System High Pressure Alarm cm H20 10 - 70
S6 PRP System DC Input Volts 6 - 16 Due to battery, must be greater than 9V
S7 PRP System DC Internal Battery Volts 12
S8 PRP System Elasped Time Meter Hours 0 - 8000
S9 PRP System Pump Life Hours 4500
S10 PRP System O2 / Air mixer O2 21% - 100 %
S11 PRP System Secondary Pressure Relief cm H20 75
S12 PRP System Timed Backup BPM
S13 PRP System Weight Kg ≤ 8
S14 Robustness Drop Height meter 1
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Revision B- Proposed RedesignUpdate:1. Battery Size-> Reduce Size & keep same capacity2. Reduce Circuit Board size-> Create custom board for all electrical
connects3. Phase motor driver to a transistor4. Display Ergonomics5. Overall Size and shape of PEV6. Instruction manual
Additions:7. Visual Animated Display-> Moving Vitals8. Memory capabilities9. USB extraction of Data10. Co2 Sensor as additional Feature to PEV11. Overload Condition due to Pump Malfunction
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Revision B- Proposed RedesignUpdate:1. Battery Size-> Reduce Size & keep same capacity2. Reduce Circuit Board size-> Create custom board for all electrical
connects3. Phase motor driver to a transistor4. Display Ergonomics5. Overall Size and shape of PEV6. Instruction manual
Additions:7. Visual Animated Display-> Moving Vitals8. Memory capabilities9. USB extraction of Data10. Co2 Sensor as additional Feature to PEV11. Overload Condition due to Pump Malfunction
NOT Discussed within Technical Review
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Battery Choice: Tenergy Li-Ion14.8 V4400mAh0.8375 lbs7.35cm x 7.1cm x
3.75cmRechargeable up to
500 timesPrice: $50.99
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Power CalculationCurrent (A)
Voltage (V)
Power (W)
Pump 3 11.1 16.65MCU + electronics 0.5 3.3 1.65LCD 0.15 10 1.5Total 3.65 19.8
Battery Voltage (V) 14.8Battery Capacity (Ah) 4.4Battery Capacity (Wh) 65.12Expected Battery Life (Hrs)
3.29
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Charger (Brick)HP AC Adapter18.5V3.5AmpsPower: 65WMax power: 70WPrice: $14.35
(Amazon)
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Regulation of Power
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Maxim Integrated MAX1737 Battery-Charge Controller
• Wide input voltage range (6-28 V)
• Charges up to four Li+ Cells (4-4.4V per cell)
• Provides overcharge protection
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Texas InstrumentsLM3940 Low Dropout Regulator
• Provides 3.3V from a 5V supply
• Low Dropout Regulator• Can hold 3.3V output
with input voltages as low as 4.5V
• Few external components needed for implementation
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ON SemiconductorMC7800 Voltage Regulator
5-18, 24 V Input voltage range
Can deliver output currents greater than 1 A
No external components needed for implementation
Internal thermal overload protection
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System Operation Flowchart
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Control System
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MCU Pinouts
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General PCB Parts Placement
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• Difference in Absorption between Red and Infrared is used to determine SpO2
SpO2 Sensor
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Simplified Design:
SpO2 Sensor Continued
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SpO2 Flow Chart
Source: Freescale Pulse Oximeter Fundamentals and Design
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Hardware/Software Feature Implementation Plan
1- High Priority- This will get implemented 2- Medium Priority- Foreseeable difficulties may prevent
proper implementation 3- Low Priority- Attempt to implement if time constraints
allow
Function Hardware SoftwareUser controllable
ventilator control system1 1
LCD Interface 1 1Audio Feedback 1 1
Memory retention/ transfer 1 2Touch Interface 1 3
Integrated Battery Charging
2 N/A
SpO2 2 2CO2 2 2
Audio Recording 3 3
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Initial strategy for Testing
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Mass Flow Analysis(Between Pump outlet and Ventilator outlet)
Replacing Mass Flow Sensor with Venturi Analysis•Assume incompressible flow, 10 diameters of straight tube, C=.99
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Option 1 Option 2 Option 3 Option 4
FreeScale MPXV7007
FreeScale MPXV7002
FreeScale MPX12
FreeScale MPXV5010
Score Score Score ScoreCost $13.94 $13.94 $8.67 $12.81 Physical Size (in 3̂) 0.084 0.084 0.292 0.084Compensated (˚C) 0-85 10-60 XXX 0-85Sensitivity (mV/kPa) 286 1000 5.5 450Operating Range (˚C) -40-125 10-60 -40-125 -40-125Operating Pressure (kPa) -7-7 -2-2 0-10 0-10Accuracy 5% 6.25% XXX 5%Output (V) .5-4.5 .5-4.5 Fullscale .2-4.7Easy to Amplify No No No Yes
Rank 2 3 4 1
Pressure Sensor: Selection Criteria
Differential pressure sensor selection
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Freescale-mpxv5050dp Pressure Sensor
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Temperature Compensation
3.3 V
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Expected Pressure change & voltage output
D1 D2 D1 D2 A1 A2 vdot vdot mdot ΔP ΔP Voltagein in m m m^2 m^2 l/min m^3/sec kg/s Pa PSI mV
0.375 0.25 0.0095 0.00635 7.13E-05 3.17E-05 1 1.67E-05 1.97E-05 0.13 1.95E-05 0.0610 1.67E-04 1.97E-04 13.42 1.95E-03 6.0425 4.17E-04 4.93E-04 83.90 1.22E-02 37.76
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Expected Centerline Velocity
Q Q D D A avg V Re n Centerline V Centerline V Mach
l/min m^3/sec in m m^2 m/s m/s mph
25 0.000416667 0.25 0.00635 3.16692E-05 13.15683 5328.183 5.007842 17.3600175 38.83435915 0.050583
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EXPECTED Total Head Loss
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Expected Major Head LossBernouli’s Equation Assumptions
• Constant velocity, height and air densityMajor Head Loss:
• Dependent on length of tube between ventilator and pump exit
Q Q D D L A avg V Re f hl ΔP ΔPl/min m^3/sec in m m m^2 m/s m2/s2 Pa PSI
25 4.17E-04 0.25 0.0064 0.1 3.17E-05 13.16 5328.18 0.0370 50.41 59.69 0.009
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Expected Minor Head LossBernouli’s Equation Assumptions
• Constant velocity, height and air densityMinor Head Loss
• Dependent on the expansion and contraction for Reducer and Diffuser
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Exhaust Pressure Sensor
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Mechanical Relief Valve
Pressure Release at 1 psi Reusable
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Thermal Analysis Heat Dissipation① System Components:
② Applied Heat Loads:
③ Assumptions:1. Neglect Radiation2. Casing acts as a control volume3. System Location at hottest temp every recorded for U.S 330K 4. Heat flux is applied at bottom surface where all components will rest on.5. Free External Convection
T∞=330Kh= 5 W/m^2K(Applied to all
surfaces)Q flux=80 W
PEV
④ Control Volume Schematic:
GOAL: Analyze worst case thermal analysis of system to understand effects of system heat dissipation.
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High Temperature: 359 K 86 ⁰C
For our material, Polystyrene,The glass transition temperature is 95 ⁰C. Therefore at worst case scenario, the material will hold shape without deforming.
Top of enclosure shows little heat transfer concern to handle so user can carry device. A rubber handle will be included on prototype as a precautionary measure as well as usability purposes.
⑤ Heat Dissipation Results:
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Another approach…① Bottom Surface Heat Dissipation:
② Assumptions:
1. Component temperature is worst case.
2. System has been under worst case condition for extended period of time.
3. Neglect convection and radiation on bottom surface.
③ Results:1. Plastic temperature at worst case will never
exceed 120⁰F due to component heating alone.2. This temperature is not enough to deform the
polystyrene surface or cause damage to surrounding components.
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Housing Modifications13026 Physical Extremes:
15in long X 10in high X 7in deep
Projected 13027 Physical Extremes:12in long X 7.5in high X 7in deep
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Housing Modifications
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Housing Modifications
Speaker
O2 Sensor port
CO2 Sensor port
Mask tube ports
BPM Flow Rate Pressure Limit
Mode
CPR Compression #
Manual
Power
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Housing Modifications
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Housing Modifications
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Housing Modifications
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Housing Modifications
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Housing Modifications
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Project ComparisonGOAL: Analyze the size and weight reduction between major contributing components of MSD 13026 PEV to our projected design.
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Summary:
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13027 – Project Schedule through MSD 1
END OF
MSD 1
Project Familiarization/ Research:
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END OF
MSD 1
Technical Evaluations/ Begin Prototyping:
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