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ME 414 : Project 1

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You have a space of 12' in the outside walls and 8' in the interior walls. Deliverables ... heat exchanger shell and tube weight. Minimize heat exchanger ... – PowerPoint PPT presentation

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Title: ME 414 : Project 1


1
ME 414 Project 1
  • Heating System for NASA North
    Pole Project

May 5, 2006
Team Members Alan Benedict Jeffrey Jones Laura
OHair Aaron Randall
2
Problem Statement
Your job as a Thermal Fluid Systems engineer is
to deliver the housing heating system in the
North Pole.
4 occupants Oxygen supply tank or
circulating fresh air from outside The
outside temperature in North Pole is -40C and the
desired temperature inside the housing is
25C. You have a space of 12 in the outside walls
and 8 in the interior walls.
3
Deliverables
  • Lowest blower cost measured by the least system
    pressure drop
  • Least material cost measured by the number of
    sheets used
  • Least labor cost per the labor rates given
  • Least operating cost measured by the cost of
    maintenance items and monthly natural gas,
    oxygen, electricity, etc usage.
  • Most comfort to occupants measured by the least
    flow rate variation between registers

4
Supply Air System
5
Return Air System
6
Heat Loss Calculation Assumptions
  • All heat loss occurs through exterior walls and
    roof.
  • The structure is perfectly sealed. No transfer of
    air.
  • There is no heat transfer between rooms.
  • There is not heat transfer to or from the
    basement.

7
Heat Loss Calculations
  • Interior Temperature
  • 25C
  • Exterior Temperature
  • -40C
  • Thermal Conductivity of Wall
  • 0.8W/mC
  • Convection Coefficients
  • Interior surfaces
  • Walls 4.2W/m2C
  • Roof 5.17W/m2C
  • Exterior
  • All surfaces 34W/m2C

8
Heat Loss Calculations
  • Used Resistance Network
  • Results
  • Roof
  • Walls
  • Heat Loss
  • Room 1 7791.5W
  • Room 2 10118.9W
  • Room 3 6269.2W
  • Room 4 7380.7W
  • Room 5 8457.8W
  • Total 40018.1W

9
Heat Loss Calculations With Insulation Added
  • Resistance Network
  • Insulation Conductivity
  • k0.043W/m2C
  • Results
  • Roof
  • Walls
  • Heat Loss
  • Room 1 489.9W
  • Room 2 634.3W
  • Room 3 394.4W
  • Room 4 466.7W
  • Room 5 534.8W
  • Total 2520.1W
  • 8598.9Btu/h

10
Heat Loss Rates
  • Heat loss rate through walls and roof
  • 2520W
  • Heat loss rate through heating of outside air
  • 72W

11
Insulation Cost Benefit Analysis
  • Cost to add insulation
  • 12 inches in walls and roof
  • Total of 3501.1 ft3 insulation required
  • Cellulose insulation cost 0.387 per ft3
  • Total cost to add insulation 1354.07

12
Insulation Cost Benefit Analysis
  • Heat loss rate without insulation
  • 40,018.1W
  • Heat loss rate with insulation
  • 2,520.1W
  • Heat loss rate reduction
  • 37,498W or 93.7

13
Insulation Cost Benefit Analysis
  • 4 month cost to heat house without insulation
  • 20,903.11
  • 4 month cost to heat house with insulation
  • 1,316.35
  • 4 month savings
  • 19,586.75
  • Time to recover cost of insulating
  • 8.4 days

14
Fresh Air or Oxygen Tank?
  • 4 month analysis of using bottled O2
  • 5.3592 x 10-4 m3/s O2 consumption rate
  • 3000L volume of O2 in tank at 1atm
  • 1,050 per bottle material
  • 75 per bottle labor
  • COST
  • 2,112,750

15
Fresh Air or Oxygen Tank?
  • 1.6 ft3/min addition of outside air to interior
  • 5.3592 x 10-4 m3/s occupants
  • 7.7794 x 10-4 m3/s burning gas
  • -40C air temperature
  • 0.045/ft3 cost for natural gas
  • COST
  • 32.28

16
Furnace and Blower
  • Gibson KG6RA Series Specifications
  • 45000 Btu/h
  • 80 Efficiency
  • Cost of 543

17
Furnace and Blower
  • Blower Electrical Consumption and Cost
  • for 4 months
  • Electricity Consumption
  • 1/5 hp 149.14W
  • 149.14W2880hrs 429.5kWhrs
  • Operational Cost
  • 429.5kWhrs0.4/kWhr 171.80

18
Materials
  • Duct Diameter
  • 7.43 inches
  • 3 ducts per each 90 X 70 sheet

19
Materials
  • Total sheets
  • 9
  • 90 degree bends
  • 6
  • Branches
  • 9
  • Registers
  • 9

20
Material and Labor Costs
  • CIRCULAR DUCTS
  • Material
  • 2,250.00
  • Labor
  • 2,400.00
  • Total
  • 4,650.00
  • SQUARE DUCTS
  • Material
  • 3,250.00
  • Labor
  • 2,600.00
  • Total
  • 5,850.00

21
Problems not Overcome
  • Flowmaster
  • Flow rates in pump do not coincide with branch
    flow rate
  • Flow rates dont produce results as expected

22
Flow Output of Pump Lower than First Branch
23
Register size vs. output discrepancy
24
Conclusion
  • Least Pressure Drop not achievable through
    Flowmaster
  • Least material cost calculated at 4147
  • Least labor cost calculated at 2400
  • Least operating cost calculated at 1488
  • Flow rate variation between registers not
    achievable through Flowmaster

25
Questions?
26
ME 414 Project 2
  • Heat Exchanger Optimization

May 5, 2006
Team Members Alan Benedict Jeffrey Jones Laura
OHair Aaron Randall
27
Problem Statement
  • Design a heat exchanger to meet the customer
    requirements for heat transfer and maximum
    dimensions, while optimizing the weight and
    pressure losses in both the tube and shell sides.

28
Project Definition
  • Chemical Specifications
  • Temperature must be reduced from 35C to 25C
  • Mass flow rate is 80,000 kg/hr
  • Material properties closely approximate that of
    water
  • Cooling Water Specifications
  • Treated city water at 20C
  • Mass flow rate is not fixed
  • Exit temperature is function of design

29
Customer Requirements
  • Must cool the chemical from 35 C to 25 C
  • Heat exchanger length can not exceed 7m
  • Heat exchanger shell diameter can not exceed 2m
  • Minimize heat exchanger shell and tube weight
  • Minimize heat exchanger pressure drop

30
Initial Design Specifications
31
Initial Results
  • Desired heat transfer rate of 928,502W
  • Calculated heat transfer rate of 924,068W
  • Difference of 4,434W
  • Desired-to-calculated ratio 0.995

32
First DOE Results
33
Initial Design Specifications
34
Final DOE Pareto Charts
35
Final DOE Optimization
Without Baffles
With Baffles
36
Specifications for Optimized Heat Exchanger
  • Counter flow design
  • Stainless steel material for shell and tube
  • Single pass shell
  • Single pass tube
  • Tube OD of 2.22cm (standard size)
  • Tube length of 3.06m
  • Tube thickness of 2.40mm
  • Tube pitch of 3.18cm
  • Square tube configuration with 90 layout angle
  • Shell ID of 1.90m
  • No baffles

37
Final Results
38
Conclusion
  • Met requirement to cool the chemical from 35 C to
    25 C
  • Tube length of 3.06m 3.06m
  • Shell diameter of 1.9m 1.9m
  • Minimized heat exchanger shell and tube weight
    26,150 kg
  • Minimized pressure drop
  • Shell side 16.72 Pa
  • Tube side 22.36 Pa

39
Questions?
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