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Next Generation Charcoal Stove for Haiti

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Presentation on theme: "Next Generation Charcoal Stove for Haiti"— Presentation transcript:

1 Next Generation Charcoal Stove for Haiti
Team P12442 Marissa Blockus, Brandon Harbridge, Sam Huynh, Brianna Stephenson-Vallot, Dustin Tyler

2 Team Members Brandon Harbridge (IE) – Team Lead, Test Technician
Stove Team Samantha Huynh (ME) – Lead Engineer Brianna Stephenson-Vallot (ME) – Team Engineer, Purchaser Thermoelectric Team Marissa Blockus (ME) – Team Facilitator Dustin Tyler (ME) – Team Engineer, EE Liaison

3 Purpose of Review Demonstrate the group’s progress in accepting the tasks involved in creating two functioning Haitian cook stoves To gain feedback on the group’s current path to verify that the team has a complete understanding of the project Finalize customer Needs/Specs To obtain constructive criticism in order to improve as young engineers

4 Customer Needs-Stove

5 Engineering Specs-Stove

6 Customer Needs-TEG

7 Engineering Specs-TEG

8 System Energy Flow-Stove

9 System Map

10 Start-Up Flow Diagram

11 TEG Diagram 1

12 TEG Diagram 2

13 TEG Heat Transfer Analysis
Delta T 200 degrees C Tc (C) 100 110 120 130 140 150 160 170 180 Th (C) 300 310 320 330 340 350 360 370 380 Imax 1.26 qh (W) 156.25 156.69 157.12 157.56 158.00 158.43 158.87 159.30 159.74 qc (W) 151.89 152.33 152.76 153.20 153.64 154.07 154.51 154.94 155.38 W (W) 4.36 At a temperature difference other than 200C 125 225 235 245 255 265 275 285 295 305 0.788 96.12 96.40 96.67 96.94 97.21 97.49 97.76 98.03 98.30 94.42 94.69 94.97 95.24 95.51 95.78 96.06 96.33 96.60 1.70 250 260 270 280 290 0.945 115.96 116.29 116.62 116.94 117.27 117.60 117.92 118.25 118.58 113.51 113.84 114.16 114.49 114.82 115.14 115.47 115.80 116.13 2.45 175 315 325 335 345 355 1.103 136.00 136.39 136.77 137.15 137.53 137.91 138.29 138.68 139.06 132.67 133.05 133.43 133.81 134.19 134.57 134.96 135.34 135.72 3.34 Measured Constants α 0.035 V/K Re 2.745 ohms Rth 1.376 K/W K 0.7267 W/K Governing Equations qh = α*Th*I + K*(Th-Tc) - 1/2*Re*I^2 qc = α*Tc*I + K*(Th-Tc) + 1/2*Re*I^2 Imax = α*(Th-Tc)/(2*Re) W = qh-qc What this shows… The heat conduction required from the fire to achieve the hot side temperature as well as the cooling required to maintain the cold side temperature. Though this is a crude representation, it represents a basis for further study.

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15 Morphological Chart

16 System, Materials and Manufacturing, TEG, Fan and Conducting Rod Risks
Associated Risks System, Materials and Manufacturing, TEG, Fan and Conducting Rod Risks

17 1-low likelihood/severity, 2-moderate likelihood/severity, 3-high likelihood/severity

18 1-low likelihood/severity, 2-moderate likelihood/severity, 3-high likelihood/severity

19 1-low likelihood/severity, 2-moderate likelihood/severity, 3-high likelihood/severity

20 1-low likelihood/severity, 2-moderate likelihood/severity, 3-high likelihood/severity

21 1-low likelihood/severity, 2-moderate likelihood/severity, 3-high likelihood/severity

22 Pugh Charts Stove Team

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24 Pugh Charts TE Team

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29 Project Plan

30 Work Breakdown Structure

31 Future Plans Detailed heat transfer analysis of proposed heat harvesting system to determine appropriate heat sink and conduction rod sizing. Calculate all percentage heat losses within the stove system to better optimize future designs. Analyzing the need for a change in combustion chamber geometry. Test existing RIT stove to compare empirical data with theoretical models and determine overall efficiency of the system.

32 Questions?


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