obanion
Automotive
- Jan 1, 2004
- 101
The CO2 idea I thought was bad, thanks to everyone here for comfirming it. Now I can inquire about something that may actually work.
Turbo will NOT be connected to exhaust. Turbine will have it's own dedicated "on demand" system.
As follows:
Combustion chamber, still unsure of size (thinking 4" tubing by 12" long, necking down to 2.5" at the end to enter turbo).
Four things will go into the chamber:
1. Propane (already being used as main fuel, others would use gasoline)
2. Pure oxygen gas
3. Water (probably pre-heated by engine coolant to save fuel)
4. Powerful ignition source. Seen some things used by back yard turbo-> jet makers, probably get something similar.
The ratio of propanexygen will be 1:3.62 (stoich), maybe a little richer if I get more heat by doing so. Ratio of waterropane I calculate at 13.76:1. My initial math tells me this should give me a result of 1500F superheated steam, with some other 1500F products of combustion.
Since at 1500F, steam has about 1.57x the volume of air, and that there are no serious drawbacks to running elevated amounts of backpressure if it aids things, I think I could power a compressor to move 60-70lb/min of air with as little as 1.6GPM water, and 3.5lb/min oxygen. Certainly a reasonable usage cost.
Feel free to point out anything I'm missing.
Turbo will NOT be connected to exhaust. Turbine will have it's own dedicated "on demand" system.
As follows:
Combustion chamber, still unsure of size (thinking 4" tubing by 12" long, necking down to 2.5" at the end to enter turbo).
Four things will go into the chamber:
1. Propane (already being used as main fuel, others would use gasoline)
2. Pure oxygen gas
3. Water (probably pre-heated by engine coolant to save fuel)
4. Powerful ignition source. Seen some things used by back yard turbo-> jet makers, probably get something similar.
The ratio of propanexygen will be 1:3.62 (stoich), maybe a little richer if I get more heat by doing so. Ratio of waterropane I calculate at 13.76:1. My initial math tells me this should give me a result of 1500F superheated steam, with some other 1500F products of combustion.
Since at 1500F, steam has about 1.57x the volume of air, and that there are no serious drawbacks to running elevated amounts of backpressure if it aids things, I think I could power a compressor to move 60-70lb/min of air with as little as 1.6GPM water, and 3.5lb/min oxygen. Certainly a reasonable usage cost.
Feel free to point out anything I'm missing.