Aluminum Extractor from Clay Concept: Difference between revisions

From Open Source Ecology
Jump to navigation Jump to search
No edit summary
No edit summary
Line 1: Line 1:
This is a machine for processing clay, an abundant feedstock in many parts of the world (already in fine particles) into [[Aluminum]] - a high value, industrial metal. Note the energy requirement: *About 15kW-hours requirement for 1 kg aluminum produced (1.5 kg diesel energy equivalent at 100% conversion). About 1 gallon fuel consumption per kilogram of aluminum produced assuming 30% conversion of diesel to electrolysis current- super energy intensive indeed if done with traditional fuels
This is a machine for processing clay, an abundant feedstock in many parts of the world (already in fine particles) into [[Aluminum]] - a high value, industrial metal. Note the energy requirement:  
 
*About 15kW-hours requirement for 1 kg aluminum produced (1.5 kg diesel energy equivalent at 100% conversion). About 1 gallon fuel consumption per kilogram of aluminum produced assuming 30% conversion of diesel to electrolysis current- super energy intensive if done with traditional fuels
*Process design for producing 1 ton of aluminum per day
*Process design for producing 1 ton of aluminum per day
*Fueled by [[Solar Concentrator]] electrical power, and [[Modern Steam Engine]] as backup only for economic sense
*Fueled by [[Solar Concentrator]] electrical power, and [[Modern Steam Engine]] as backup only, for economic sense on a micro-scale
*About 300kW energy requirement for 24 hours per day - huge
*About 300kW energy requirement for 24 hours per day - huge
**Practical conversion: 2 acres of biomass fuel required to produce 1 ton of aluminum per year
**Practical conversion: 2 acres of biomass fuel required to produce 1 ton of aluminum per year
**For 15MW-hours of energy per year - solar concentrator requres under 100 square meters of area to fuel this production (assuming 10% solar conversion efficiency). Less than 1/40th of an acre. 100 times as area efficient as biomass.
**For 15MW-hours of energy per year - solar concentrator requres under 100 square meters of area to fuel this production (assuming 10% solar conversion efficiency). Less than 1/40th of an acre. 100 times as area efficient as biomass.
*About 100 grams of hydroflouric acid are required in a closed loop cycle to carry out the first hydrofluoric acid leaching process phase of aluminosilicate to alumina
*About 100 grams of hydroflouric acid are required in a closed loop cycle to carry out the first hydrofluoric acid leaching process phase of aluminosilicate to alumina
*Second phase is standard [[Hall-Heroult]] electrolysis
*Second phase is standard [[Hall-Heroult]] electrolysis.
*Approximately a 6000 square foot facility is required for housing the above process.
 
Strategically speaking - lunar regolith and Mars settlers are quite interested in this. This process has been developed for extraterrestrial applications initially, where there may be no bauxite.


Subject Matter Experts


[[Category:Design Rationale]]
[[Category:Design Rationale]]

Revision as of 02:16, 18 April 2011

This is a machine for processing clay, an abundant feedstock in many parts of the world (already in fine particles) into Aluminum - a high value, industrial metal. Note the energy requirement:

  • About 15kW-hours requirement for 1 kg aluminum produced (1.5 kg diesel energy equivalent at 100% conversion). About 1 gallon fuel consumption per kilogram of aluminum produced assuming 30% conversion of diesel to electrolysis current- super energy intensive if done with traditional fuels
  • Process design for producing 1 ton of aluminum per day
  • Fueled by Solar Concentrator electrical power, and Modern Steam Engine as backup only, for economic sense on a micro-scale
  • About 300kW energy requirement for 24 hours per day - huge
    • Practical conversion: 2 acres of biomass fuel required to produce 1 ton of aluminum per year
    • For 15MW-hours of energy per year - solar concentrator requres under 100 square meters of area to fuel this production (assuming 10% solar conversion efficiency). Less than 1/40th of an acre. 100 times as area efficient as biomass.
  • About 100 grams of hydroflouric acid are required in a closed loop cycle to carry out the first hydrofluoric acid leaching process phase of aluminosilicate to alumina
  • Second phase is standard Hall-Heroult electrolysis.
  • Approximately a 6000 square foot facility is required for housing the above process.

Strategically speaking - lunar regolith and Mars settlers are quite interested in this. This process has been developed for extraterrestrial applications initially, where there may be no bauxite.

Subject Matter Experts