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Synfuel Production

Inventor: Frederick MacDonnell
Year: 2016
Device: Photothermochemical Flow Reactor
Folder: macdonell
Original: Open article
Confidence
0.90
Practicability
0.60
Evidence
0.60
Fringe Score
0.30
Risk
0.20
TRL
4

Goal

Convert carbon dioxide and water directly into usable liquid hydrocarbon fuels.

Problem

Atmospheric CO_2 emissions and the need for renewable, drop-in liquid fuels for transportation.

Concept Summary

A single-stage photothermochemical process that uses concentrated sunlight (photochemical excitation) and heat (thermochemical reaction) in a flow reactor at 180-200 deg C and 1-6 bar to reduce CO_2 and H_2O to C_5^+ liquid hydrocarbons and O_2, employing a TiO_2-based catalyst doped with cobalt and other additives.

Principles

  • Photocatalysis
  • Thermochemistry
  • Solar concentration

Scientific Domains

Chemistry Chemical Engineering Materials Science

Materials

  • Titanium dioxide (TiO_2)
  • Cobalt (Co) on TiO_2
  • Hygroscopic salts (e.g., phosphates, sulfates)
  • Redox-active metal salts (e.g., Mn, Fe, Co, Ni salts)

Mechanisms of Action

  • Photochemical excitation of TiO_2 to generate high-energy intermediates
  • Thermal carbon-chain formation driven by elevated temperature and pressure
  • Coupled water oxidation and CO_2 reduction

Energy Sources

Solar radiation (concentrated sunlight)

Applications

  • Renewable gasoline, diesel, and jet fuel
  • Carbon-neutral fuel cycle
  • Solar-driven chemical production

Claimed Performance

In the best laboratory run, >13 % by mass of the product stream were C_5^+ hydrocarbons (e.g., octane) and O_2 yields ranged from 64 % to 150 % of the theoretical maximum.

Experimental Evidence

Demonstrated in a gas-phase flow photoreactor at 180-200 deg C and 1-6 bar using a 5 % Co/TiO_2 catalyst under UV irradiation; product distribution shifted to higher carbon numbers with increased temperature and pressure.

Replication Status

Only reported by the original research team; no independent replication or commercial scaling documented.

Limitations

  • Low hydrocarbon yield (13 % mass) - not yet commercially viable
  • Requires elevated temperature and pressure
  • Current catalyst absorbs only UV portion of solar spectrum
  • Scale-up and continuous operation not demonstrated

Red Flags

  • Potential overstatement of near-term commercial viability

Keywords

CO_2 reduction Solar fuels Photocatalysis Thermochemistry Liquid hydrocarbons Renewable energy

Related Technologies

Solar-driven fuel synthesis Photocatalytic water splitting Fischer-Tropsch synthesis

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