Integrated membrane-pyrolysis systems and methods

1. A method of processing a mixture of heated vapors, at least two of which substantially differ in polarity from each other, the method comprising directing said mixture of heated vapors at a temperature of at least 150° C. through a hydrophobic or hydrophilic mesoporous membrane comprising a mesoporous coating of hydrophobized or hydrophilized metal oxide nanoparticles, respectively, wherein the hydrophobic mesoporous membrane permits passage of one or more hydrophobic heated vapors in said mixture of heated vapors and blocks passage of one or more hydrophilic heated vapors in said mixture of heated vapors, and wherein the hydrophilic mesoporous membrane permits passage of one or more hydrophilic heated vapors in said mixture of heated vapors and blocks passage of one or more hydrophobic heated vapors in said mixture of heated vapors.

2. The method of claim 1 , wherein the mesoporous membrane is hydrophobic and permits passage of said one or more hydrophobic heated vapors and blocks passage of said one or more hydrophilic heated vapors.

3. The method of claim 1 , wherein the mesoporous membrane is hydrophilic and permits passage of said one or more hydrophilic heated vapors and blocks passage of said one or more hydrophobic heated vapors.

4. The method of claim 1 , wherein said mixture of heated vapors includes water vapor.

5. The method of claim 4 , wherein said water vapor is separated from other less polar gaseous products when said mixture of heated vapors is processed by the mesoporous membrane.

6. The method of claim 5 , wherein the mesoporous membrane is hydrophilic and permits passage of water vapor and blocks passage of one or more hydrophobic heated vapors.

7. The method of claim 5 , wherein the mesoporous membrane is hydrophobic and permits passage of one or more hydrophobic heated vapors and blocks passage of water vapor.

8. The method of claim 5 , wherein at least 85% of the water in the mixture of heated vapors is separated from other less polar gaseous products.

9. The method of claim 5 , wherein at least 90% of the water in the mixture of heated vapors is separated from other less polar gaseous products.

10. The method of claim 1 , wherein said temperature is at least 200° C.

11. The method of claim 1 , wherein said temperature is at least 250° C.

12. The method of claim 1 , wherein said heated vapors emanate from a pyrolysis process.

13. The method of claim 12 , wherein said pyrolysis process comprises thermally decomposing organic material into a mixture of heated gaseous products, at least two of which substantially differ in polarity from each other.

14. The method of claim 13 , wherein said organic material is a hydrocarbon and said pyrolysis process is a hydrocarbon combustion process.

15. The method of claim 14 , wherein said hydrocarbon is a petrochemical fuel.

16. The method of claim 13 , wherein said organic material is a petrochemical fuel and said mixture of heated gaseous products is from an exhaust stream of an engine.

17. The method of claim 16 , wherein said exhaust stream further comprises water as a combustion byproduct, and said water is separated from other less polar gaseous products when said exhaust stream is processed by the mesoporous membrane.

18. The method of claim 13 , wherein said pyrolysis process is a biomass pyrolysis process.

19. The method of claim 13 , wherein said pyrolysis process is a biofuel production process.

20. The method of claim 19 , wherein said biofuel production process comprises a biomass pyrolysis step followed by an upgrading step followed by a fractionation step.

21. The method of claim 20 , wherein said mesoporous membrane is integrated in the biofuel production process by being located between the pyrolysis and upgrading steps and/or between the upgrading and fractionation steps.

22. The method of claim 21 , wherein the mixture of heated gaseous products emanating from said pyrolysis step or said upgrading step includes water as a combustion byproduct, and said water is separated from other less polar gaseous products when said mixture of heated gaseous products is processed by the mesoporous membrane.

23. The method of claim 22 , wherein the mesoporous membrane is hydrophilic and permits passage of water vapor and blocks passage of one or more hydrophobic gaseous products.

24. The method of claim 22 , wherein the mesoporous membrane is hydrophobic and permits passage of one or more hydrophobic gaseous products and blocks passage of water vapor.

25. The method of claim 22 , wherein at least 85% of the water in the mixture of heated gaseous products is separated from other less polar gaseous products.

26. The method of claim 22 , wherein at least 90% of the water in the mixture of heated gaseous products is separated from other less polar gaseous products.

27. An apparatus useful for the separation of heated vapors in a mixture of heated vapors wherein at least two of the heated vapors substantially differ in polarity from each other, the apparatus comprising a vapor production chamber that contains a heating element and is integrally connected with a hydrophobic or hydrophilic mesoporous membrane comprising a mesoporous coating of hydrophobized or hydrophilized metal oxide nanoparticles, respectively, wherein the hydrophobic mesoporous membrane permits passage of one or more hydrophobic heated vapors in said mixture of heated vapors and blocks passage of one or more hydrophilic heated vapors in said mixture of heated vapors, and wherein the hydrophilic mesoporous membrane permits passage of one or more hydrophilic heated vapors in said mixture of heated vapors and blocks passage of one or more hydrophobic heated vapors in said mixture of heated vapors.

28. The apparatus of claim 27 , wherein said vapor production chamber is a pyrolysis chamber.

29. The apparatus of claim 28 , wherein said pyrolysis chamber is a fuel-burning engine.