Reactive Separation To Upgrade Bioprocess Intermediates To Higher Value Liquid Fuels or Chemicals

• US 20090182064A1
• Filed: 01/14/2009
• Published: 07/16/2009
• Est. Priority Date: 01/14/2008
• Status: Abandoned Application

• Current Assignee: Logos Technologies, Inc. (Instem Plc)
• Original Assignee: Pennsylvania Sustainable Technologies LLC (Instem Plc)
• Inventors: Griffin, Thomas Paul
• Application Number:
  US12/353,654
• Publication Number:
  US 20090182064A1
• Time in Patent Office: Days
• US Class Current: 518/711
• CPC Class Codes: C07C 29/32 increasing the number of carbon atoms by reactions without formation of -OH groups
• CPC Class Codes: C07C 31/12 containing four carbon atoms
• CPC Class Codes: C07C 31/125 containing five to twenty-two carbon atoms
• CPC Class Codes: Y02P 20/10 Process efficiency

Abstract

The process and system of the embodiments utilize a reactive separation unit to upgrade a bioprocess intermediate stream to higher value liquid fuels or chemicals. The reactive separation unit simultaneously enables molecular weight and density increases, oxygen content reduction, efficient process energy integration, optional water separation for potential reuse, and incorporation of additional hydrocarbons or oxygenated hydrocarbons as co-feed(s). The use and selection of particular co-feed(s) for this purpose enables tailoring of the intended product composition. The process and system yields a product of higher alcohols, liquid hydrocarbons, or a combination of these. These can be split into two (or more) boiling point fractions by the same reactive separations unit operation resulting in product(s) that can be used as chemicals, chemical intermediates, or alternative (non-fossil-based) liquid transportation fuels.

Claims

1. A chemical conversion process that converts a bioprocess output stream to higher-valve liquids, the process comprising:

introducing the bioprocess output stream into a reactive separation unit, the bioprocess output stream comprising at least one component selected from the group consisting of a hydrocarbon product, an oxygenated hydrocarbon product, and mixtures thereof;

introducing a second stream into the reactive separation unit, the second stream comprising at least one component selected from the group consisting of carbon monoxide, hydrogen, syngas, alcohols, oxygenated hydrocarbons, and mixtures thereof;

combining the bioprocess output stream and the second stream; and

subjecting the combined streams to reactive separation to produce at least one product selected from the group consisting of higher alcohols, higher aliphatic hydrocarbons, and mixtures thereof,

thereby converting at least a portion of the bioprocess output stream to higher value liquid fuels or chemicals by reaction and separation of selected size fractions or boiling point product fractions of the bioprocess output stream.

2. The process of claim 1, wherein the first stream is an aqueous solution comprising one or more alcohols or poly-alcohols.

3. The process of claim 2, wherein the aqueous solution is an intermediate product of fermentation or other bioprocessing operations.

4. The process of claim 1, wherein the second stream is a syngas stream comprising CO and H₂.

5. The process of claim 4, wherein the relative molar concentrations of H₂ and CO in the syngas (H₂ to CO ratio) is within the range of from about 1.0 to about 3.0.

6. The process of claim 1, wherein the reactive separation is accomplished by reactive distillation.

7. The process of claim 1, wherein subjecting the combined streams to reactive separation produces an oxygenated hydrocarbon product, the oxygenated hydrocarbon product produced by one or more processes selected from the group consisting of catalytic alcohol condensation with dehydration, and catalytic aldol coupling reaction.

8. The process of claim 1, wherein subjecting the combined streams to reactive separation produces higher aliphatic hydrocarbons, the aliphatic hydrocarbons produced by a catalytic Fischer-Tropsch reaction.

9. The process of claim 1, wherein subjecting the combined streams to reactive separation produces both higher alcohols and higher aliphatic hydrocarbons through parallel reactive separation schemes, in which and a first reactive separation yields primarily liquid aliphatic hydrocarbons, and a second reactive separation yields primarily liquid higher alcohols.

10. The process of claim 9, wherein the primarily liquid aliphatic hydrocarbons from the first reactive separation and the primarily liquid higher alcohols from the second reactive separation are combined in a desired ratio.

11. The process of claim 1, further comprising:

operating slurry-phase, multiphase, or other well-mixed heterogeneous catalytic liquid upgrading reactions in a region in the reactive separation unit in tandem with the remaining portions of the process.

12. The process of claim 11, further comprising:

operating phase separation in a region in the reactive separation unit, the phase separation operated in tandem with the slurry-phase, multiphase, or other well-mixed heterogeneous catalytic liquid upgrading reactions, wherein the phase separation facilitates removal of a water-rich phase from reactive slurry and return of organic-rich phase for continued reaction or rectification.

13. The process of claim 11, further comprising:

separating an aqueous-organic phase mixture and removing water or a water-rich phase from the reactive separation unit through one or more processes selected from the group consisting of an interstage pressure drop, nozzle arrangement, and isenthalpic flash.

14. The process of claim 11, further comprising:

removing water or a water-rich phase from the reactive separation unit during an intermediate stage in which the interstage pressure drops and the overall pressure profile over the path of the reactive separations facilitates the removal.

15. The process of claim 1, wherein the bioprocess output stream comprises at least dilute bioethanol.