Heavy fossil hydrocarbon conversion and upgrading using radio-frequency or microwave energy

Patent metadata

Field	Value
Publication number	US-9862892-B2
Application number	US-201414464635-A
Country	US
Kind code	B2
Filing date	Aug 20, 2014
Priority date	Feb 21, 2012
Publication date	Jan 9, 2018
Grant date	Jan 9, 2018

Abstract

Conversion of heavy fossil hydrocarbons (HFH) to a variety of value-added chemicals and/or fuels can be enhanced using microwave (MW) and/or radio-frequency (RF) energy. Variations of reactants, process parameters, and reactor design can significantly influence the relative distribution of chemicals and fuels generated as the product. In one example, a system for flash microwave conversion of HFH includes a source concentrating microwave or RF energy in a reaction zone having a pressure greater than 0.9 atm, a continuous feed having HFH and a process gas passing through the reaction zone, a HFH-to-liquids catalyst contacting the HFH in at least the reaction zone, and dielectric discharges within the reaction zone. The HFH and the catalyst have a residence time in the reaction zone of less than 30 seconds. In some instances, a plasma can form in or near the reaction zone.

First claim

The invention claimed is:

1. A method for selectively preparing paraffins from heavy fossil hydrocarbons (HFH), the method comprising:
continuously providing reactants to a reaction zone, the reactants comprising HFH, catalyst, and methane wherein the providing the reactants to the reaction zone comprises continuously dispersing the HFH feed within a process gas to form a mixture of the HFH feed and the process gas within the reaction zone;
exposing the reactants in the reaction zone to microwave or RF energy, the exposing selectively converting at least a portion of the HFH to paraffins; and
recovering at least the paraffins from the reaction zone.

2. The method of claim 1 , wherein the catalyst comprises one or more of iron, char, and/or a promoter of dielectric discharge.

3. The method of claim 1 , further comprising maintaining a pressure in the reaction zone of from between 0.9 atm and 7 atm.

4. The method of claim 1 , wherein the reactants are exposed within the reaction zone for residence time from between 5 milliseconds and 30 seconds.

5. The method of claim 1 wherein the paraffins comprise straight chained hydrocarbons.

6. The method of claim 1 wherein the exposing selectively converts the HFH to paraffins rather than aromatic hydrocarbons.

7. A method for converting aromatic hydrocarbons of heavy fossil fuel (HFH) to methylated aromatic hydrocarbons, the method comprising:
continuously providing reactants to a reaction zone, the reactants comprising HFH, catalyst, and methane, wherein the HFH comprises aromatic hydrocarbons, and wherein the providing the reactants to the reaction zone comprises continuously dispersing the HFH feed within a process gas to form a mixture of the HFH feed and the process gas within the reaction zone;
exposing the reactants in the reaction zone to microwave or RF energy to form a product, the exposing selectively converting at least a portion of the aromatic hydrocarbons to methylated aromatic hydrocarbons; and
recovering at least a portion of the product from the reaction zone, the portion of the product comprising at least a portion of the methylated aromatic hydrocarbons.

8. The method of claim 7 , wherein the reactants are exposed within the reaction zone for residence time from between 5 milliseconds and 30 seconds.

9. The method of claim 7 , further comprising separating a flowable portion of the product from a remainder of the product, the flowable portion of the product comprising methylated aromatic hydrocarbons and paraffins.

10. The method of claim 9 wherein the remainder of the product comprises unflowable aromatic hydrocarbons.

11. A method for selectively preparing paraffins from heavy fossil hydrocarbon (HFH), the method comprising:
continuously providing reactants to a reaction zone, the reactants comprising HFH, catalyst, and methane, wherein the providing the reactants to the reaction zone comprises continuously dispersing the HFH feed within a process gas to form a mixture of the HFH feed and the process gas within the reaction zone;
exposing the reactants in the reaction zone to microwave or RF energy, the exposing selectively converting at least a portion of the HFH to product, the product comprising paraffins and aromatics, wherein the ratio of paraffins to aromatics is greater than 0.05:1; and
recovering at least the paraffins from the reaction zone.

12. The method of claim 11 wherein the product comprises gaseous, liquid flowable, and non-flowable materials, and wherein the method further comprises separating at least one of the gaseous, liquid flowable, and non-flowable materials from the product of the reaction zone.

13. The method of claim 12 wherein the liquid flowable material comprises paraffins.

14. The method of claim 12 wherein the liquid flowable material comprises methylated aromatics.

15. The method of claim 12 wherein the liquid flowable material comprises both methylated aromatics and paraffins.

16. The method of claim 12 wherein the gaseous material comprises single ring aromatics.

17. The method of claim 12 wherein the liquid flowable material comprises alkylated aromatics.

Assignees

• Battelle Memorial Institute

Inventors

• Strohm James J
• Roberts Benjamin Q
• Smurthwaite Tricia D
• Bergsman Theresa M
• Bearden Mark D

Classifications

• B01J2219/00835

  Comprising catalytically active material · CPC title

• B01J2219/00792

  One or more tube-shaped elements · CPC title

• B01J2219/1272

  Materials of construction · CPC title

• B01J2219/1239

  Means for feeding and evacuation · CPC title

• B01J2219/0894

  Processes carried out in the presence of a plasma · CPC title