IP Library Granted Patent US 12678761
Granted Patent B2
US 12678761 · App. 18/623,477 · Granted Jul 14, 2026

Gas-to-liquid reactor and method of using

Inventors: Dennis Keith Manning (Miami, OK); Arland H. Johannes (Stillwater, OK)
Assignee: PlasMerica, LLC
B01J19/088C07C2/80B01J2219/0809B01J2219/0813B01J2219/083B01J2219/0875B01J2219/0892B01J2219/0896
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12678761
App. No.
18/623,477
Granted
Jul 14, 2026
Kind
B2
Abstract

A device and a process to propagate molecular growth of hydrocarbons, either straight or branched chain structures, that naturally occur in the gas phase to a molecular size sufficient to shift the natural occurring phase to a liquid or solid state is provided. According to one embodiment, the device includes a grounded reactor vessel having a gas inlet, a liquid outlet, and an electrode within the vessel; a power supply coupled to the electrode for creating an electrostatic field within the vessel for converting the gas to a liquid and or solid state.

Claims (32)

1 . A method for hydrocarbon conversion, comprising:

introducing a first gaseous hydrocarbon having a first molecular weight into a vessel, the vessel comprising an outlet and a liquid level controller coupled to a liquid control valve, and wherein the vessel is charged or grounded;

maintaining, via manipulation of the liquid control valve by the liquid level controller, a liquid level within the vessel so that the outlet of the vessel is located at a level below a liquid gas interface of the vessel, and

subjecting the first gaseous hydrocarbon to an electric field to create a plasma in the vessel, whereby at least a portion of the first gaseous hydrocarbon is converted to a second hydrocarbon having a second molecular weight.

2 . The method of claim 1 , wherein the second molecular weight is greater than the first molecular weight.

3 . The method of claim 2 , wherein the heavier hydrocarbon is a liquid hydrocarbon.

4 . The method of claim 1 , wherein the electric field is variable frequency electric field.

5 . The method of claim 4 , further comprising adjusting a frequency of the variable frequency electric field to adjust a rate of conversion of the first gaseous hydrocarbon to the second hydrocarbon.

6 . The method of claim 4 , further comprising:

measuring a characteristic of a product formed in the vessel, the product comprising the second hydrocarbon; and

adjusting a frequency of the variable frequency electric field in response to the measured characteristic.

7 . The method of claim 1 , further comprising subjecting the first gaseous hydrocarbon to a variable voltage electric field.

8 . The method of claim 7 , further comprising adjusting a voltage of the variable voltage electric field to adjust a rate of conversion of the first gaseous hydrocarbon to the second hydrocarbon.

9 . The method of claim 7 , further comprising:

measuring a characteristic of a product formed in the vessel, the product comprising the second hydrocarbon; and

adjusting a voltage of the variable voltage electric field in response to the measured characteristic.

10 . The method of claim 1 , further comprising subjecting the first gaseous hydrocarbon to a variable frequency and a variable voltage electric field.

11 . The method of claim 10 , further comprising adjusting a frequency and a voltage of the variable frequency and variable voltage electric field to adjust a rate of conversion of the first gaseous hydrocarbon to the second hydrocarbon.

12 . The method of claim 1 , further comprising introducing the first gaseous hydrocarbon introduced into the vessel at a controlled rate based on conversion of the first gaseous hydrocarbon to the second hydrocarbon.

13 . The method of claim 1 , wherein an amount of the first gaseous hydrocarbon introduced into the vessel is controlled based on a pressure within the vessel.

14 . The method of claim 1 , wherein the electric field is an oscillating electric field.

15 . The method of claim 14 , wherein the electric field oscillates at a frequency from 60 to 1000 Hz.

16 . The method of claim 1 , wherein the vessel comprises an electrode covered with an insulating material having dielectric properties.

17 . The method of claim 1 , further comprising applying an alternating current to one or more electrodes to form the electric field.

18 . A method for hydrocarbon conversion, comprising:

introducing a first gaseous hydrocarbon having a first molecular weight into a vessel, wherein the vessel is charged or grounded; and

subjecting the first gaseous hydrocarbon to an electric field to create a plasma in the vessel, whereby at least a portion of the first gaseous hydrocarbon is converted to a second hydrocarbon having a second molecular weight,

wherein the vessel comprises one or more powered electrodes and one or more grounded electrodes, wherein the vessel comprises a different number of powered electrodes than grounded electrodes.

19 . The method of claim 18 , further comprising:

subjecting the first gaseous hydrocarbon to a variable frequency and a variable voltage electric field;

measuring a characteristic of a product formed in the vessel, the product comprising the heavier hydrocarbon; and

adjusting a frequency or a voltage of the variable frequency and variable voltage electric field in response to the measured characteristic.