IP Library Granted Patent US 9,920,257
Granted Patent B2
US 9,920,257 · App. 15/150,132 · Granted Mar 20, 2018

Method and apparatus for making hybrid crude oils and fuels

Inventors: Robert Miller (Cashmere, WA); Delmar Guenther (Dallas, TX); Rick Lutterbach (Long Beach, IN); Jeff Nichols (Lewiston, ID)
Assignee: Clean Global Energy, Inc.
C10G9/36B01J19/2405B01J19/26C10G9/34C10G47/22C10G47/34C10G55/02C10L1/04B01J2219/24C10G2400/02C10G2400/04C10G2400/08
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 9,920,257
App. No.
15/150,132
Granted
Mar 20, 2018
Kind
B2
Abstract

A simplified process is provided for creating hybrid crude oils and hybrid crude fractions with characteristics superior to the original. The process uniquely combines gases with crude oil or crude fractions in an effervescent turbulent manner at low temperatures and pressures and without the further aid of catalysts. The process breaks large chain hydrocarbons into smaller chain hydrocarbons, molecularly combines carbon, hydrogen, and/or hydrocarbon molecules from the gases with and into hydrocarbon molecules of the crude or crude fraction, and separates contaminants and impurities.

Claims (14)

1. A method for molecularly combining gas molecules with liquid hydrocarbon molecules found in crude oil or crude fractions and separating asphaltenes, contaminants and impurities in the crude oil or crude fractions from lighter fractions of the crude oil or crude fractions, comprising:

combining one or more gases selected from methane, ethane, propane, butane, pentane, ethanol, methanol, nitrogen, carbon dioxide, carbon monoxide and hydrogen with a crude oil or crude fraction feedstock in the absence of catalysts and in a turbulent manner at temperatures between about 200 to 450° F. and low pressures within a self-contained network of raw material inflow and product outflow to create numerous localized high energy collisions of gas molecules with liquid hydrocarbon molecules and ongoing collisions of these molecules within a sustained turbulent environment;

using one or more nozzles, selected nozzle placements, and nozzle alignments to create the collisions within a processing vessel;

turbulently combining the one or more gases with the crude oil or crude fraction feedstock to force direct high energy collisions of the gas molecules with liquid hydrocarbon molecules in the crude oil or crude fraction feedstock, and to sustain an ongoing turbulent interaction of the gas molecules and the liquid hydrocarbon molecules as the gas molecules rise through the liquid hydrocarbon molecules;

generating a gaseous off-flow from a top of the crude oil or crude fraction feedstock that rises to a top of the processing vessel, the gaseous off-flow escaping via one or more outlets located at the processing vessel top;

drawing the gaseous off-flow through the outlets and into and through one or more heat exchangers in which gases of the gaseous off-flow are cooled;

as the gases of the gaseous off-flow cool, depositing portions thereof that condense to liquids into a product tank;

drawing the gases of the gaseous off-flow that do not condense in the cooling step out of the top of the product tank, channeling the gases of the gaseous off-flow that do not condense in the cooling step back into a first stage of the processing vessel, and combining the gases of the gaseous off-flow that do not condense in the cooling step with the crude oil or crude fraction feedstock; and

removing from the processing vessel asphaltenes, contaminates, and impurities.

2. The method of claim 1 , wherein the feedstock of the combining step has a temperature between 200 and 300° Fahrenheit.

3. The method of claim 1 , wherein the feedstock of the combining step has a temperature between 240 and 300° Fahrenheit.

4. The method of claim 1 , further comprising pumping the feedstock from the processing vessel to a heater to heat the feedstock and returning the heated feedstock to the processing vessel.

5. The method of claim 1 , wherein the low pressure ranges from 12 to 25 psi.

6. The method of claim 1 , wherein the crude fraction feedstock is asphaltene.

Assignments (2)
CHANGE OF NAME Recorded Nov 8, 2018
From: CLEAN GLOBAL ENERGY, INC.
To: CAPCO WORLDWIDE, INC.
Reel/Frame 047455/0961 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 20, 2016
From: MILLER, ROBERT; GUENTHER, DELMAR; LUTTERBACH, RICK; NICHOLS, JEFF
To: CLEAN GLOBAL ENERGY, INC.
Reel/Frame 039201/0375 →
Continuity (5)
Continuation 14614380 · Feb 4, 2015
Continuation 14220067 · Mar 19, 2014
Continuation 14070450 · Nov 1, 2013
Provisional Application 61848636 · Jan 7, 2013
Related Publication 20160251581A1 · Sep 1, 2016