IP Library Granted Patent US 9,359,562
Granted Patent B2
US 9,359,562 · App. 14/614,380 · Granted Jun 7, 2016

Method and apparatus for making hybrid crude oils and fuels

Inventors: Robert Miller (Lewiston, ID); Delmar Guenther (Dallas, TX); Rick Lutterbach (Long Beach, IN); Jeff Nichols (Lewiston, ID)
Assignee: CLEAN GLOBAL ENERGY, INC.
C10G55/02B01J19/2405B01J19/26C10G9/34C10G47/22C10G47/34C10L1/04B01J2219/24C10G2400/02C10G2400/04C10G2400/08
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Quick Facts
Patent No.
US 9,359,562
App. No.
14/614,380
Granted
Jun 7, 2016
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 (7)

1. A method for making hybrid crude oils and fuels, comprising:

breaking down liquid hydrocarbon molecules within a feedstock having a temperature range between 200 and 450° Fahrenheit into smaller chain hydrocarbon molecules by turbulently combining gas hydrocarbon molecules with said liquid hydrocarbon molecules, the smaller chain hydrocarbon molecules having a distillate temperature range between 99.39 to 570.02° Fahrenheit in the absence of catalysts;

after breaking down said liquid hydrocarbons within the feedstock, separating heaviest components from lighter fractions thereof;

separating a material portion of contaminants and impurities from the lighter fractions; and

separating a light fraction gaseous off-flow from the lighter fractions into separate commercial product-equivalent fractions, comprising any of: diesels, kerosenes, and gasolines.

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

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

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 (4)
Continuation 14220067 · Mar 19, 2014
Continuation 14070450 · Nov 1, 2013
Provisional Application 61848636 · Jan 7, 2013
Related Publication 20150152342A1 · Jun 4, 2015