Cerium dioxide nanoparticle-containing fuel additive

a fuel additive and nanoparticle technology, applied in the field of fuel additive reversemicellar compositions, can solve the problems of increasing engine wear, diesel engines often develop carbon deposits on the walls of their cylinders, and incomplete combustion and exhaust smoke, and achieve the effect of improving engine power during fuel combustion

Inactive Publication Date: 2010-08-12
CERION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0084]The present invention is directed to a fuel additive composition that comprises: a) a reverse micellar composition comprising an aqueous disperse phase that includes stabilized, non-agglomerated cerium dioxide nanoparticles in a continuous phase comprising a hydrocarbon liquid, a surfactant, and optionally a co-surfactant; and b) a reverse micellar composition comprising an aqueous disperse phase that includes a cetane improver effective for improving engine power during fuel combustion.

Problems solved by technology

On the other hand, too high cetane fuels can result in incomplete combustion and exhaust smoke due to too brief of an ignition delay which does not allow proper mixing of the fuel and air.
During the normal course of operation, diesel engines often develop carbon deposits on the walls of their cylinders due to incomplete combustion of fuel.
These deposits can increase engine wear and, because of friction induced by the deposits, decrease engine efficiency.
Incomplete fuel combustion can also lead to the environmentally harmful emission of particulate materials, also referred to as soot.
The maintenance concentration is effective to maintain the catalytic iron oxide layer on the combustion surfaces but insufficient to decrease timing delay in the engine.
However, this method may accelerate the aging of the engine by formation of rust.
However, fuel additives of this type, in addition to using the rare and expensive metals such as platinum, can require several months before the engine is “conditioned”.
Vehicle on-board dosing systems that dispense cerium dioxide into the fuel before it enters the engine are known, but such systems are complicated and require extensive electronic control to feed the appropriate amount of additive to the fuel.
The resulting high water content can lead to a loss in engine power and lower fuel economy.
However, current methods do not allow the economical and facile preparation of cerium nanoparticles in a short period of time at very high suspension densities (greater than 0.5 molal, i.e., 9 wt.
Cerium dioxide particles prepared using this type of mixing are often too large to be useful for certain applications.
Addition of reactants, such as cerium nitrate, an oxidant, and hydroxide ion, can result in the formation of nanoparticles.
This nucleation and growth process is not desirable if one wishes to limit the final size of the particles while still maintaining a high particle suspension density.
Such a batch reactor is not useful for producing a high yield (greater than 1 molal) of cerium dioxide nanoparticles that are very small, for example, less than 10 nm in a reasonably short reaction time (for example, less than 60 minutes).
Colloid mills are not useful for reducing the particle size of large cerium dioxide particles because the particles are too hard to be sheared by the mill in a reasonable amount of time.
This is a time consuming, expensive process that invariably produces a wide distribution of particle sizes.
Most stabilizers used to prevent agglomeration in an aqueous environment are ill suited to the task of stabilization in a nonpolar environment.
When placed in a nonpolar solvent, such particles tend to immediately agglomerate and, consequently, lose some, if not all, of their desirable nanoparticulate properties.
Changing stabilizers can involve a difficult displacement reaction or separate, tedious isolation-redispersal methods (for example, precipitation and subsequent redispersal with the new stabilizer using ball milling).
As there was no attendant measurement of engine power, the claimed 85-90% reductions in particulate emissions may have been an artifact of the loss of engine power and thus been an unacceptable trade-off of power for emissions reduction.
These types of fuel additives also have a long conditioning period.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

Preparation of Cerium Dioxide Nanoparticles: Single Jet Addition

[0236]To a 3 liter round bottom stainless steel reactor vessel was added 1.267 liters of distilled water, followed by 100 ml of Ce(NO3)3.6H2O solution (600 gm / liter Ce(NO3)3.6H2O). The solution was clear and has a pH of 4.2 at 20° C. Subsequently, 30.5 gm of 2-[2-(2-methoxyethoxy)ethoxy]acetic acid (MEEA) was added to the reactor vessel. The solution remained clear, and the pH was 2.8 at 20° C. A high sheer mixer was lowered into the reactor vessel, and the mixer head was positioned slightly above the bottom of the reactor vessel. The mixer was a colloid mill manufactured by Silverson Machines, Inc., modified to enable reactants to be introduced directly into the mixer blades by way of a peristaltic tubing pump. The mixer was set to 5,000 rpm, and 8.0 gm of 30% H2O2 was added to the reactor vessel. Then 16 ml of 28%-30% NH4OH, diluted to 40 ml, was pumped into the reactor vessel by way of the mixer head in about 12 seco...

examples 1a-f

Evaluation of Alternative Stabilizers to MEEA

[0241]Example 1 was repeated, except that in Example 1a an equivalent molar amount of succinic acid was substituted for the MEEA stabilizer. A brown precipitate that readily settled was obtained, which is an indication of very large particles (several tens of microns), The same experiment was repeated each time substituting an alternative stabilizer (malonic acid—Example 1b, glycerol—Example 1c, ethyl acetoacetate—Example 1d). In each case, a readily settling brown precipitate was obtained, indicating the failure to obtain nanoparticles. For Example 1e, lactic acid at twice the molar concentration was substituted for the MEEA stabilizer. Quasi-inelastic dynamic light scattering measurements revealed a mean hydrodynamic diameter particle size of 5.4 nm when the hydroxide was doubled, and 5.7 nm when the hydroxide was increased by 75%. Mixtures of EDTA (which by itself produces no particles) and lactic acid at a ratio of about 20% / 80% also ...

example 2

CeO2 Precipitation with EDTA / Lactic Acid Stabilizer—Effect of Mixing

[0242]To a 3 liter round bottom stainless steel reactor vessel was added 76.44 gm EDTA disodium salt in distilled water to a total weight of 1000 gm, 74.04 gm of DL-lactic Acid (85%), 240.0 gm of Ce(NO3)3.6H2O in 220 gm of distilled water and 19.2 gm of 50% H2O2 aqueous solution. As in Example 1, the mixer speed was set to 5000 rpm, and the contents of the reactor were brought to a temperature of 22° C. Separately, a solution of 128.0 gm NH4OH (28-30%) was prepared. This quantity of hydroxide is equivalent to twice the number of moles of cerium solution, so the initially nucleated precipitate was presumably the bis-hydroxyl intermediate. In one experiment, the ammonium hydroxide solution was single jetted into the reactor in the reaction zone defined by the mixer blades and perforated screen. In another experiment, the hydroxide was added via a single jet just subsurface into the reactor in a position remote from th...

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Abstract

A fuel additive composition includes: a) a reverse-micellar composition having an aqueous disperse phase that includes cerium dioxide nanoparticles in a continuous phase that includes a hydrocarbon liquid, a surfactant, and optionally a co-surfactant and b) a reverse micellar composition having an aqueous disperse phase that includes a cetane improver effective for improving engine power during fuel combustion. A method of making a cerium-containing fuel additive includes the steps of: a) providing a mixture of a nonpolar solvent, a surfactant, and a co-surfactant; and b) combining the mixture with an aqueous suspension of stabilized cerium dioxide nanoparticles.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS [0001]This application claims the benefit of priority from: U.S. Provisional Application Ser. No. 60 / 824,514, CERIUM-CONTAINING FUEL ADDITIVE, filed Sep. 5, 2006; U.S. Provisional Application Ser. No. 60 / 911,159, REVERSE MICELLAR FUEL ADDITIVE COMPOSITION, filed Apr. 11, 2007; and U.S. Provisional Application Ser. No. 60 / 938,314, REVERSE MICELLAR FUEL ADDITIVE COMPOSITION, filed May 16, 2007, the disclosures of which are incorporated herein by reference.FIELD OF THE INVENTION [0002]The present invention relates to fuel additives and, in particular, to fuel additive reverse-micellar compositions that preferably include cerium dioxide nanoparticles.BACKGROUND OF THE INVENTION[0003]Diesel fuel ranks second only to gasoline as a fuel for internal combustion engines. Trucks, buses, tractors, locomotives, ships, power generators, etc. are examples of devices that use diesel fuel. Passenger cars and sport utility vehicles are another area of potentia...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10L1/12B01F23/00C01F17/235C09K23/00
CPCB01F3/0807Y02T50/678B01J13/0047B01J13/0086B82Y30/00C10L1/10C10L1/103C10L1/1233C10L1/125C10L1/1258C10L1/1608C10L1/1616C10L1/1811C10L1/1824C10L1/1881C10L1/1883C10L1/19C10L1/1985C10L1/2222C10L1/2437C10L10/02C10L10/08C10L10/12C10M2201/062C10N2230/06C10N2240/10B01F7/164B01J23/10C10N2210/03C10N2220/082C01P2002/72C01P2004/04C01P2004/52C01P2004/64C10N2030/06C10N2040/25C01F17/235B01F23/41B01F27/812C10N2010/06C10N2020/06
Inventor REED, KENNETH
Owner CERION
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