Method For Producing Lubricating Compositions, Industrial Degreasing Oily Additives For Fuels
OwnerDavid de Jasus Martucci Urdaneta, William J. Jimenez Cumareinventors
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Abstract
The invention relates to a method for producing lubricating compositions, oily corrosion-inhibiting industrial degreasers for oils and fuels, which are not degradable in the presence of oxygen, water, high temperatures and via contamination with particles, based on distilled and double-distilled fatty acids, a ternary compound, halogenated compounds, organic polymers, alcohols and mineral oil.
Claims17
1-16. (canceled)
Solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil, the ranges of concentrations of each compound are set forth in TABLE I below:
- TABLE I
- % P/P
- PERMISSIBLE
- COMPOUND
- CONCENTRATION
- LIMIT
- Halogented Compound
- 0.1%-37%
- 0.1% to 10% of
- the total mixture
- Mineral Oil
- —
- 0.1% to 10% of
- the total mixture
- Distilled Fatty Acids
- 5-35 Atoms
- 0.1% to 99% of
- the total mixture
- Di-Distillate Fatty Acids
- 5-35 Atoms
- 0.1% to 99% of
- the total mixture
- Organic polymers
- —
- 0.1% to 20% of
- the total mixture
- Ternary Compound
- 0.1%-90%
- 0.1% to 30% of
- the total mixture
- Aliphatic Alcohols
- —
- 0.1% to 30% of
- the total mixture
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compound, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that allow the preservation, by lubrication, of the mechanism systems of all equipment with mechanical gears and engines to gasoline, diesel, electric motors, petroleum liquefied gas motors and any motor and/or mechanical transmission operating under any other type of fuel or energy mechanism.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that have decomposition temperatures above 404° C. (760° F.) to adapt their rheological properties to operations of high temperatures.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I with freezing temperatures below −10° C. that adapt to the work of motors under winter temperatures.
Use of solutions that mix and fuse organic compositions based on distilled and di-distillated fatty acids, ternary compound, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I resistant to decomposition in environment is subsoil of high friction and temperatures present in drilling and fracturing operations of metal deposits, non-metallic deposits and in energetic deposits for extraction of oil and gas that have abound presence of sediments, high pressures, and high temperatures.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that can be used as corrosion inhibitors because they have the dual ability to inhibit corrosion, on the one hand, by oxidizing H2S and CO2 gases and on the other hand, for possessing a high absorption isothermal capacity that allows the formation of inhibitory film on the surface of lubricated metals which is seen, both in the 1A rating commonly observed in its exposures to copper strips under the ASTM-D130 method as well as in the reduction of reducing surface battery colonies present in congenite waters of deposits.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that allows to obtain lubricant oils of lower viscosity.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I with self-ignition point greater than 440° C. (824° F.).
Use of solutions that mix and fuse organic compositions based on distilled and di-distillate fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I capable of reducing the Coefficient of Friction (A) Metal-Metal and Metal—Rock of Deposits, thereby reducing wear from mechanical friction and increasing fuel savings.
Use of solutions that mix and fuse organic compositions based on distilled and di-distillated fatty acids, ternary compound, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that allow the obtaining of compositions that can be used for all oily additives with fuel quality improvement capacity by improving the cetane index, de-icing of the water content, improving combustion and reducing soot deposits derived from inadequate combustion which also impacts fuel savings and emissions reduction.
Use of solutions that mix and fuse organic compositions based on distilled and di-distillate fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I with surfactant capacity for the surfactant treatment of water used during the drilling and rock fracturing processes in metal mining, non-metallic and energy deposits.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that allow the obtaining of compositions that can be used as oily additives with capacity to improve quality of commercial lubricants for common use due to their antioxidative cacapity that slow down the aging and oxidation process by preventing the formation of acids, sludge and increases in viscosity derived from oxidation.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I that can achieve more than 240 M of metal-metal frictional force.
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, lcoholes and mineral oil described in TABLE I for use as lubricants that reduce emission a concentrations of:
- hydrocarbons (HC);
- carbon monoxide (CO) carbon dioxide (CO2) and nitrogen oxide (NOx).
Use of solutions that mix and fuse organic compositions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I which presents the characteristics of gravity and viscosity in the ranges indicated in the following TABLE II:
- TABLE II
- PARAMETERS
- Range
- Gravity Specifies
- 0.8000-0.8800
- API Severity—15.6° C. (60° F.)
- 33-48
- Dynamic Viscosity 15.6° C. (60° F.)
- 3-10 cSt
Use of solutions that mix and fuse organic compositions based on distilled and di-distilled fatty acids, ternary compounds, halogenated compounds, organic polymers, alcohols and mineral oil described in TABLE I, which is obtained by subjecting them to the pressure and temperature ranges indicated in the following TABLE III:
- TABLE III
- VARIABLES
- ALLOWABLE RANGE
- Temperature
- 5° C. (41° F.) to 200° C. (392° F.)
- Pressure (Psi)
- 0.1 Psi to 100 Psi
Dependencies are inferred from the claim text.