US2022243140A1PendingUtilityA1

Method For Producing Lubricating Compositions, Industrial Degreasing Oily Additives For Fuels

Assignee: URDANETA DAVID DE JASUS MARTUCCIPriority: Nov 1, 2018Filed: Nov 1, 2018Published: Aug 4, 2022
Est. expiryNov 1, 2038(~12.3 yrs left)· nominal 20-yr term from priority
C10N 2030/04C10M 2207/1253C10M 2207/125C10N 2040/04C10M 171/00C10N 2040/25C10N 2020/017C10M 2207/0215C10N 2030/02C10M 2207/021C10N 2030/54C10N 2030/06C10M 2203/102C10M 111/04C10M 2211/00C10N 2030/22C10N 2030/12C10M 2211/003C10N 2030/50C10N 2030/10C10M 105/22C10M 105/50
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Claims

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.

Claims

exact text as granted — not AI-modified
1 - 16 . (canceled) 
     
     
         17 . 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 
                 
                     
                 
             
                
                
                
                
                
               
               
                
                
                
                
                
                
                
                
                
                
                
                
                
                
                
               
            
           
         
       
     
     
         18 . 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. 
     
     
         19 . 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. 
     
     
         20 . 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. 
     
     
         21 . 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. 
     
     
         22 . 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 CO 2  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. 
     
     
         23 . 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. 
     
     
         24 . 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.). 
     
     
         25 . 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. 
     
     
         26 . 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. 
     
     
         27 . 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. 
     
     
         28 . 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. 
     
     
         29 . 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. 
     
     
         30 . 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). 
     
     
         31 . 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 
                 
                     
                 
             
                
                
                
                
               
               
                
                
                
                
               
            
           
         
       
     
     
         32 . 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

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