US2231169A - Steam cylinder oil and process of preparing the same - Google Patents
Steam cylinder oil and process of preparing the same Download PDFInfo
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- US2231169A US2231169A US254504A US25450439A US2231169A US 2231169 A US2231169 A US 2231169A US 254504 A US254504 A US 254504A US 25450439 A US25450439 A US 25450439A US 2231169 A US2231169 A US 2231169A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M1/00—Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants
- C10M1/08—Liquid compositions essentially based on mineral lubricating oils or fatty oils; Their use as lubricants with additives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/10—Carboxylix acids; Neutral salts thereof
- C10M2207/12—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
- C10M2207/125—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of eight up to twenty-nine carbon atoms, i.e. fatty acids
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/10—Carboxylix acids; Neutral salts thereof
- C10M2207/12—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms
- C10M2207/129—Carboxylix acids; Neutral salts thereof having carboxyl groups bound to acyclic or cycloaliphatic carbon atoms having hydrocarbon chains of thirty or more carbon atoms
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2207/00—Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
- C10M2207/10—Carboxylix acids; Neutral salts thereof
- C10M2207/16—Naphthenic acids
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/04—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
- C10M2219/044—Sulfonic acids, Derivatives thereof, e.g. neutral salts
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/02—Groups 1 or 11
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/04—Groups 2 or 12
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/06—Groups 3 or 13
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/08—Groups 4 or 14
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/10—Groups 5 or 15
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/12—Groups 6 or 16
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/14—Group 7
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2010/00—Metal present as such or in compounds
- C10N2010/16—Groups 8, 9, or 10
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/135—Steam engines or turbines
Definitions
- This invention relates to the treatment of lubricating oil to insure stability under conditions of high temperatures and pressures in the presence of steam and has for a particular object 5 the preparation of a lubricating oil especially adapted to function in the cylinders of steam engines.
- Steam cylinder oils may not be supplied to the walls of the pistons and cylinders of the engine in many of the well-known forms of lubrication,
- Oils which have a tendency to emulsify with 30 steam are best suited for steam cylinder oils and heretofore it has been common practice to compound with a mineral oil a certain percentage of a fatty oil, such as tallow, which causes emulsification.
- a mineral oil a certain percentage of a fatty oil, such as tallow, which causes emulsification.
- Such fatty oil, or oils usually represent up to 8% to 10% of the mineral oil, but in addition to being costly, are decomposed at high temperatures which do not affect the mineral oil hydrocarbons, thus forming free fatty acids which attack metals under such temperature 40 conditions.
- This invention provides a way of insuring the stability of steam cylinder. oils while emulsifying the same under operating conditions, which is preferably accomplished in the following manner.
- a base stock for steam cylinder oils it is preferredto select a, lubricating oil which is composed mainly of saturated hydrocarbons, such oil, for example, being an asphaltic base, or mixed base, oil, which is highly refined by treatment with liquid sulphur dioxide, as in the wellknown Edeleanu process, to remove unsaturated hydrocarbons, aromatics, etc.
- saturated hydrocarbons such oil, for example, being an asphaltic base, or mixed base, oil, which is highly refined by treatment with liquid sulphur dioxide, as in the wellknown Edeleanu process, to remove unsaturated hydrocarbons, aromatics, etc.
- Such lubricating oil, thus treated shows the greatest stability under high heat conditions, but, of course, a body of saturated hydrocarbons may also be prepared by extensive sulphuric acid treatment, or even distilled from certain stocks, such as Pennsylvam'a crudes.
- oils of less saturated character can be stabilized by the processing method herein described.
- oils may include distillates from asphaltic or mixed base crudes, as well as lubricating oils obtained from such distillates by comparatively mild refining operations, such as the conventional acid treatment.
- a polyvalent metal soap as lime or magnesium soap, of an organic acid, such for example as oleic acid, stearic acid, palmitic acid, naphthenic acids, or sulphonicacid, the proportion of such added soap ranging from very small percentages of the oil, e.g., .01% to .1% up to the limit of solubility of said soap in said oil.
- the alkaline earth metal soaps do not form incrustatlons in service and When such soaps of a stable nature are 45' of these calcium and magnesium soaps are preferred for economical reasons.
- the soaps of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury may also be used.
- Any organic acid which will yield a polyvalent metal soap with suitable stabilizing properties is applicable to the process.
- Fatty acids for example, oleic, stearic, palmitic, and derivatives of the same, have been successfully employed. Of the fatty acids we prefer to use those of fourteen or more carbon atoms. Normally the more saturated acids, as stearic and palmitic, yield soaps which are less soluble in oil than the unsaturated acids, e. g., oleic, but a saturated acid of excellent solubility may be obtained through the hydrogenation of unsaturated acids of certain types.
- unsaturated acids from fish oil when hydrogenated yield acids which can be made into polyvalent metal soaps having superior oil solubility properties.
- the acids from fish oils may be obtained in large quantities by splitting the esters normally present therein.
- Polyvalent metal soaps of the hydrogenated acids derived as above described are soluble in oil up to 5 per cent by weight, and are very eflicient stabilizing agents.
- Sulphonic acid soaps are very soluble in oil. Acids of this type which have been found particularly suitable, may be derived from the sulphonation of to 200 seconds, Saybolt Universal F., oils of asphaltic origin, or raffinates derived therefrom by the well known Edeleanu treatment with liquid sulphur dioxide. Also from the extracted portion of the Edeleanu treatment aromatic type sulphonic acids may be prepared, from which suitable polyvalent alkaline earth or other metal aromatic sulphonic acid soaps can be made for the described purpose.
- Polyvalent metal soaps of the naphthenic acids are normally more oil soluble than those of the fatty acids, and are excellent stabilizing and emulsifying agents.
- those of calcium, magnesium, tin, and aluminum are preferred.
- the content of soaps dissolved in the oil may vary from a minute amount up to the limit of oil solubility.
- the following table is illustrative of the solubilities of the calcium soaps in the oil.
- the compounded oils possess a stringy structure, which for our purpose is undesirable.
- the preferred range for aluminum soaps is between 0.01% up to 1.0% by weight of the oil.
- solubility of the less soluble polyvalent metal soaps can be increased by the mixing therewith of a more soluble soap of polyvalent metals.
- solubility of calcium oleate can be tremendously increased by the simultaneous incorporation in the lubricant of a comparatively small percentage of a more soluble calcium or other polyvalent metal soap, such as calcium naphthenate or calcium sulphonate. This is a particularly important feature when it is desired to permanently incorporate in the oil soaps of relatively low solubility.
- the following table clearly illustrates this feature, and it should be noted that the solubility of calcium oleate in the same oil and under the-same conditions has been increased manyfold by the addition of a small percentage of a more soluble soap.
- such emulsifiable oil should contain a maximum quantity of the preferred soaps described herein.
- the novel feature of mixing two or more soaps is utilized when it is desired to increase the solubility of the more insoluble polyvalent metal soaps in oil over the maximum noted in Table I.
- Table I The following table is illustrative of the quantitles of polyvalent metal soaps normally added to the oil and the preferred range of soap content for the steam cylinder oils.
- soap results in a steam cylinder oil of unimpaired stability which emulsifles sufficiently to get the desired distribution, the soaps being easily combined with the saturated hydrocarbons, due to their oil solubility.
- a steam cylinder oil having the required emulsifying properties may be prepared from oils which result from the distillation of a suitable crude stock and which may be naturally composed mainly of saturated hydrocarbons.
- oils of Pennsylvania origin when traces of oxides, or'hydroxides, are added to the oil when heated, such oil develops the desired pronounced emulsifying properties.
- an organic acid or acids not normally present in petroleum may be added, and the requisite amount of polyvalent metal oxide or hydroxide, to accomplish substantial neutralization of the oils, applied.
- a preferred amount of polyvalent metal oxide or hydroxide, for example, magnesium oxide, or lime, or other alkaline earth oxide, or hydroxide, which may be added to such residual oil varies from 0.01% to 0.1%, and such is incorporated in the oil by intimate mixing at elevated temperatures, preferably about 300 F., and generally in excess of atmospheric temperatures.
- This oil may then be used as straight steam cylinder oil, or may be blended in amounts of from 10% to 20% with a body of a highly refined oil of high stability, such as the S02 treated oil previously described.
- the soaps may be added directly to the oil, during agitation either mechanically or with air, and the oil heated to 200-300 F.
- the preferred method is to first dissolve the desired quantity of organic acid in the oil and slowly add a metallic oxide or hydroxide, or the polyvalent metals previously cited, heating preferably to about 300;F., and generally in excess of atmospheric temperature, and agitating the mixture until neutralization of the free acid is substantially complete.
- the soap is more readily incorporated in the oil and excel-- lent distribution and dispersion of the soap in the oil is accomplished.
- This oil may be used as is,
- a steam cylinder oil to emulsify in the cylinders of steam engines to form water-in-oil emulsion which will be maintained in such cylinders consisting mainly of saturated hydrocar-- bons substantially free from organic acids and containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury, said percentage ranging upward from .0l% to- 0.1%, said steam cylinder oil being highly refined and stabilized by said metal naphthenate so as not to decompose in the presence of steam in a steam engine at usual pressures and temperatures as high as 500 F.
- the improvement which comprises commingling with the steam supplied to such cylinders, a hydrocarbon lubricating oil containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury, said percentages ranging upward from .01% to a percentage insufiicient to cause a substantial deposit or incrustation when the mixture of soap and oil is injected into the cylinder of a steam. engine.
- the improvement which comprises commingling with the steam supplied to such cylinders, a hydrocarbon lubricating oil containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium. manganese, iron, cobalt, nickel, tin, and mercury, said percentages ranging upward from .01% to 0.1%.
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- Oil, Petroleum & Natural Gas (AREA)
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- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Description
Patented Feb. 11, 1941 UNITED STATES PATENT OFFICE I STEAM CYLINDER OIL AND PROCESS OF PREPARING THE SAME No Drawing. Original application June 11, 1937,
Serial No. 147,784. Divided and this application February 3, 1939, Serial No. 254,504
5 Claims. (Cl. 252-35) This invention relates to the treatment of lubricating oil to insure stability under conditions of high temperatures and pressures in the presence of steam and has for a particular object 5 the preparation of a lubricating oil especially adapted to function in the cylinders of steam engines.
In the manufacture of steam cylinder oils certain specifications must be strictly adhered 1 to because of operating conditions peculiar to the uses of such oils.
Steam cylinder oils may not be supplied to the walls of the pistons and cylinders of the engine in many of the well-known forms of lubrication,
15 but are introduced to the cylinder with the steam in such fashion that they are fine divided by atomization, whereby they are spread evenly over the moving parts.
In the modern steam engine practice the tem- 20 perature of the steam in the cylinder of the engine when closed by the piston goes as high as 500 under its corresponding pressure, and under such conditions it is highly important not only that a proper distribution of the oil is assured, but also that the stability of the oil is such as to resist decomposition, whereby undesirable deposits, such as coke, and the like, are eliminated.
Oils which have a tendency to emulsify with 30 steam are best suited for steam cylinder oils and heretofore it has been common practice to compound with a mineral oil a certain percentage of a fatty oil, such as tallow, which causes emulsification. Such fatty oil, or oils, usually represent up to 8% to 10% of the mineral oil, but in addition to being costly, are decomposed at high temperatures which do not affect the mineral oil hydrocarbons, thus forming free fatty acids which attack metals under such temperature 40 conditions.
' The problems of steam cylinder lubrication are thus inherently different from the problems of lubricating the cylinders of internal combustion engines, due to operating conditions at high temperatures and pressures in the presenceof water vapor, which factors require that the cylinders be preferentially wet with the oil rather than with the water.
For this reason, high viscosity oils have been 5 found best suited for steam cylinder lubrication and such oils should be processed for emulsification with the steam used in order to provide the desired preferential wetting of the cylinder with oil.
5 Although high viscosity oils are generally applicable to steam cylinder lubrication, this factor is not necessarily limiting as the invention involves the preparation of an oil which will provide adequate lubrication while possessing an inherent quality of stability under severe condi- 5 tions of high temperature and in the presence of steam.
This invention provides a way of insuring the stability of steam cylinder. oils while emulsifying the same under operating conditions, which is preferably accomplished in the following manner.
As a base stock for steam cylinder oils it is preferredto select a, lubricating oil which is composed mainly of saturated hydrocarbons, such oil, for example, being an asphaltic base, or mixed base, oil, which is highly refined by treatment with liquid sulphur dioxide, as in the wellknown Edeleanu process, to remove unsaturated hydrocarbons, aromatics, etc. Such lubricating oil, thus treated shows the greatest stability under high heat conditions, but, of course, a body of saturated hydrocarbons may also be prepared by extensive sulphuric acid treatment, or even distilled from certain stocks, such as Pennsylvam'a crudes.
It has been found, however, that certain oils of less saturated character can be stabilized by the processing method herein described. Such oils may include distillates from asphaltic or mixed base crudes, as well as lubricating oils obtained from such distillates by comparatively mild refining operations, such as the conventional acid treatment.
To the base lubricating oil is added a polyvalent metal soap, as lime or magnesium soap, of an organic acid, such for example as oleic acid, stearic acid, palmitic acid, naphthenic acids, or sulphonicacid, the proportion of such added soap ranging from very small percentages of the oil, e.g., .01% to .1% up to the limit of solubility of said soap in said oil..
The alkaline earth metals, calcium, strontium, barium, and magnesium, yield soaps with organic acids which exhibit suitable stabilizing qualifications. added to oils, the resistance of the lubricant to decomposition, particularly under the high temperatures encountered in steam cylinder lubrication and other services, is greatly improved, and as a feature necessary for steam cylinder lubrication we again emphasize the necessity of a stable compounded lubricant as heretofore out-1 lined.
We have found that the alkaline earth metal soaps do not form incrustatlons in service and When such soaps of a stable nature are 45' of these calcium and magnesium soaps are preferred for economical reasons. However, the soaps of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury, may also be used.
Any organic acid which will yield a polyvalent metal soap with suitable stabilizing properties, is applicable to the process. Fatty acids, for example, oleic, stearic, palmitic, and derivatives of the same, have been successfully employed. Of the fatty acids we prefer to use those of fourteen or more carbon atoms. Normally the more saturated acids, as stearic and palmitic, yield soaps which are less soluble in oil than the unsaturated acids, e. g., oleic, but a saturated acid of excellent solubility may be obtained through the hydrogenation of unsaturated acids of certain types. To illustrate; unsaturated acids from fish oil when hydrogenated, yield acids which can be made into polyvalent metal soaps having superior oil solubility properties. The acids from fish oils may be obtained in large quantities by splitting the esters normally present therein.
Polyvalent metal soaps of the hydrogenated acids derived as above described are soluble in oil up to 5 per cent by weight, and are very eflicient stabilizing agents.
Sulphonic acid soaps are very soluble in oil. Acids of this type which have been found particularly suitable, may be derived from the sulphonation of to 200 seconds, Saybolt Universal F., oils of asphaltic origin, or raffinates derived therefrom by the well known Edeleanu treatment with liquid sulphur dioxide. Also from the extracted portion of the Edeleanu treatment aromatic type sulphonic acids may be prepared, from which suitable polyvalent alkaline earth or other metal aromatic sulphonic acid soaps can be made for the described purpose.
Polyvalent metal soaps of the naphthenic acids are normally more oil soluble than those of the fatty acids, and are excellent stabilizing and emulsifying agents. Of the naphthenates those of calcium, magnesium, tin, and aluminum are preferred.
Depending largely on the degree of emulsification and the stabilizing influence desired, the content of soaps dissolved in the oil may vary from a minute amount up to the limit of oil solubility. The following table is illustrative of the solubilities of the calcium soaps in the oil.
Table I Solubility in Solubility in parafiine oils of asphaloils tic origin Calcium sulphonate 507 or more... 50 7 or more. Calcium naphthenate-- 4%;nax 107: max. Calcium oleate 0.5% max. i 1% max. Calcium steal-ate 0.2% max. 0.4% max. Calcium palmitate 0.1% max- 0.3% max.
ever, when added in. percentages in excess of" about 2%, the compounded oils possess a stringy structure, which for our purpose is undesirable. The preferred range for aluminum soaps is between 0.01% up to 1.0% by weight of the oil.
In the preparation of lubricants we have also found that the solubility of the less soluble polyvalent metal soaps can be increased by the mixing therewith of a more soluble soap of polyvalent metals. For example, the solubility of calcium oleate can be tremendously increased by the simultaneous incorporation in the lubricant of a comparatively small percentage of a more soluble calcium or other polyvalent metal soap, such as calcium naphthenate or calcium sulphonate. This is a particularly important feature when it is desired to permanently incorporate in the oil soaps of relatively low solubility. The following table clearly illustrates this feature, and it should be noted that the solubility of calcium oleate in the same oil and under the-same conditions has been increased manyfold by the addition of a small percentage of a more soluble soap.
TABLE II Solubility of calcium oleate in California lubricating oil Per cent Calcium olea 1.0
Calcium oleate+l0% calcium naphthenate 2.5 Calcium oleate+20% calcium naphthenate 4.0 Calcium oleate+30% calcium naphthenate 7.0
lution of soaps be incorporated in the oil.
Therefore, in order to increase the total soap content for this or other possible lubrication purposes, it has been found advantageous to utilize stable soaps made from a mixture'of acids.
In order to provide the maximum stability to resist the high temperature conditions encountered, and still provide enough soap for proper lubrication in conjunction with steam or otherwise, such emulsifiable oil should contain a maximum quantity of the preferred soaps described herein.
The novel feature of mixing two or more soaps is utilized when it is desired to increase the solubility of the more insoluble polyvalent metal soaps in oil over the maximum noted in Table I. The following table is illustrative of the quantitles of polyvalent metal soaps normally added to the oil and the preferred range of soap content for the steam cylinder oils.
Table III Sulphonates N aphthenates l tes It is important in the application of the a ove ranges of soap content to lubricants to add just sufiicient soap to give the desired stabilization properties. In steam cylinder oils the addition is such as to give the desired emulsifying properties and prevent the formation of incrustations or deposits on the cylinder walls of the lubricated mechanism. In general the addition is so small that the amount of ash arising from its use as an emulsifier is too small to be determined analytically.
The use of soap results in a steam cylinder oil of unimpaired stability which emulsifles sufficiently to get the desired distribution, the soaps being easily combined with the saturated hydrocarbons, due to their oil solubility.
Likewise, a steam cylinder oil having the required emulsifying properties may be prepared from oils which result from the distillation of a suitable crude stock and which may be naturally composed mainly of saturated hydrocarbons.
For instance, residual oils of Pennsylvania origin when traces of oxides, or'hydroxides, are added to the oil when heated, such oil develops the desired pronounced emulsifying properties. To such oils, an organic acid or acids not normally present in petroleum may be added, and the requisite amount of polyvalent metal oxide or hydroxide, to accomplish substantial neutralization of the oils, applied.
A preferred amount of polyvalent metal oxide or hydroxide, for example, magnesium oxide, or lime, or other alkaline earth oxide, or hydroxide, which may be added to such residual oil varies from 0.01% to 0.1%, and such is incorporated in the oil by intimate mixing at elevated temperatures, preferably about 300 F., and generally in excess of atmospheric temperatures. This oil may then be used as straight steam cylinder oil, or may be blended in amounts of from 10% to 20% with a body of a highly refined oil of high stability, such as the S02 treated oil previously described.
The soaps may be added directly to the oil, during agitation either mechanically or with air, and the oil heated to 200-300 F. The preferred method however, is to first dissolve the desired quantity of organic acid in the oil and slowly add a metallic oxide or hydroxide, or the polyvalent metals previously cited, heating preferably to about 300;F., and generally in excess of atmospheric temperature, and agitating the mixture until neutralization of the free acid is substantially complete. In such manner the soap is more readily incorporated in the oil and excel-- lent distribution and dispersion of the soap in the oil is accomplished. When prepared in this manner with excess quantities of acid and oxide the quantity of the soap which is retained in the oil represents the maximum of solubility. This oil may be used as is,
or blended in. amounts from 10% to 50% with additional quantities of suitable base oils.
While it is unnecessary, the use of small amounts of an acidless fatty oil with the steam cylinder oils prepared as above described, has sometimes a beneficial efiect in lowering the surface tension, but the quantity used, from 0% to 3%, is kept as low as possible andin any event is far less than the amount normally used in compounding steam cylinder oils.
This application is a division of our copending application Serial Number 147,784 filed June 11, 1937 which is a continuation in part of our copending applications, now Patents Nos. 2,084,5312, dated June 22, 1937.
We claim:
1. A steam cylinder oil to emulsify in the cylinders of steam engines to form water-in-oil emulsion which will be maintained in such cylinders consisting mainly of saturated hydrocar-- bons substantially free from organic acids and containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury, said percentage ranging upward from .0l% to- 0.1%, said steam cylinder oil being highly refined and stabilized by said metal naphthenate so as not to decompose in the presence of steam in a steam engine at usual pressures and temperatures as high as 500 F.
2. A steam cylinder oil according to claim 1 in which the naphthenate is aluminum naphthenate.
3. A steam cylinder oil according to claim 1 in which the'naphthenate is tin naphthenate.
4. In the lubrication of the cylinders'of steam engines, the improvement which comprises commingling with the steam supplied to such cylinders, a hydrocarbon lubricating oil containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium, manganese, iron, cobalt, nickel, tin and mercury, said percentages ranging upward from .01% to a percentage insufiicient to cause a substantial deposit or incrustation when the mixture of soap and oil is injected into the cylinder of a steam. engine.
5. In the lubrication of the cylinders of steam engines, the improvement which comprises commingling with the steam supplied to such cylinders, a hydrocarbon lubricating oil containing a percentage of a naphthenate of a metal of the group consisting of cadmium, aluminum, zinc, lead, copper, chromium. manganese, iron, cobalt, nickel, tin, and mercury, said percentages ranging upward from .01% to 0.1%.
ARTHUR LAZAR. JOSEPH V. CRENNA.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US254310A US2231168A (en) | 1937-06-11 | 1939-02-02 | Steam cylinder oil and process of preparing the same |
| US254504A US2231169A (en) | 1937-06-11 | 1939-02-03 | Steam cylinder oil and process of preparing the same |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US147784A US2231167A (en) | 1937-06-11 | 1937-06-11 | Steam cylinder oil and process of preparing the same |
| US254310A US2231168A (en) | 1937-06-11 | 1939-02-02 | Steam cylinder oil and process of preparing the same |
| US254504A US2231169A (en) | 1937-06-11 | 1939-02-03 | Steam cylinder oil and process of preparing the same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2231169A true US2231169A (en) | 1941-02-11 |
Family
ID=27386597
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US254310A Expired - Lifetime US2231168A (en) | 1937-06-11 | 1939-02-02 | Steam cylinder oil and process of preparing the same |
| US254504A Expired - Lifetime US2231169A (en) | 1937-06-11 | 1939-02-03 | Steam cylinder oil and process of preparing the same |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US254310A Expired - Lifetime US2231168A (en) | 1937-06-11 | 1939-02-02 | Steam cylinder oil and process of preparing the same |
Country Status (1)
| Country | Link |
|---|---|
| US (2) | US2231168A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4778611A (en) * | 1985-05-02 | 1988-10-18 | Herbert Bishop | Oil additive process |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB641694A (en) * | 1948-02-10 | 1950-08-16 | Shell Refining & Marketing Co | Improvements in or relating to lubricating compositions |
| US2640811A (en) * | 1951-03-26 | 1953-06-02 | Standard Oil Co | Demulsifiable lubricant compositions |
| DE972052C (en) * | 1953-11-24 | 1959-07-23 | Bataafsche Petroleum | Cylinder lubricant for internal combustion engines operated with sulfur-containing fuels with a sulfur content of at least 0.01 to over 5 percent by weight |
| US2820007A (en) * | 1953-11-24 | 1958-01-14 | Shell Dev | Lubricating compositions |
| US3071546A (en) * | 1958-09-26 | 1963-01-01 | Emery Industries Inc | Lubricant composition |
-
1939
- 1939-02-02 US US254310A patent/US2231168A/en not_active Expired - Lifetime
- 1939-02-03 US US254504A patent/US2231169A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4778611A (en) * | 1985-05-02 | 1988-10-18 | Herbert Bishop | Oil additive process |
Also Published As
| Publication number | Publication date |
|---|---|
| US2231168A (en) | 1941-02-11 |
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