US3146079A - Fuel oil composition - Google Patents
Fuel oil composition Download PDFInfo
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- US3146079A US3146079A US55731A US5573160A US3146079A US 3146079 A US3146079 A US 3146079A US 55731 A US55731 A US 55731A US 5573160 A US5573160 A US 5573160A US 3146079 A US3146079 A US 3146079A
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- fuel oil
- oil
- corrosion
- fuel
- oil composition
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
- C10L1/224—Amides; Imides carboxylic acid amides, imides
Definitions
- This invention relates to novel corrosion and/or rust inhibitors particularly adapted for use in preventing corrosion of metals especially iron, steel and ferrous alloys by liquids containing corrosive compounds such as, for example, petroleum fuel oil and to the method of preventing such corrosion.
- the corrosion inhibitor is an imide prepared by reacting propylene diamine with polybasic aromatic acid.
- the corrosion inhibitor of the present invention is an imide represented by the formula C coon NCH2CH2 2N placed in a reactor.
- R is C1248 alkyl radical and R is a member of the group consisting of H and a C alkyl radical.
- the alkyl groups of the above formula are preferably hydrocarbon alkyl groups.
- the preferable hydrocarbon groups are those groups having from about 12 carbon atoms to about 18 carbon atoms such as, for example, those derived from higher fatty acids, e.g., lauryl, oleyl, linoleyl, tallow, soybean, coco, stearyl, palmityl, myristyl and the like.
- the corrosion inhibitors of this invention may be used to form a fuel oil composition containing a major proportion of a distillate fuel oil and a small or minor amount of the corrosion inhibitor.
- Such distillate fuel oil compositions may comprise a distillate fuel oil containing from about 0.0001 to about 5 weight percent and preferably from about 0.0001 to about 0.05 weight percent of the corrosion inhibitor.
- the corrosion inhibitor may also be formulated as an addition agent concentrate in a suitable organic solvent as more particularly described below. This concentrate may be used by further dilution with the distillate fuel oil to form the distillate fuel oil composition.
- the corrosion inhibitors of the present invention are advantageously oil-soluble.
- the corrosion inhibitors of this present invention may be prepared by reacting the corresponding propylene diamine in the presence of inert solvent with polybasic aromatic acid.
- the reaction may be carried out in the presence of a solvent such as benzene, ethanol, n-butanol, isobutanol, xylene, etc.
- a acceptable temperature for the reaction may be in the range of from about F. to about 200 F. although higher or lower temperatures may be used.
- PROCEDURE A A mixture of 5.94 g. of N,N ditallow 1,3 propylene diamine, 1.92 g. of trimellitic anhydride, and 50 ml. of xylene were placed in a reactor. The reactor was heated to the reflux temperature of Xylene and maintained at this temperature for a period of 8 hours after which 0.20 ml. of water was recovered. A total of 6.5 g. of product having the following formula was recovered:
- PROCEDURE B A mixture of 20 g. of N-tallow 1,3-propylene diamine, 9.6 g. of trimellitic anhydride, and 250 ml. of Xylene were The reactor was heated to the reflux temperature of xylene after which 0.90 ml. of water was recovered. A total of 29 g. of product having the following formula was recovered:
- corrosion inhibitors defined herein such as those prepared as described above as well as those set forth in the above examples are usable in minor amounts from about 0.0001 to about 5 weight percent and preferably from about 0.001 to about 0.05 weight percent in distillate fuel oils.
- the distillate fuel oil may belvirgin or cracked petroleum distillate fuel oil. 'The fuel oil may boil in the range of from about 200 to about 750 F., and preferably in the range of 350 to 650 F.
- the distillate fuel oil may contain or consist of cracked-components such as, for example, those derived from cycle oils or cycle oil cuts boiling heavier than gasoline, usually in the range of from about 450 to 750 F. and may be derived by catalytic or thermal cracking.
- the distillate oil may contain other components such as addition agents used for a particular function such as, for example, pour point depressants, combustion improvers, or the like.
- the distillate fuel oil is preferably a heating oil in which the corrosion inhibitors of this invention are used in accordance herewith.
- These oils are intended for use by burning to obtain heat such as is intended for furnace or heater fuel use as opposed to internal combustion engine fuel wherein the explosiveness of the fuel in a combustion chamber is of prime importance.
- Examples of such heating oils are a heavy industrial residual fuel (e.g.,-Bunker C), a heater oil fraction, a gas oil, a furnace oil, kerosene, or any other light oil intended for furnace or heater fuel use.
- INDIANA CONDUCTOMETRIC TEST This test, which quantitatively measures corrosion rates, depends upon the measurement of the change in electrical resistance of a steel test strip immersed in the corrosive medium. The change in resistance is simply related to the decrease in the thickness of the test specimen caused by corrosion.
- specimen holders are designed to make electrical connections to two steel strips suspended in large glass test tubes. A mixture is prepared using six parts of hydrocarbon oil containing the rust inhibitor and four parts double distilled water. The corrosion test strips are first immersed in the oil containing the rust inhibitor for a period of one-half hour and subsequently suspended in the mixture such that approximately one-half of the specimen is above the oil-water interface and the remaining half of the specimen is below the oil-water interface.
- the strips are maintained in the mixture for a period of 24 hours at a temperature of 25 C.
- the corrosion rates are calculated on a quantative basis from the observed change in electrical resistance comparing the specimen from the inhibited mixture with a specimen run under the same conditions in an uninhibited mixture.
- the corrosion inhibitors of the present invention may, for convenience, be prepared as an addition agent concentrate. Accordingly, the corrosion inhibitor is prepared in or dissolved in a suitable organic solvent therefor in amounts greater than 10% and preferably from'about 25% to about 65%.
- the solvent, in such concentrate may conveniently be present in amounts of from about 35% to about 75%.
- the organic solvent preferably boils within the range of from about 100 F. to about 700 F.
- the organic solvents may advantageously be hydrocarbon solvents, for example, petroleum, petroleum fractions, such as naphtha, heater oil, mineral spirits and the like, because of their clean burning properties.
- the solvents selected should, of course, be selected with regards to beneficial or adverse effects it may have on the ultimate fuel oil compo- I sition.
- the solvent should preferably burn with- 'out leaving a residue and should be non-corrosive with regard to metal, and especially ferrous metals.
- Other desirable properties are obvious from the intended use of the solvent.
- coco, soybeans, tallow, and the like as used herein denote that the group so identified is derive/1 from a particular source.
- the coco groups are derived from mixtures of coco fatty acids; the soybean groups are derived from soybean fatty acids; the tallow groups are derived from tallow fatty acids.
- coco, soybean and tallow fatty acids are derived from coconut, soybean and tallow oils and are marketed commercially.
- Each such group is usually a mixture of carbon chains differing slightly in length and/or configuration.
- the tallow groups are a mixture of C to C groups predominating in stearyl and palmityl groups.
- a distillate fuel oil composition comprising a major proportion of a hydrocarbon oil fraction in the fuel oil wherein R is a C1248 alkyl radical and R is a member of the group consisting of H and a C alkyl radical.
- a corrosion inhibitor concentrate for use in a distillate fuel oil comprising from about 35% to about 75% by weight of an organic solvent and from about 25% to 5 6 about 65% by weight of an imide having the formula 4.
- a fuel oil composition comprising a major proportion of a hydrocarbon oil fraction in the fuel oil disstillation range and from about 0.0001 to about 5.0%
- a fuel oil composition comprising a major proh R C k 1 a1 d R portion of a hydrocarbon oil fraction in the fuel oil dis- W erem 1s a a1 Ia 1C an 1 1S ydmgen tillation range and from about 0.0001 to about 5.0% by 15 References Clted 111 the file of thls Patent Weight of an imide having the formula UNITED STATES PATENTS 0 1,908,705 Jaeger May 16, 1933 ll 2,604,451 Rocchini July 22, 1952 R 2,699,427 Smith et a1 Jan. 11, 1955 COOH 2,816,897 Wolf Dec. 17, 1957 H 3,056,832 Stromberg Oct.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Lubricants (AREA)
Description
3,145,079 FUEL GIL CGIViPOfiTHBN John H. Udelhofen, Cahiniet City, TIL, assignor to Satandard ()il Company, Chicago, EL, a corporation of Indiana No Drawing. Filed Sept. 13, 1960, Ser. No. 55,731 4 Claims. (Ci. 44-63) This invention relates to novel corrosion and/or rust inhibitors particularly adapted for use in preventing corrosion of metals especially iron, steel and ferrous alloys by liquids containing corrosive compounds such as, for example, petroleum fuel oil and to the method of preventing such corrosion.
The rusting of steel used in the transportation and storage of petroleum fuel oils has always presented a serious problem. The presence of sediment and rust as a result of corrosion and the carry-over of the sediment into the fuel burning installations presents a serious operating problem. In addition to the possibility of storage tank rusting through with the consequent loss of fuel oil, there is the additional danger that the furnace filters and failure of the heating system.
The problem of corrosion or rusting is associated with the presence of moisture in the oil products caused by entrainment, condensation and solution. In most cases, the problem is accentuated by the presence of a separate water phase. Thus, in the storage and bulk shipment of fuel oil, it is common practice to maintain a water layer as tank bottoms. Even where a separate water layer is not maintained as tank bottoms, a separate water phase may be formed by repeated condensation of moisture associated with tank breathing or the repeated expansion and contraction of the bulk due to temperature changes unless special precautions are taken. Complete protection against rusting, therefore, requires a corrosion inhibitor which is effective in both the oil and water phase.
It is an object of the present invention to provide a corrosion and/ or rust inhibitor adapted for use in preventing the corrosion and/or rusting of metals by liquids containing corrosive compounds associated with oleaginous materials such as petroleum fuel oils. It is a further object of this invention to provide a normally liquid nonlubricating hydrocarbon fuel oil composition having improved rust inhibiting properties for the protection of metal surfaces of oil storage and/or handling equipment whether metal surfaces be exposed to the oil or to the water phase. Other objects and advantages of the invention will become apparent from the following description thereof.
I have now discovered certain new corrosion inhibitors which find utility as inhibitors for fuel oils. The corrosion inhibitor is an imide prepared by reacting propylene diamine with polybasic aromatic acid. The corrosion inhibitor of the present invention is an imide represented by the formula C coon NCH2CH2 2N placed in a reactor.
$,M,79 Patented Aug. 25, 1964 wherein R is C1248 alkyl radical and R is a member of the group consisting of H and a C alkyl radical.
The alkyl groups of the above formula are preferably hydrocarbon alkyl groups. The preferable hydrocarbon groups are those groups having from about 12 carbon atoms to about 18 carbon atoms such as, for example, those derived from higher fatty acids, e.g., lauryl, oleyl, linoleyl, tallow, soybean, coco, stearyl, palmityl, myristyl and the like.
- The corrosion inhibitors of this invention may be used to form a fuel oil composition containing a major proportion of a distillate fuel oil and a small or minor amount of the corrosion inhibitor. Such distillate fuel oil compositions may comprise a distillate fuel oil containing from about 0.0001 to about 5 weight percent and preferably from about 0.0001 to about 0.05 weight percent of the corrosion inhibitor. The corrosion inhibitor may also be formulated as an addition agent concentrate in a suitable organic solvent as more particularly described below. This concentrate may be used by further dilution with the distillate fuel oil to form the distillate fuel oil composition. The corrosion inhibitors of the present invention are advantageously oil-soluble.
The corrosion inhibitors of this present invention may be prepared by reacting the corresponding propylene diamine in the presence of inert solvent with polybasic aromatic acid. The reaction may be carried out in the presence of a solvent such as benzene, ethanol, n-butanol, isobutanol, xylene, etc. A acceptable temperature for the reaction may be in the range of from about F. to about 200 F. although higher or lower temperatures may be used.
The following procedures illustrate the method of preparing the corrosion inhibitor of the invention.
PROCEDURE A A mixture of 5.94 g. of N,N ditallow 1,3 propylene diamine, 1.92 g. of trimellitic anhydride, and 50 ml. of xylene were placed in a reactor. The reactor was heated to the reflux temperature of Xylene and maintained at this temperature for a period of 8 hours after which 0.20 ml. of water was recovered. A total of 6.5 g. of product having the following formula was recovered:
PROCEDURE B A mixture of 20 g. of N-tallow 1,3-propylene diamine, 9.6 g. of trimellitic anhydride, and 250 ml. of Xylene were The reactor was heated to the reflux temperature of xylene after which 0.90 ml. of water was recovered. A total of 29 g. of product having the following formula was recovered:
The corrosion inhibitors defined herein, such as those prepared as described above as well as those set forth in the above examples are usable in minor amounts from about 0.0001 to about 5 weight percent and preferably from about 0.001 to about 0.05 weight percent in distillate fuel oils.
The distillate fuel oil may belvirgin or cracked petroleum distillate fuel oil. 'The fuel oil may boil in the range of from about 200 to about 750 F., and preferably in the range of 350 to 650 F. The distillate fuel oil may contain or consist of cracked-components such as, for example, those derived from cycle oils or cycle oil cuts boiling heavier than gasoline, usually in the range of from about 450 to 750 F. and may be derived by catalytic or thermal cracking. The distillate oil may contain other components such as addition agents used for a particular function such as, for example, pour point depressants, combustion improvers, or the like.
The distillate fuel oil is preferably a heating oil in which the corrosion inhibitors of this invention are used in accordance herewith. These oils are intended for use by burning to obtain heat such as is intended for furnace or heater fuel use as opposed to internal combustion engine fuel wherein the explosiveness of the fuel in a combustion chamber is of prime importance. Examples of such heating oils are a heavy industrial residual fuel (e.g.,-Bunker C), a heater oil fraction, a gas oil, a furnace oil, kerosene, or any other light oil intended for furnace or heater fuel use.
The rust inhibiting properties of the above described compositions were evaluated by the following test:
INDIANA CONDUCTOMETRIC TEST (STATIC) This test, which quantitatively measures corrosion rates, depends upon the measurement of the change in electrical resistance of a steel test strip immersed in the corrosive medium. The change in resistance is simply related to the decrease in the thickness of the test specimen caused by corrosion. In the test, specimen holders are designed to make electrical connections to two steel strips suspended in large glass test tubes. A mixture is prepared using six parts of hydrocarbon oil containing the rust inhibitor and four parts double distilled water. The corrosion test strips are first immersed in the oil containing the rust inhibitor for a period of one-half hour and subsequently suspended in the mixture such that approximately one-half of the specimen is above the oil-water interface and the remaining half of the specimen is below the oil-water interface. The strips are maintained in the mixture for a period of 24 hours at a temperature of 25 C. The corrosion rates are calculated on a quantative basis from the observed change in electrical resistance comparing the specimen from the inhibited mixture with a specimen run under the same conditions in an uninhibited mixture.
The data obtained by subjecting theproducts of this invention to the above test are tabulated in the following table and demonstrate the effectiveness of the herein described products in inhibiting rust in fuel oil compositions.
2 Virgin gas 011. water.
do 92 10- 'M HCL. 93 97. 5
Heater oil Gasoliue The corrosion inhibitors of the present invention may, for convenience, be prepared as an addition agent concentrate. Accordingly, the corrosion inhibitor is prepared in or dissolved in a suitable organic solvent therefor in amounts greater than 10% and preferably from'about 25% to about 65%. The solvent, in such concentrate, may conveniently be present in amounts of from about 35% to about 75%. The organic solvent preferably boils within the range of from about 100 F. to about 700 F. For the preferred heating oil use, the organic solvents may advantageously be hydrocarbon solvents, for example, petroleum, petroleum fractions, such as naphtha, heater oil, mineral spirits and the like, because of their clean burning properties. The solvents selected should, of course, be selected with regards to beneficial or adverse effects it may have on the ultimate fuel oil compo- I sition. Thus, the solvent should preferably burn with- 'out leaving a residue and should be non-corrosive with regard to metal, and especially ferrous metals. Other desirable properties are obvious from the intended use of the solvent.
The terms coco, soybeans, tallow, and the like as used herein denote that the group so identified is derive/1 from a particular source. The coco groups are derived from mixtures of coco fatty acids; the soybean groups are derived from soybean fatty acids; the tallow groups are derived from tallow fatty acids. Such coco, soybean and tallow fatty acids are derived from coconut, soybean and tallow oils and are marketed commercially. Each such group is usually a mixture of carbon chains differing slightly in length and/or configuration. For example, the tallow groups are a mixture of C to C groups predominating in stearyl and palmityl groups.
a, at
' The groups are well known in the additive art.
Wherever percentages are given herein, weight percentages are intended unless otherwise indicated.
It is evident from the foregoing that I have provided new and useful corrosion inhibitors for distillate fuel oils and particularly in distillate heating oils.
I claim:
1. A distillate fuel oil composition comprising a major proportion of a hydrocarbon oil fraction in the fuel oil wherein R is a C1248 alkyl radical and R is a member of the group consisting of H and a C alkyl radical.
2. A corrosion inhibitor concentrate for use in a distillate fuel oil comprising from about 35% to about 75% by weight of an organic solvent and from about 25% to 5 6 about 65% by weight of an imide having the formula 4. A fuel oil composition comprising a major proportion of a hydrocarbon oil fraction in the fuel oil disstillation range and from about 0.0001 to about 5.0%
by weight of an irnide having the formula COOH 0 NCHZCHZCHZN II 0 R1 R OOOH ll NcmomomN 10 R1 wherein R is a C1248 alkyl radical and R is a member of the group consisting of H and a C alkyl radical. 0
3. A fuel oil composition comprising a major proh R C k 1 a1 d R portion of a hydrocarbon oil fraction in the fuel oil dis- W erem 1s a a1 Ia 1C an 1 1S ydmgen tillation range and from about 0.0001 to about 5.0% by 15 References Clted 111 the file of thls Patent Weight of an imide having the formula UNITED STATES PATENTS 0 1,908,705 Jaeger May 16, 1933 ll 2,604,451 Rocchini July 22, 1952 R 2,699,427 Smith et a1 Jan. 11, 1955 COOH 2,816,897 Wolf Dec. 17, 1957 H 3,056,832 Stromberg Oct. 2, 1962 7; R1 OTHER REFERENCES New Reactions of Fatty Amines Show Promise for Many Applications, article by McCorkle in Chemical and wherein 1 and 2 are each C12-18 alkyl Tadlcal- Engineering News, August 17, 1953, pages 3354-3355.
Claims (1)
1. A DISTILLATE FUEL OIL COMPOSITION COMPRISING A MAJOR PROPORTION OF A HYDROCARBON OIL FRACTION IN THE FUEL OIL DISTILLATION RANGE AND FROM ABOUT 0.0001 TO ABOUT 5.0% BY WEIGHT OF AN IMIDE HAVING THE FORMULA
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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US55731A US3146079A (en) | 1960-09-13 | 1960-09-13 | Fuel oil composition |
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US55731A US3146079A (en) | 1960-09-13 | 1960-09-13 | Fuel oil composition |
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US3146079A true US3146079A (en) | 1964-08-25 |
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US55731A Expired - Lifetime US3146079A (en) | 1960-09-13 | 1960-09-13 | Fuel oil composition |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2102559A1 (en) * | 1970-01-21 | 1971-08-26 | Institut Francais du Petrole des Carburants et Lubrifiants, Rueil Mal maison, Entrepnse de Recherches et d Activites Petroheres Elf, Paris, (Frankreich) | New imide compounds, processes for their production and their use as fuel additives |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1908705A (en) * | 1931-07-23 | 1933-05-16 | Selden Co | Motor fuel |
US2604451A (en) * | 1948-09-16 | 1952-07-22 | Gulf Research Development Co | Mineral oil compositions |
US2699427A (en) * | 1952-10-02 | 1955-01-11 | Gulf Oil Corp | Mineral oil compositions containing amidic acids or salts thereof |
US2816897A (en) * | 1956-06-05 | 1957-12-17 | Ethyl Corp | Organic chemicals |
US3056832A (en) * | 1958-01-16 | 1962-10-02 | Petrolite Corp | Partial amides |
-
1960
- 1960-09-13 US US55731A patent/US3146079A/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1908705A (en) * | 1931-07-23 | 1933-05-16 | Selden Co | Motor fuel |
US2604451A (en) * | 1948-09-16 | 1952-07-22 | Gulf Research Development Co | Mineral oil compositions |
US2699427A (en) * | 1952-10-02 | 1955-01-11 | Gulf Oil Corp | Mineral oil compositions containing amidic acids or salts thereof |
US2816897A (en) * | 1956-06-05 | 1957-12-17 | Ethyl Corp | Organic chemicals |
US3056832A (en) * | 1958-01-16 | 1962-10-02 | Petrolite Corp | Partial amides |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2102559A1 (en) * | 1970-01-21 | 1971-08-26 | Institut Francais du Petrole des Carburants et Lubrifiants, Rueil Mal maison, Entrepnse de Recherches et d Activites Petroheres Elf, Paris, (Frankreich) | New imide compounds, processes for their production and their use as fuel additives |
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