US2882232A - Improving the odor of specialty naphthas - Google Patents

Improving the odor of specialty naphthas Download PDF

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Publication number
US2882232A
US2882232A US546785A US54678555A US2882232A US 2882232 A US2882232 A US 2882232A US 546785 A US546785 A US 546785A US 54678555 A US54678555 A US 54678555A US 2882232 A US2882232 A US 2882232A
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odor
naphtha
specialty
naphthas
nitrile
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US546785A
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Robert M Haines
John W Walsh
Weldon G Annable
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Pure Oil Co
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Pure Oil Co
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/228Organic compounds containing nitrogen containing at least one carbon-to-nitrogen double bond, e.g. guanidines, hydrazones, semicarbazones, imines; containing at least one carbon-to-nitrogen triple bond, e.g. nitriles
    • C10L1/2286Organic compounds containing nitrogen containing at least one carbon-to-nitrogen double bond, e.g. guanidines, hydrazones, semicarbazones, imines; containing at least one carbon-to-nitrogen triple bond, e.g. nitriles containing one or more carbon to nitrogen triple bonds, e.g. nitriles

Definitions

  • This invention relates to specialty naphthas. It .is more specifically concerned witliximprovingthe .odor' characteristics of petroleum-derived industrial naphthas.
  • any odor which may be unpleasant or disagree able tothe consumer be changed.
  • petroleum products develop a rancid odor after an initial induction period.
  • this type of odor is due to the oxidation of the hydrocarbons contained in the petroleum product and can be obviated by the use of additives which function as oxidation inhibitors.
  • specialty naphthas have strong lacrymal and/or rhinitic effects which become in certain products more disagreeable when the naphtha is used in relatively high temperature processing.
  • no standard test has been developed which will permit the evaluation of the odoriferous properties of naphthas.
  • Petroleum naphthas may have a wet odor which occurs in naphtha in bulk form. They also may have a dry or residual odor which could be present in fabrics which have been in contact with petroleum naphthas, such as in the dry cleaning industries. Even though the dry cleaning solvent is substantially completely extracted from the goods being cleaned, there may persist in the goods an unpleasant odor attributed to the dry cleaning solvent.
  • improvement in the odor of specialty naphthas is provided by the addition thereto of trace amounts of an organic nitrile compound. It has been found that. if small amounts of an organic nitrile, having not morethan 12. carbon atoms per molecule, are admixed with a specialty petroleumnaphtha, a.composi-' tion free from irritating odors can be produced;
  • The. organic nitriles which can be employed in carrying out this invention include aliphatic and alicyclic nitriles, aromatic nitriles and alkaryl nitriles.
  • acetonitrile butyronitrile, caprylonitrile, isovaleronitrile, trideconitrile, benzonitrile, O- methylbenzonitrile, O-tolunitrile, napthylnitrile, cyclohexylbenzonitrile, cyclohexylnitrile, phenylbutyronitrile, phenylacetonitrile, etc.
  • These additives have an inherent peculiar odor. However, when they are incorporated in a specialty petroleum naphtha possessing irritating odors, the blended composition has a substantially improved, mild odor having non-irritating characteristics.
  • An important feature of the instant invention is the use of only trace amounts of the nitrile reodorant to bring about the objectives of this invention. While the exact amount of nitrile used will depend upon the naphtha boiling range, the source of the naphtha, the composition of the naphtha, the treatment of the naphtha, and the temperature at which the naphtha is to be used, it has been found that between 190 p.p.m. will provide satisfactory results, and in most instances about 10 parts per million will provide a specialty naphtha having a suitable odor.
  • the naphtha composition If more than about parts per million are employed, there will be imparted to the naphtha composition an offensive nitrile odor which is as disagreeable as the strong, irritating odor normally present in the specialty naphtha.
  • an offensive nitrile odor which is as disagreeable as the strong, irritating odor normally present in the specialty naphtha.
  • the wet and/or dry or residual odor of petroleum specialty naphthas is substantially improved by the addition of nitrile reodorants of this invention, the use of the more volatile nitriles is preferred when the Wet odor is to be corrected, and less volatile nitriles are preferred for improving the dry or residual odor.
  • the petroleum specialty naphthas which can be reodorized according to this invention are low sulfur content, straight-run, specialty naphthas.
  • These naphthas are produced from crude petroleum oils of the paratfinic, naphthenic or mixed base types, such as Pennsylvania, California, or Mid-Continent crude oils. These naphthas have boiling ranges between about to 425 F., and have been refined by conventional refining processes to remove or convert the sulfur compounds contained therein to produce naphthas having a low sulfur content, as determined by the doctor test or distillation-corrosion 3 test.
  • a specialty petroleum naphtha produced from a Mid-Continent-type crude petroleum oil and treated in a conventional Linde sweetening process, had the following characteristics:
  • nitrile is an aliphatic nitrile.
  • Method in accordance nitrile is an alicyclic nitrile.
  • Method in accordance nitrile is an aromatic nitrile.
  • Method in accordance nitrile is an alkaryl nitrile.
  • nitrile is selected from the group consisting of acetoniin which the with claim 1 in which the wit hclaim 1 in which the with claim 1 in which the I trile, butyronitrile, caprylonitrile, isovaleronitrile, trideper se, as reodorants for light petroleum disullatcs bo1ling in the naphtharange.

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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)
  • Fats And Perfumes (AREA)

Description

United States Patent IMPROVING THE. ODOR or SPECIALTY HTHAS NAP Robert M. Haines and John W. Walsh, Crystal Lake,- and Weldon G. Annable,.Mundelein, Ill., assignors to The Pure Oil Company, Chicago, Ill.,.a corporation of Ohio No Drawing. Application November 14, 1955 Serial No. 546,785
8 Claims. (Cl. 252-50).
This invention relates to specialty naphthas. It .is more specifically concerned witliximprovingthe .odor' characteristics of petroleum-derived industrial naphthas.
The re-odorizing of various'. substances by adding odor to them to disguise orconceal any disagreeable odors that. may be. an'inherent characteristic isan old art. Products the disagreeable odor to a pleasant one. In the case of.
unsatisfactory or undesirable odors this objective is efiectuated by the use of odor masking agents or re-ordorants. The technique of're-odorizing is'practical in many products, including a variety of petroleum products. One class of petroleum products which in recent years has achieved commercial significance is the highly refined naphthas. These goods are defined as selected fractions of the lighter, more volatile constituents of crude petroleum, chemically refined and separated into various boiling ranges. Although this definition includes aromatic compounds the instant invention is concerned only with straight-run or virgin products. Because of their good solvent properties, essentially nontoxic character, low corrosion, ready availability, and their functional versatility, petroleum naphthas can be prepared which are adaptable to a wide variety of industrial uses. It is therefore desirable that any odor which may be unpleasant or disagree able tothe consumer be changed. In some instances, petroleum products develop a rancid odor after an initial induction period. Generally, this type of odor is due to the oxidation of the hydrocarbons contained in the petroleum product and can be obviated by the use of additives which function as oxidation inhibitors. However, specialty naphthas have strong lacrymal and/or rhinitic effects which become in certain products more disagreeable when the naphtha is used in relatively high temperature processing. Although many qualitative and quantitative tests have been devised to control the properties of naphthas and insure their uniform quality, no standard test has been developed which will permit the evaluation of the odoriferous properties of naphthas. Petroleum naphthas may have a wet odor which occurs in naphtha in bulk form. They also may have a dry or residual odor which could be present in fabrics which have been in contact with petroleum naphthas, such as in the dry cleaning industries. Even though the dry cleaning solvent is substantially completely extracted from the goods being cleaned, there may persist in the goods an unpleasant odor attributed to the dry cleaning solvent.
In evaluating the odor characteristics of a petroleum This type of testing is used extensively in the evaluation of odor and flavor in foods and beverages. In general, the technique involves the selectionof a carefully selected panel of several individuals which minimizes errors which might arise from the use of a single evaluation. Panel testing as ameans for detecting odors is a recognized" expedient for the determination of the type and source. of odor and the level. Fora more COITIPIGhCHSiVGdlS-e cussion of the techniques of organoleptic panel testing, reference is made to Analytical Chemistry 24 (3-), March 1952, at page 503; Modern Packaging 25 (11), July 1952, at page 145, and 26 10), June'1953, at page 149.
It is therefore an object-of thisinvention to-re-odorize specialty petroleum naphthas. It is another objective of this invention to provide a petroleumnaphtha free from lacrymal and/or rhinitic efiects. Still another objective of this invention is to improve the odor of specialty naphthas. It is also an objective of this'invention to improve the wet and/or dry orresidual odors of specialty petroleum naphthas. These and other objectives will be apparent from the following detailed description of this invention.
According to this invention, improvement in the odor of specialty naphthas is provided by the addition thereto of trace amounts of an organic nitrile compound. It has been found that. if small amounts of an organic nitrile, having not morethan 12. carbon atoms per molecule, are admixed with a specialty petroleumnaphtha, a.composi-' tion free from irritating odors can be produced; The. organic nitriles which can be employed in carrying out this invention include aliphatic and alicyclic nitriles, aromatic nitriles and alkaryl nitriles. Specific examples include but are not limited to acetonitrile, butyronitrile, caprylonitrile, isovaleronitrile, trideconitrile, benzonitrile, O- methylbenzonitrile, O-tolunitrile, napthylnitrile, cyclohexylbenzonitrile, cyclohexylnitrile, phenylbutyronitrile, phenylacetonitrile, etc. These additives have an inherent peculiar odor. However, when they are incorporated in a specialty petroleum naphtha possessing irritating odors, the blended composition has a substantially improved, mild odor having non-irritating characteristics. An important feature of the instant invention is the use of only trace amounts of the nitrile reodorant to bring about the objectives of this invention. While the exact amount of nitrile used will depend upon the naphtha boiling range, the source of the naphtha, the composition of the naphtha, the treatment of the naphtha, and the temperature at which the naphtha is to be used, it has been found that between 190 p.p.m. will provide satisfactory results, and in most instances about 10 parts per million will provide a specialty naphtha having a suitable odor. If more than about parts per million are employed, there will be imparted to the naphtha composition an offensive nitrile odor which is as disagreeable as the strong, irritating odor normally present in the specialty naphtha. Although the wet and/or dry or residual odor of petroleum specialty naphthas is substantially improved by the addition of nitrile reodorants of this invention, the use of the more volatile nitriles is preferred when the Wet odor is to be corrected, and less volatile nitriles are preferred for improving the dry or residual odor.
The petroleum specialty naphthas which can be reodorized according to this invention are low sulfur content, straight-run, specialty naphthas. These naphthas are produced from crude petroleum oils of the paratfinic, naphthenic or mixed base types, such as Pennsylvania, California, or Mid-Continent crude oils. These naphthas have boiling ranges between about to 425 F., and have been refined by conventional refining processes to remove or convert the sulfur compounds contained therein to produce naphthas having a low sulfur content, as determined by the doctor test or distillation-corrosion 3 test. an article entitled Effect of Sulfur and Sulfur Compounds in Naphtha Upon Certain Corrosion Tests, I. & E. Chemistry, Analytical Edition 12 (1), 1. Refined, straight-run petroleum naphthas, which'pass the doctor test and the distillation-corrosion test and are low in sulfur content, containing not more than about 0.05%- by weight of sulfur, are employed in this invention.
To illustrate the subject invention, a specialty petroleum naphtha, produced from a Mid-Continent-type crude petroleum oil and treated in a conventional Linde sweetening process, had the following characteristics:
Gravity 46.5 API. ASTM boiling range, F.:
I.B.P. 365 F. 50% 370 F. El. 405 F. Color 29. Doctor test Negative. Distillation-corrosion test Negative. T.C.C. flash point 142 F. H2804 absorption 1.5%. Odor (panel testing) Strong, irritating.
To this specialty naphtha was added 50 parts per million of caprylonitrile. In subjecting this to an organoleptic panel testing evaluation, it was found that a substantial improvement in odor was effected and the resultant composition had a mild and pleasant, non-irritating odor.
The foregoing example is an illustrative and nonlimiting embodiment of this invention. The unusualness of this invention is made manifest by the use of selected organic nitriles which have disagreeable odors,
These tests are described by Henderson et al., in
Therefore, we claim as our invention:
1. The method of preparing a specialty naphtha of satisfactory odor from refined straight-run petroleum naphtha of disagreeable odor, having a sulfur content sufliciently low to pass the doctor test and distillation-corrosion test, "which consists in blending with said naphtha at ambient temperature between 1 and 90 parts per'million of an organic nitrile having not more than 12 carbon atoms per molecule, the amount ofnitrile being suflicient to improve the disagreeable and unpleasant odor of said naphtha.
2. Method in accordance with claim 1 nitrile is an aliphatic nitrile. 3. Method in accordance nitrile is an alicyclic nitrile. 4. Method in accordance nitrile is an aromatic nitrile.
5. Method in accordance nitrile is an alkaryl nitrile.
6. Method in accordance with claim 1 in which the" nitrile is a caprylonitrile. 1
' 7. Method in accordance with claim 1 in which the nitrile is selected from the group consisting of acetoniin which the with claim 1 in which the wit hclaim 1 in which the with claim 1 in which the I trile, butyronitrile, caprylonitrile, isovaleronitrile, trideper se, as reodorants for light petroleum disullatcs bo1ling in the naphtharange.
References Cited in the file of this patent V UNITED STATES PATENTS 2,235,936 Lerch et al. Mar. 25, 1941 2,393,212 Young et a1. Jan. 15, 1946

Claims (1)

1. THE METHOD OF PREPARING A SPECIALTY NAPHTHA OF SATISFACTORY ODOR FROM REFINED STRAIGHT-RUN PETROLEUM NAPHTHA OF DISAGREEABLE ODOR, HAVING A SULFUR CONTENT SUFFICIENTLY LOW TO PASS THE "DOCTOR TEST" AND DISTILLATION-CORROSION TEST", WHICH CONSISTS IN BLENDING WITH SAID NAPHTHA AT AMBIENT TEMPERATURE BETWEEN 1 AND 90 PART PER MILLION OF AN ORGANIC NITRILE HAVING NOT MORE THAN 12 CARBON ATOMS PER MOLECULE, THE AMOUNT OF NITRILE BEING SUFFICIENT TO IMPROVE THE DISAGREEABLE AND UNPLEASANT ODOR OF SIAD NAPHTHA.
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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2978406A (en) * 1959-07-07 1961-04-04 Pure Oil Co Production of odorless naphthas
US3073778A (en) * 1959-11-09 1963-01-15 Pure Oil Co Method of preparing odorless naphthas
US3090748A (en) * 1959-11-17 1963-05-21 Exxon Research Engineering Co Process for desulfurization employing a nitrile impregnated substrate
US3223631A (en) * 1962-12-07 1965-12-14 Exxon Research Engineering Co Lubricating composition
FR2235187A1 (en) * 1973-06-26 1975-01-24 Naphtachimie Sa
US4802973A (en) * 1986-01-30 1989-02-07 The British Petroleum Company P.L.C. Removal of hydrogen sulphide
WO1998004656A1 (en) * 1996-07-31 1998-02-05 Elf Antar France Fuel with low sulphur content for diesel engines

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2235936A (en) * 1938-06-20 1941-03-25 Phillips Petroleum Co Process for treating hydrocarbons
US2393212A (en) * 1942-07-15 1946-01-15 Standard Oil Dev Co Blended lubricating oils

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2235936A (en) * 1938-06-20 1941-03-25 Phillips Petroleum Co Process for treating hydrocarbons
US2393212A (en) * 1942-07-15 1946-01-15 Standard Oil Dev Co Blended lubricating oils

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2978406A (en) * 1959-07-07 1961-04-04 Pure Oil Co Production of odorless naphthas
US3073778A (en) * 1959-11-09 1963-01-15 Pure Oil Co Method of preparing odorless naphthas
US3090748A (en) * 1959-11-17 1963-05-21 Exxon Research Engineering Co Process for desulfurization employing a nitrile impregnated substrate
US3223631A (en) * 1962-12-07 1965-12-14 Exxon Research Engineering Co Lubricating composition
FR2235187A1 (en) * 1973-06-26 1975-01-24 Naphtachimie Sa
US4802973A (en) * 1986-01-30 1989-02-07 The British Petroleum Company P.L.C. Removal of hydrogen sulphide
WO1998004656A1 (en) * 1996-07-31 1998-02-05 Elf Antar France Fuel with low sulphur content for diesel engines
FR2751982A1 (en) * 1996-07-31 1998-02-06 Elf Antar France ONCTUOSITY ADDITIVE FOR FUEL ENGINES AND COMPOSITION OF FUELS
EP1310547A1 (en) * 1996-07-31 2003-05-14 TotalFinaElf France Fuel with low sulphur content for diesel engines
US20040049971A1 (en) * 1996-07-31 2004-03-18 Elf Antar France Fuel with low sulphur content for diesel engines
US7374589B2 (en) 1996-07-31 2008-05-20 Elf Antar France Fuel with low sulphur content for diesel engines

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