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US2977310A - Oxidation of petroleum fractions - Google Patents

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US2977310A
US2977310A US653299A US65329957A US2977310A US 2977310 A US2977310 A US 2977310A US 653299 A US653299 A US 653299A US 65329957 A US65329957 A US 65329957A US 2977310 A US2977310 A US 2977310A
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dicyclic
hydrocarbons
fraction
petroleum
ring
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Archibald P Stuart
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Sunoco Inc
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Sun Oil Co
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
    • C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
    • C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
    • C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
    • C07C45/36—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in compounds containing six-membered aromatic rings

Definitions

  • This invention relates to the preparation of valuable products from cracked petroleum fractions containing dicyclic hydrocarbons.
  • the products include in addition to gasoline certain higher boiling fractions, generally known as catalytic gas oil, which contain dicyclic hydrocarbons, These higher boiling fractions can be recycled to the cracking operation to obtain gasoline from some ofthe hydrocarbons therein, but some of the hydrocarbons are refractory to cracking and remain in the higher boiling range after the second pass through the cracking operation.
  • Catalytic gas oils are often used only for fuel, and it would be highly desirable to obtain more valuable products from catalytic gas oils obtained after either one or two passes through a catalytic cracking operation.
  • valuable products are obtained from catalytic gas oils by hydrogenation thereof and partial oxidation of dicyclic hydrocarbons in the hydrogenation products, which hydrocarbons have one cycloaliphatic ring inthe molecule and one aromatic ring in the molecule.
  • the products of the oxidation are believed to be ketones, the carbon atom of the carbonyl group of which is a member of the cycloaliphatic ring.
  • the oxygenated compounds which are formed in the partial oxidation are useful as petroleum additives, resin intermediates, etc. They can be removed from the unoxidized hydrocarbons by various methods, such as by extraction of the oxygenated compounds by means of a polar solvent, e.g. ethanol, acetone, furfural, phenol, liquid S0 etc., by selective adsorption of the oxygenated compounds on an adsorbent such as silica gel,'etc.
  • a polar solvent e.g. ethanol, acetone, furfural, phenol, liquid S0 etc.
  • the partial oxidation according to the invention is not applicable to catalytic gas oils as obtained directly from cracking operations, since such catalytic gas oils generally contain too small amounts of dicyclic compounds containing a cycloaliphatic ring. it is therefore necessary.
  • oxygenated compounds which are prepared according to the invention are'used, in one embodiment, as
  • additives for gasoline or motor oil, for the purpose of reducing combustion chamber deposits, in internal combustion engines 7 compounds employed for such, use is within the approximate range from 0.05 to weight percent based on the hydrocarbon fraction to-which it is added, more preferably 0.1 to Zweightpercent.
  • the oxygenated compounds can "be re p duc'ed, by.catalytic”.hydrogenation orreductionwith-soe..
  • An'y suitable hydrogenation catalystcan be e e preferred catalysts b'eing' metals such as cobal molybdium and alcohol or other known procedures, to obtain Preferably the amount of oxygenated I alyst bed per hour, and at a temperature wt n t PatentedMar. 28, 19 61 oxygenated dicyclic compounds in a lesser stage of oxida-] tion, believed to be dicyclic compounds having'a hydroxyl group attached to the cycloaliphatic ring.
  • ,Suchi com pounds may be employed as additives for gasolineor motor oil, for the purpose of reducing combustion chamber deposits, in proportions similar to those described previously.
  • these oxygenated compounds in a lesser stage of oxidation can be chemically dehydrated accord ing. to known procedures in order to form dicyclic hydrocarbons which differ from the original dicyclic hydro'. carbons in having an olefinicdouble bond in the 1,2 position in' the cyclo aliphatic ring
  • These ultimate dicyclic hydrocarbons can be polymerized or copolyrnerized with other monomers such as butadiene to form synthetic plastics or rubber-like materials.
  • Theoxidation according to the invention is performed by contacting a suitable fraction containing dicyclic hydrocarbons with a free-oxygen containing gas at a temperature within theapproximate range from 150 F. to- 300 F. in the, presence. of a metallic catalyst of the. well known drier type, e.g. compounds of manganese, cobalt, copper, lead, iron,.etc., e.g.
  • the chargestock for the oxidation according to the. inveution is a hydrogenated petroleum fraction contain.- ing at least 5 weight percent based on charge ofidicyclic. hydrocarbons containing one aromatic ring and one cyclo aliphatic ring.
  • the charge stock contains at, least 10 percent of such dicyclic hydrocarbons, e.g.;10 to 50 percent. .A major proportion of the charge'stockj boils. within the approximate range from 480 F.i'to
  • At least l0 percent of the charge. boils below 500 F., and at. least 10 percent above 550 F.
  • the charge stock can be a hydrogenated cracked petro- 1 leum fraction containing for example 15 to 50 .Weight percent of aromatic hydrocarbons, i.e. hydrocarbons containing atleast one aromatic ring per molecule. .Alterfl natively, it can be a hydrogenated aromaticconcentrat'e'. I from cracked petroleum containing up to percent aromatic hydrocarbons and obtained by extraction with;
  • a selective solvent for aromatics e.g. furfural, orselec tive adsorption on a selective adsorbent for aromatics
  • a selective adsorbent for aromatics e.g. silica gel, oraby other known methods.
  • the charge stock contains a large proportionlof'dii cyclic hydrocarbons having'alkyl side chains in themole-1 cule,-
  • the conditions employedin the oxidation as dis'fj closed previously are such that-the principal oXidatiQD j involves carbon atoms in the cycloaliphatic ring,..rathe1r--;' than carbon atoms in alkylside chains.
  • the carbonyl group formeclin the oxidation is, formed. primarily at" the alpha carbon atom of the cycloaliphatic ringin the dicyclic molecule, except'in cases Where that.carb.on atom has an alkyl radical attached thereto.
  • anysuitable hydrogenation procedure can be employed priorto the oxidation according tothe invention, Prefer; f ably, the hydrogenationisperformed by passing thecharge K stock downwardly through a bed of solid hydrogenation catalyst at a space rate within the approximate. rang? from 0.25 to 5.0 volumes of charge ,per volume 'of cat denum, nickel, etc., or oxides or sulfides thereof, associated with a suitable carrier, e.g. alumina, bauxite, silica alumina composites.
  • a suitable carrier e.g. alumina, bauxite, silica alumina composites.
  • Hydrogenation catalysts for partial hydrogenation of dicyclic aromatic hydrocarbons are well known in the art, and any suitable known catalyst can be employed
  • the hydrogenation should be performed at conditions which produce a maximum amount of dicyclic compounds containing one aromatic ring and one cycloaliphatic ring and a minimum amount of compounds containing two cycloaliphatic rings.
  • the temperature in the hydrogenation should not be substantially greater than 650 F. and the liquid hourly space velocity is preferably at least 1.
  • a person skilled in the art can select proper hydrogenation conditions to bring about the desired result in a given instance.
  • Example I A hydrogenated first pass catalytic gas oil containing 64 weight percent of saturated hydrocarbons and 36 weight percent of aromatic hydrocarbons, of which 15 weight percent are dicyclic hydrocarbons containing one cycloaliphatic ring and 2 percent are dicyclic hydrocarbons containing two cycloaliphatic rings, which hydrogenated gas oil has refractive index r1 of 1.4879, specific gravity d of 0.8689 and the following Engler distillation in F.:
  • the previous hydrogenation was performed at 608 F., 800 p.s.i.g., and liquid hourly space velocity of 0.9 volume per volume of catalyst bed per hour, using a catalyst comprising about 20 percent molybdenum disulfide on alumina.
  • the original first pass catalytic gas oil contained about 62 percent saturates and 38 percent aromatics, of which 3 percent based on charge were dicyclic hydrocarbons containing one cycloaliphatic ring.
  • the oxygen-containing compounds are separated from the extracting solvent, e.g. ethanol, by dilution of the ethanol solution with water in order to precipitate the oxygen-containing dicyclic compounds.
  • the extracting solvent e.g. ethanol
  • the recovered oxygen-containing dicyclic compounds are in one embodiment employed as additives for gasoline, e.g. a 90-400" F. commercially available leaded gasoline, for the purpose of reducing combustion chamber deposits, using for example 0.1% of additive material, or as additives for motor oil, e.g.'a commercially available SAE 10W30 oil, for the same purpose and using for example 0.1% of additive material.
  • gasoline e.g. a 90-400" F. commercially available leaded gasoline
  • motor oil e.g.'a commercially available SAE 10W30 oil
  • the oxygen-containing dicyclic compounds are reduced to dicyclic compounds having a hydroxyl group attached to a cycloaliphatic ring by suitable procedure for converting cyclic ketones to cyclic hydroxyl compounds.
  • the carbonyl compounds can be contacted with hydrogen at 190 F. to 230 F. in the presence of a catalyst comprising copper oxide and chromium oxide for a period sufiicient to convert the carbonyl oxygen to a hydroxyl group.
  • known methods of reduction by hydrogenation with a Raney nickel catalyst can be employed to convert the carbonyl compounds to hydroxyl compounds.
  • the resulting hydroxyl compounds can be employed as additives for gasoline or motor oil in amanner generally simi- 4 lar to that previously described with reference to the carbonyl compound.
  • the hydroxyl compounds can in one embodiment be dehydrated, for example by contact with alumina at 750 F., to convert the hydroxyl compounds into dehydration products thereof containing a cyclohexene ring and an aromatic ring.
  • dehydration products have an olefinic double bond in the cycloaliphatic ring in the 1,2 position. They are capable of undergoing vinyl-type addition polymerization at the olefinic double bond.
  • Any suitable known means of bringing about such polymerization can be employed to produce dimers or higher molecular weight vinyl polymers from these unsaturated hydrocarbons. Thus for example they can be polymerized, e.g.
  • the polymer can be recovered from the product mixture by adding water to hydrolyze the sodium compounds and filtering the precipitated polymer.
  • the unsaturated hydrocarbons can also be copolymerized with olefins such as propylene or isobutylene, e.g. at minus 150 F., in butane with 0.5 gram of an aluminum chloride or other Friedel-Crafts catalyst per ml. of monomers.
  • Such polymers of the unsaturated hydrocarbons can be employed, e.g. in 1% concentration, as viscosity index improving additives for petroleum lubricating oil, e.g. a mixed base oil having Saybolt Universal viscosity at 100 F. of about 100 and viscosity index of about 80 prior to addition of the additive.
  • Example II In a manner generally similar to that described in Example I, a hydrogenated second pass catalytic gas oil containing about 58 weight percent of saturated hydrocarbons and 42 weight percent of aromatic hydrocarbons of which 20 weight percent are dicyclic hydrocarbons containing one cycloaliphatic ring is partially oxidized in liquid phase to produce oxygen-containing dicyclic compounds which are extracted from the unoxidized hydrocarbons by means of ethanol.
  • the products thus obtained can be further employed in a manner similar to that described in Example I.
  • Process for producing valuable products from petroleum which comprises; contacting a petroleum'fraction containing at least 5 weight percent of dicyclic hydrocarbons containing one aromatic ring and' one cycloaliphatic ring and containing alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., in liquid phase with free-oxygen containing gas at a temperature of F. to 300 F. in the presence of a metallic oxidation catalyst, thereby to convert said dicyclic hydrocarbons to dicyclic ketones, said fraction having been previously prepared by hydrogenation of a cracked petroleum fraction to convert dicyclic hydrocarbons containing two aromatic rings into dicyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring.
  • Process for producing valuable products from petroleum which comprises: contacting a petroleum fraction containing at least 5 weight percent of dicyclic hydrocarbons having one aromatic ring and one cycloaliphatic ring and having alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., inliquid phase with free-oxygen containing gas at a temperature of 150 to 300 F. in the presence'of a metallic oxidation catalyst.;
  • said fraction having been previously prepared by hydrogenation of a cracked petroleum fraction to convert'dicyclic hydrocarbons containing two aromatic rings into dicyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring.
  • a petroleum fraction selected fromthe group consisting of gasoline and motor oil for use in internal combustion engines containing from 0.05 to 5 weight percent of dicyclic hydroxyl compounds produced by contacting a petroleum fraction containing at least 5 weight percent of dicyclic hydrocarbons having one aromatic ring and one cycloaliphatic ring and having alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., in liquid phase with free-oxygen containing gas at a temperature of 150 F. to 300 F.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

OXIDATIGN F PETROLEUM FRACTIONS Archibald P. Stuart, Media, Pa., assignor to Sun Oil Company, Philadelphia, Pa, a corporation of New .lersey No Drawing. Filed Apr. 17, 1957, Ser. No. 653,299
4 Claims. (Cl. 252-55) This invention relates to the preparation of valuable products from cracked petroleum fractions containing dicyclic hydrocarbons. i
In the catalytic cracking of high molecular weight petroleum materials to produce lower molecular weight products, principally gasoline, the products include in addition to gasoline certain higher boiling fractions, generally known as catalytic gas oil, which contain dicyclic hydrocarbons, These higher boiling fractions can be recycled to the cracking operation to obtain gasoline from some ofthe hydrocarbons therein, but some of the hydrocarbons are refractory to cracking and remain in the higher boiling range after the second pass through the cracking operation. Catalytic gas oils are often used only for fuel, and it would be highly desirable to obtain more valuable products from catalytic gas oils obtained after either one or two passes through a catalytic cracking operation.
According to the present invention, valuable products are obtained from catalytic gas oils by hydrogenation thereof and partial oxidation of dicyclic hydrocarbons in the hydrogenation products, which hydrocarbons have one cycloaliphatic ring inthe molecule and one aromatic ring in the molecule. The products of the oxidation are believed to be ketones, the carbon atom of the carbonyl group of which is a member of the cycloaliphatic ring.
The oxygenated compounds which are formed in the partial oxidation are useful as petroleum additives, resin intermediates, etc. They can be removed from the unoxidized hydrocarbons by various methods, such as by extraction of the oxygenated compounds by means of a polar solvent, e.g. ethanol, acetone, furfural, phenol, liquid S0 etc., by selective adsorption of the oxygenated compounds on an adsorbent such as silica gel,'etc.
The partial oxidation according to the invention is not applicable to catalytic gas oils as obtained directly from cracking operations, since such catalytic gas oils generally contain too small amounts of dicyclic compounds containing a cycloaliphatic ring. it is therefore necessary.
to subject the catalytic gas oil to a hydrogenation prior to the oxidation according to the-invention, thereby to convert compounds containing two aromatic rings to di cyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring. Such hydrogenations are known in .the art assuch, and any suitable hydrogenation pro; cedurefor bringing. about this result can be employed.
The oxygenated compounds which are prepared according to the invention are'used, in one embodiment, as
additives for gasoline or motor oil, for the purpose of reducing combustion chamber deposits, in internal combustion engines. 7 compounds employed for such, use is within the approximate range from 0.05 to weight percent based on the hydrocarbon fraction to-which it is added, more preferably 0.1 to Zweightpercent.
Alternatively, the oxygenated compounds can "be re p duc'ed, by.catalytic".hydrogenation orreductionwith-soe.. An'y :suitable hydrogenation catalystcan be e e preferred catalysts b'eing' metals such as cobal molybdium and alcohol or other known procedures, to obtain Preferably the amount of oxygenated I alyst bed per hour, and at a temperature wt n t PatentedMar. 28, 19 61 oxygenated dicyclic compounds in a lesser stage of oxida-] tion, believed to be dicyclic compounds having'a hydroxyl group attached to the cycloaliphatic ring. ,Suchi com: pounds may be employed as additives for gasolineor motor oil, for the purpose of reducing combustion chamber deposits, in proportions similar to those described previously.
Alternatively these oxygenated compounds in a lesser stage of oxidation can be chemically dehydrated accord ing. to known procedures in order to form dicyclic hydrocarbons which differ from the original dicyclic hydro'. carbons in having an olefinicdouble bond in the 1,2 position in' the cyclo aliphatic ring These ultimate dicyclic hydrocarbons can be polymerized or copolyrnerized with other monomers such as butadiene to form synthetic plastics or rubber-like materials.
Theoxidation according to the invention is performed by contacting a suitable fraction containing dicyclic hydrocarbons with a free-oxygen containing gas at a temperature within theapproximate range from 150 F. to- 300 F. in the, presence. of a metallic catalyst of the. well known drier type, e.g. compounds of manganese, cobalt, copper, lead, iron,.etc., e.g. oxides or acetylacetoe mates of such metals, salts of such metals with carboxylic acids such as acetic acid, benzoic .acid, petroleum naphthenic acids, .etc., .Anyk'nown oxidation catalyst ,of, this well knowutype can be employed, Air is the preferred freeroxygen containing gas, althonghisubstantially pure oxygen can be. employed if desired. Any ,knowndiluent for oxygen can be employed if'desiredin the'oxidation.
. The chargestock for the oxidation according to the. inveutionis a hydrogenated petroleum fraction contain.- ing at least 5 weight percent based on charge ofidicyclic. hydrocarbons containing one aromatic ring and one cyclo aliphatic ring. Preferably the charge stock contains at, least 10 percent of such dicyclic hydrocarbons, e.g.;10 to 50 percent. .A major proportion of the charge'stockj boils. within the approximate range from 480 F.i'to
600 F. Preferably, at least l0 percent of the charge. boils below 500 F., and at. least 10 percent above 550 F.
The charge stock can be a hydrogenated cracked petro- 1 leum fraction containing for example 15 to 50 .Weight percent of aromatic hydrocarbons, i.e. hydrocarbons containing atleast one aromatic ring per molecule. .Alterfl natively, it can be a hydrogenated aromaticconcentrat'e'. I from cracked petroleum containing up to percent aromatic hydrocarbons and obtained by extraction with;
a selective solvent for aromatics, e.g. furfural, orselec tive adsorption on a selective adsorbent for aromatics] e.g. silica gel, oraby other known methods. Charge stocks having high aromatic contents'are. preferred; I v i The charge stock contains a large proportionlof'dii cyclic hydrocarbons having'alkyl side chains in themole-1 cule,- The conditions employedin the oxidation as dis'fj closed previously are such that-the principal oXidatiQD j involves carbon atoms in the cycloaliphatic ring,..rathe1r--;' than carbon atoms in alkylside chains. The carbonyl group formeclin the oxidation is, formed. primarily at" the alpha carbon atom of the cycloaliphatic ringin the dicyclic molecule, except'in cases Where that.carb.on atom has an alkyl radical attached thereto.
Anysuitable hydrogenation procedure can be employed priorto the oxidation according tothe invention, Prefer; f ably, the hydrogenationisperformed by passing thecharge K stock downwardly through a bed of solid hydrogenation catalyst at a space rate within the approximate. rang? from 0.25 to 5.0 volumes of charge ,per volume 'of cat denum, nickel, etc., or oxides or sulfides thereof, associated with a suitable carrier, e.g. alumina, bauxite, silica alumina composites. Hydrogenation catalysts for partial hydrogenation of dicyclic aromatic hydrocarbons are well known in the art, and any suitable known catalyst can be employed The hydrogenation should be performed at conditions which produce a maximum amount of dicyclic compounds containing one aromatic ring and one cycloaliphatic ring and a minimum amount of compounds containing two cycloaliphatic rings. Thus the temperature in the hydrogenation should not be substantially greater than 650 F. and the liquid hourly space velocity is preferably at least 1. In the light of the present specification a person skilled in the art can select proper hydrogenation conditions to bring about the desired result in a given instance.
The following examples illustrate the invention:
Example I A hydrogenated first pass catalytic gas oil containing 64 weight percent of saturated hydrocarbons and 36 weight percent of aromatic hydrocarbons, of which 15 weight percent are dicyclic hydrocarbons containing one cycloaliphatic ring and 2 percent are dicyclic hydrocarbons containing two cycloaliphatic rings, which hydrogenated gas oil has refractive index r1 of 1.4879, specific gravity d of 0.8689 and the following Engler distillation in F.:
Initial 440 50 524 5 467 60 536 479 70 551 20 492 80 574 30 504 90 614 40 514 End (94) 628 is contacted in liquid phase with 5 standard cubic feet of air per liter of charge per hour at a temperature of 250 F. and pressure of 100 p.s.i.g. in the presence 'of 0.5 weight percent of manganese benzoate based on charge for a period of 5 hours. The product contains oxygencontaining dicyclic compounds, which are extracted from the unoxidized hydrocarbons by means of ethanol.
The previous hydrogenation was performed at 608 F., 800 p.s.i.g., and liquid hourly space velocity of 0.9 volume per volume of catalyst bed per hour, using a catalyst comprising about 20 percent molybdenum disulfide on alumina. The original first pass catalytic gas oil contained about 62 percent saturates and 38 percent aromatics, of which 3 percent based on charge were dicyclic hydrocarbons containing one cycloaliphatic ring.
The oxygen-containing compounds are separated from the extracting solvent, e.g. ethanol, by dilution of the ethanol solution with water in order to precipitate the oxygen-containing dicyclic compounds.
The recovered oxygen-containing dicyclic compounds are in one embodiment employed as additives for gasoline, e.g. a 90-400" F. commercially available leaded gasoline, for the purpose of reducing combustion chamber deposits, using for example 0.1% of additive material, or as additives for motor oil, e.g.'a commercially available SAE 10W30 oil, for the same purpose and using for example 0.1% of additive material.
In one embodiment, the oxygen-containing dicyclic compounds are reduced to dicyclic compounds having a hydroxyl group attached to a cycloaliphatic ring by suitable procedure for converting cyclic ketones to cyclic hydroxyl compounds. Thus for example the carbonyl compounds can be contacted with hydrogen at 190 F. to 230 F. in the presence of a catalyst comprising copper oxide and chromium oxide for a period sufiicient to convert the carbonyl oxygen to a hydroxyl group. Alternatively, known methods of reduction by hydrogenation with a Raney nickel catalyst can be employed to convert the carbonyl compounds to hydroxyl compounds. The resulting hydroxyl compounds can be employed as additives for gasoline or motor oil in amanner generally simi- 4 lar to that previously described with reference to the carbonyl compound.
The hydroxyl compounds can in one embodiment be dehydrated, for example by contact with alumina at 750 F., to convert the hydroxyl compounds into dehydration products thereof containing a cyclohexene ring and an aromatic ring. These dehydration products have an olefinic double bond in the cycloaliphatic ring in the 1,2 position. They are capable of undergoing vinyl-type addition polymerization at the olefinic double bond. Any suitable known means of bringing about such polymerization can be employed to produce dimers or higher molecular weight vinyl polymers from these unsaturated hydrocarbons. Thus for example they can be polymerized, e.g. at minus 40 F., in dimethyl ether with a sodium naphthalene (C H Na catalyst to produce high molecular weight polymers. The polymer can be recovered from the product mixture by adding water to hydrolyze the sodium compounds and filtering the precipitated polymer. The unsaturated hydrocarbons can also be copolymerized with olefins such as propylene or isobutylene, e.g. at minus 150 F., in butane with 0.5 gram of an aluminum chloride or other Friedel-Crafts catalyst per ml. of monomers.
Such polymers of the unsaturated hydrocarbons can be employed, e.g. in 1% concentration, as viscosity index improving additives for petroleum lubricating oil, e.g. a mixed base oil having Saybolt Universal viscosity at 100 F. of about 100 and viscosity index of about 80 prior to addition of the additive.
Example II In a manner generally similar to that described in Example I, a hydrogenated second pass catalytic gas oil containing about 58 weight percent of saturated hydrocarbons and 42 weight percent of aromatic hydrocarbons of which 20 weight percent are dicyclic hydrocarbons containing one cycloaliphatic ring is partially oxidized in liquid phase to produce oxygen-containing dicyclic compounds which are extracted from the unoxidized hydrocarbons by means of ethanol. The products thus obtained can be further employed in a manner similar to that described in Example I.
The invention claimed is: r
1. Process for producing valuable products from petroleum which comprises; contacting a petroleum'fraction containing at least 5 weight percent of dicyclic hydrocarbons containing one aromatic ring and' one cycloaliphatic ring and containing alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., in liquid phase with free-oxygen containing gas at a temperature of F. to 300 F. in the presence of a metallic oxidation catalyst, thereby to convert said dicyclic hydrocarbons to dicyclic ketones, said fraction having been previously prepared by hydrogenation of a cracked petroleum fraction to convert dicyclic hydrocarbons containing two aromatic rings into dicyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring.
2. A petroleum fraction selected from the group consisting of gasoline and motor oil for use in internal combustion engines containing from 0.05 to 5 weight percent of dicyclic ketones produced according to claim 1, said ketones having one aromatic ring and one cycloaliphatic ring, and having alkyl substituents on nuclear carbon atoms. t
3. Process for producing valuable products from petroleum which comprises: contacting a petroleum fraction containing at least 5 weight percent of dicyclic hydrocarbons having one aromatic ring and one cycloaliphatic ring and having alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., inliquid phase with free-oxygen containing gas at a temperature of 150 to 300 F. in the presence'of a metallic oxidation catalyst.;
thereby to convert said dicyclic hydrocarbons to dicyclic ketones, and subsequently reducing said dicyclic ketones to dicyclic hydroxyl compounds, said fraction having been previously prepared by hydrogenation of a cracked petroleum fraction to convert'dicyclic hydrocarbons containing two aromatic rings into dicyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring.
4. A petroleum fraction selected fromthe group consisting of gasoline and motor oil for use in internal combustion engines, containing from 0.05 to 5 weight percent of dicyclic hydroxyl compounds produced by contacting a petroleum fraction containing at least 5 weight percent of dicyclic hydrocarbons having one aromatic ring and one cycloaliphatic ring and having alkyl substituents on nuclear carbon atoms, a major proportion of which fraction boils within the range from 480 F. to 600 F., in liquid phase with free-oxygen containing gas at a temperature of 150 F. to 300 F. in the presence of a metallic oxidation catalyst, thereby to convert said dicyclic hydrocarbons to dicyclic ketones having one aromatic ring and one cycloaliphatic ring and having alkyl substituents on nuclear carbon atoms, and subsequently reducing said dicyclic ketones to dicyclic hydroxyl compounds, said fraction having been previously prepared by hydrogenation of a cracked petroleum fraction to convert dicyclic hydrocarbons containing two aromatic rings into dicyclic hydrocarbons containing one aromatic ring and one cycloaliphatic ring.
References Cited in the file of this patent UNITED STATES PATENTS OTHER REFERENCES Chemistry of Organic Compounds, Noller, 1951, W. B. Saunders Co., page 558.

Claims (2)

1. PROCESS FOR PRODUCING VALUABLE PRODUCTS FROM PETROLEUM WHICH COMPRISES: CONTACTING A PETROLEUM FRACTION CONTAINING AT LEAST 5 WEIGHT PERCENT OF DICYCLIC HYDROCARBONS CONTAINING ONE AROMATIC RING AND ONE CYCLOALIPHATIC RING AND CONTAINING ALKYL SUBSTITUENTS ON NUCLEAR CARBON ATOMS, A MAJOR PROPORTION OF WHICH FRACTION BOILS WITHIN THE RANGE FROM 480*F. TO 600*F., IN LIQUID PHASE WITH FREE-OXYGEN CONTAINING GAS AT A TEMPERATURE OF 150*F. TO 300*F. IN THE PRESENCE OF A METALLIC OXIDATION CATALYST, THEREBY TO CONVERT SAID DICYCLIC HYDROCARBONS TO DICYCLIC KETONES, SAID FRACTION HAVING BEEN PREVIOUSLY PREPARED BY HYDROGENATION OF A CRACKED PETROLEUM FRACTION TO CONVERT DICYCLIC HYDROCARBONS CONTAINING TWO AROMATIC RINGS INTO DICYCLIC HYDROCARBONS CONTAINING ONE AROMATIC RING AND ONE CYCLOALIPHATIC RING.
3. PROCESS FOR PRODUCING VALUABLE PRODUCTS FROM PETROLEUM WHICH COMPRISES: CONTACTING A PETROLEUM FRACTION CONTAINING AT LEAST 5 WEIGHT PERCENT OF DICYCLIC HYDROCARBONS HAVING ONE AROMATIC RING AND ONE CYCLOALIPHATIC RING AND HAVING ALKYL SUBSTITUENTS ON NUCLEAR CARBON ATOMS, A MAJOR PROPORTION OF WHICH FRACTION BOILS WITHIN THE RANGE FROM 480*F. TO 600*F., IN LIQUID PHASE WITH FREE-OXYGEN CONTAINING GAS AT A TEMPERATURE OF 150*F. TO 300*F. IN THE PRESENCE OF A METALLIC OXIDATION CATALYST, THEREBY TO CONVERT SAID DICYCLIC HYDROCARBONS TO DICYCLIC KETONES, AND SUBSEQUENTLY REDUCING SAID DICYCLIC KETONES TO DICYCLIC HYDROXYL COMPOUNDS, SAID FRACTION HAVING BEEN PREVIOUSLY PREPARED BY HYDROGENATION OF A CRACKED PETROLEUM FRACTION TO CONVERT DICYCLIC HYDROCARBONS CONTAINING TWO AROMATIC RINGS INTO DICYCLIC HYDROCARBONS CONTAINING ONE AROMATIC RING AND ONE CYCLOALIPHATIC RING.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3381785A (en) * 1966-10-26 1968-05-07 Charles A. Mendenhall Combined coil mounting and bearing for an electromagnetic clutch
US4105843A (en) * 1976-04-15 1978-08-08 Mitsui Petrochemical Industries Ltd. Process for producing hydrocarbon resins having improved color and thermal stability by heat treatment with an α,βunsaturated anhydride

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GB542834A (en) * 1938-12-03 1942-01-29 Standard Oil Dev Co An improved method of decreasing metal corrosion
US2422247A (en) * 1940-12-27 1947-06-17 Standard Oil Dev Co Lubricants, etc., containing waxy hydrocarbons and a ketone-aromatic condensation product as wax modifier
US2462103A (en) * 1946-03-23 1949-02-22 Koppers Co Inc Preparation of alpha-ketodihydronaphthalene
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