US2115781A - Process for the treatment of stored cracked gasoline - Google Patents
Process for the treatment of stored cracked gasoline Download PDFInfo
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- US2115781A US2115781A US752707A US75270734A US2115781A US 2115781 A US2115781 A US 2115781A US 752707 A US752707 A US 752707A US 75270734 A US75270734 A US 75270734A US 2115781 A US2115781 A US 2115781A
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- gasoline
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- 238000011282 treatment Methods 0.000 title description 15
- 238000000034 method Methods 0.000 title description 13
- 230000008569 process Effects 0.000 title description 11
- 150000003839 salts Chemical class 0.000 description 18
- 239000000446 fuel Substances 0.000 description 13
- 150000002978 peroxides Chemical class 0.000 description 9
- 239000000243 solution Substances 0.000 description 8
- 230000001603 reducing effect Effects 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 150000007513 acids Chemical class 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910021591 Copper(I) chloride Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 229940045803 cuprous chloride Drugs 0.000 description 1
- 150000001993 dienes Chemical class 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229960002089 ferrous chloride Drugs 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- -1 halogen acids Chemical class 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- NMCUIPGRVMDVDB-UHFFFAOYSA-L iron dichloride Chemical compound Cl[Fe]Cl NMCUIPGRVMDVDB-UHFFFAOYSA-L 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- 150000002926 oxygen Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000012260 resinous material Substances 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052716 thallium Inorganic materials 0.000 description 1
- BKVIYDNLLOSFOA-UHFFFAOYSA-N thallium Chemical compound [Tl] BKVIYDNLLOSFOA-UHFFFAOYSA-N 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/06—Metal salts, or metal salts deposited on a carrier
- C10G29/12—Halides
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/06—Metal salts, or metal salts deposited on a carrier
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/06—Metal salts, or metal salts deposited on a carrier
- C10G29/08—Metal salts, or metal salts deposited on a carrier containing the metal in the lower valency
Definitions
- the anti-knock property of a gasoline is among its most important and valuable characteristics which have a tendency to depreciate under average storage conditions in refineries. Knocking in a motor is evidenced by a pinging metallic sound which is accompanied by a reduction in the efliciency of the motor and in the mileage obtained per gallon of the fuel.
- the use of agents or kinds of motor fuel which prevent knocking adds to the efliciency of the motor and the motor fuell
- the rate at which different hydrocarbon motor fuels deteriorate on storage in' respect to their valuable properties varies markedly with the chemical characteristics of the fuel which depend in turn upon the nature of the on distilled or oil.
- the present process comprises a method of treatment for restoring as far as possible the valuable properties of motor fuels which have been lost on storage.
- the present invention comprises the treatment of materially deteriorated motor fuels with selected inorganic salts having a reducing action.
- the salts may be used either as solids or in solution.
- the restoration of properties involving the substantially complete elimination of peroxides, the partial reduction of aldehydes, alcohols and acids and the depolymerization of high boiling polymers may be accomplished according to the present invention by treatment with solutions (generally aqueous) of various inorganic metal salts in which the metal exhibits its lower valence.
- solutions generally aqueous
- the salts may be used in the solid form. This point will be discussed further in later paragraphs.
- Such salts are usually known as the ous salts and the different salts included in this category have the general property of absorbing oiwgen or other elements and assuming a higher valence.
- metals having reducing salts which are well known and as a rule easily available may be mentioned iron, tin, chromium, nickel, cobalt, cerium, copper, manganese, mercury and thallium.
- the use of salts of the commoner acids, such as the halogen acids and sulfuric acid will be preferable since these can be used with varying degrees of efliciency without having recourse to rarer and pos-' sibly more expensive compounds.
- the solubility of these reducing salts in water varies considerably .and in the case of any one salt there will be an optimum concentration in water, a definite temperature andagdefinite volume of solution corresponding to most effective treatment. It is not intended to infer that salts which may be used alternatively have identical treating effects, this fact being more or less obvious to chemists.
- reducing salts which may be used within the concepts of the present invention include certain *arsenites, antimonites andphosphites, usually of the alkali metals since these have sufficient solubility in water at ordinary q temperatures to make possible the use of treating solutions of good efllciency. It is within the scope of the invention also to use ferrocyanides 'in case their solubility in water is great enough.
- the operations of treatment for restoring properties of deteriorated gasolines by the present process are relatively simple and when solutions of salts are used may be conducted in the same general types of-equipment as are ordinarily employed in treating oils with liquid reagents such as sulfuric acid, caustic soda and sweetening and washing solutions.
- a solution of a reducing salt may be agitated with a deteriorated gasoline in the ordinary type of batch agitator usingmechanical stirring devices or circulation from the bottom of the agitator back into the top'by means of outside force pumps.
- solutions may also be used in continuous treat ing plants consisting of a series ofconnected units each comprising a mixer followed by a settling tank from the bottom of which spent or partly spent aqueous reagents are drawn and the treated liquids are discharged from the top.
- the process is not limited to the use of any particular type of mechanical equipment.
- the solid may be agitated with the gasoline to be treated either at ordinary or elevated temperatures. (using refluxing or increased pressures to prevent loss of light constituents), or the gasoline may be filtered through granular beds of reducing salts. Each employed as desired.
- the present process may also be employed in conjunction with any other treatments which may be considered necessary or of advantage in bringing aged stocks back as nearly as possible to their original values.
- Analytical data indicate that the principal action of reducing agents of the present character on stored distillates is to deoxidize the same, to eliminate peroxides and to some extent the compounds in which the oxygen is in more stable combination such as the aldehydes, alcohols and acids already mentioned. It is seldom possible to depolymerize to any great extent and in case gummy or resinous materials have "been formed in relatively large amounts, redistillation following the treatments will be necessary, in which step the materials boiling above the desired endpoint of the finished gasoline remain as a heavy reflux in the fractionator.
- the present process oifers a definite supplementary treatment which renders stocks otherwise not susceptible to inhibition capable of proper response.
- a deteriorated cracked gasoline was treated granular ferrous chloride used in an amount of significantproperties of the gasoline before and after this treatment are given in the-following table: a
- Example I The same gasoline as in Example I was treated with solid cuprous chloride. In this case-itwas found that after agitation for about'24 hours at ordinary. temperatures that the peroxide number was substantially zero while the color and antisuits of this treatment are again tabulated beknock value had been restored the same as in low: Example I.
- Example III the same deteriorated gasoline used in Example III was treated with about 5% by' volume of a saturated solution of stannous chlov ride which contained no stannic salt.
- the features and advantages of the present process are obvious from a consideration of the preceding specification and numerical data pre-p peroxides, and separating any unconsumed quantity of said salt and the reaction products from the thus treated gasoline.
Landscapes
- 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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Patented May 3, 1938 PROCESS FOR THE TREATMENT OF STORED CRACKED GASOLINE Jacque C. Morrell, Chicago, Ill., assignor to Universal Oil Products Company, Chicago, 111., a corporation of Delaware Application November 12, 1984, Serial No. 752,707 a '1 Claim. (01. 196-43) This invention relates more particularly to the treatment of unstable gasolines whose properties have deteriorated on storage due to oxidation,
polymerization and other reactions among their constituents, the present application being a continuation in part of my earlier applicationSerial No. 406,514 filed Nov. 11, 1929.
It has been observed that when motor fuels or gasolines are stored, particularly cracked gasolines, and especially under the influence-of light and oxygen, chemical changes occur which aflect color, increase the gum formation, and reduce the anti-knock properties. The chemistry of these changes is somewhat obscure, although in practically all cases oxidation promotes these depreciatin'g effects which occur upon storage. Cracked gasolines contain a relatively high percentage of unsaturated hydrocarbons, and it is believed that the changes whichoccur in the properties of the motor fuel during storage are related to chemical changes in these unsaturated hydrocarbons, especially in the more highly unsaturated groups, for example, the diolefins.
The formation of color in gasoline is undesirable because changes in color areusually accompanied by the formation of gum and tar-like substances which affect not only the sales value of the motor fuel, but also its performance in the operationof the motor, particularly in clogging up the gasoline feed lines, the moving parts of the carburetor and causing the sticking of valves in the motor. The development of more intense coloration is very undesirable from a sales standpoint as a small change in intensity makes a great diflerence in the appearance of gasoline in glass pump bowls.
The anti-knock property of a gasoline is among its most important and valuable characteristics which have a tendency to depreciate under average storage conditions in refineries. Knocking in a motor is evidenced by a pinging metallic sound which is accompanied by a reduction in the efliciency of the motor and in the mileage obtained per gallon of the fuel. The use of agents or kinds of motor fuel which prevent knocking adds to the efliciency of the motor and the motor fuell The rate at which different hydrocarbon motor fuels deteriorate on storage in' respect to their valuable properties varies markedly with the chemical characteristics of the fuel which depend in turn upon the nature of the on distilled or oil.
cracked and the conditions of cracking'in the case 'of cracked gasolines. The presence of relatively small quantities of nitrogen, sulfur and oxygen derivatives of hydrocarbons may also influence the rate of deterioration. In refinery practice it may be most economical to produce and store con-' siderable quantities of motor fuel during the seasons when consumption of gasoline is low, so that it frequently happens that stocks are stored for abnormally longperiods. In such cases considerable deterioration may ensue, particularly if the storage tanks are not full and there is considerable breathing" in the vapor space above the The present process comprises a method of treatment for restoring as far as possible the valuable properties of motor fuels which have been lost on storage.
In one specific embodiment the present invention comprises the treatment of materially deteriorated motor fuels with selected inorganic salts having a reducing action. The saltsmay be used either as solids or in solution.
A large amount of experimental and analytical 7 work has shown the approximate course of the reactions which lead ultimately to the loss in color and anti-knock value and the increase'in gums commonly observed in anti-knock 'motor fuels which have'been stored for considerable periods of time. It is .quite well established that the -'primary reaction which instigates the later changes consists in the addition of oxygen to olefins containing conjugated double bonds" to form organic peroxides. At first the formation of these compounds is relatively-slow but as they accumulate and their total percentage exceeds some definite value, the rate of formation is considerably accelerated-so that the process becomes autocatalytic and not only hastens the formation of further quantities of peroxides but exerts, a pronounced polymerizing eflect upon olefins and other polymerizable compounds. In addition,
'. tam-considerable quantities of peroxides. The
presence of these peroxides in a motor fuel tends to accelerate combustion and increase the knocking propensities of the fuel.
The restoration of properties, involving the substantially complete elimination of peroxides, the partial reduction of aldehydes, alcohols and acids and the depolymerization of high boiling polymers may be accomplished according to the present invention by treatment with solutions (generally aqueous) of various inorganic metal salts in which the metal exhibits its lower valence. In some cases the salts may be used in the solid form. This point will be discussed further in later paragraphs. Such salts are usually known as the ous salts and the different salts included in this category have the general property of absorbing oiwgen or other elements and assuming a higher valence. v
As examples of metals having reducing salts which are well known and as a rule easily available may be mentioned iron, tin, chromium, nickel, cobalt, cerium, copper, manganese, mercury and thallium. As a general rule, the use of salts of the commoner acids, such as the halogen acids and sulfuric acid will be preferable since these can be used with varying degrees of efliciency without having recourse to rarer and pos-' sibly more expensive compounds. The solubility of these reducing salts in water varies considerably .and in the case of any one salt there will be an optimum concentration in water, a definite temperature andagdefinite volume of solution corresponding to most effective treatment. It is not intended to infer that salts which may be used alternatively have identical treating effects, this fact being more or less obvious to chemists.
Other groups of reducing salts which may be used within the concepts of the present invention include certain *arsenites, antimonites andphosphites, usually of the alkali metals since these have sufficient solubility in water at ordinary q temperatures to make possible the use of treating solutions of good efllciency. It is within the scope of the invention also to use ferrocyanides 'in case their solubility in water is great enough.
The operations of treatment for restoring properties of deteriorated gasolines by the present process are relatively simple and when solutions of salts are used may be conducted in the same general types of-equipment as are ordinarily employed in treating oils with liquid reagents such as sulfuric acid, caustic soda and sweetening and washing solutions. For example, a solution of a reducing salt may be agitated with a deteriorated gasoline in the ordinary type of batch agitator usingmechanical stirring devices or circulation from the bottom of the agitator back into the top'by means of outside force pumps. The
solutions may also be used in continuous treat ing plants consisting of a series ofconnected units each comprising a mixer followed by a settling tank from the bottom of which spent or partly spent aqueous reagents are drawn and the treated liquids are discharged from the top. In other words, the process is not limited to the use of any particular type of mechanical equipment.
As an alternative mode of procedure it may sometimes be convenient and practical to effect the desired reducing treatments using finely d1- vided solid salts. In such cases the solid may be agitated with the gasoline to be treated either at ordinary or elevated temperatures. (using refluxing or increased pressures to prevent loss of light constituents), or the gasoline may be filtered through granular beds of reducing salts. Each employed as desired.
The present process may also be employed in conjunction with any other treatments which may be considered necessary or of advantage in bringing aged stocks back as nearly as possible to their original values. Analytical data indicate that the principal action of reducing agents of the present character on stored distillates is to deoxidize the same, to eliminate peroxides and to some extent the compounds in which the oxygen is in more stable combination such as the aldehydes, alcohols and acids already mentioned. It is seldom possible to depolymerize to any great extent and in case gummy or resinous materials have "been formed in relatively large amounts, redistillation following the treatments will be necessary, in which step the materials boiling above the desired endpoint of the finished gasoline remain as a heavy reflux in the fractionator.
It is a feature of the present invention that its greatest value lies in its application to unstable gasoline stocks which have suffered more or less serious deterioration in their properties.
amounts of reactive oxygen. Since the amount' of inhibitor which may be used is limited by such considerations as the cost of the material, the residue formed on evaporation, possible color effects, et cetera, the present process oifers a definite supplementary treatment which renders stocks otherwise not susceptible to inhibition capable of proper response.
The following examples are given to indicate the general character of treating effects obtainable in thepractical application of the present process and while they are illustrative they are selected from a considerable number and they are not given with the intent of limiting the scope of the invention to the specific instances presented:
A deteriorated cracked gasoline was treated granular ferrous chloride used in an amount of significantproperties of the gasoline before and after this treatment are given in the-following table: a
V I Y Before treattreat- PNMY- m; t
Puoxidenumbersn fl. 5.4 1.0 Color; Saybolt Light yellow 26 Octanenumbu' an Example II by agitation at ordinary temperatures with 7 about 1% of the weight of the gasoline. The
The same gasoline as in Example I was treated with solid cuprous chloride. In this case-itwas found that after agitation for about'24 hours at ordinary. temperatures that the peroxide number was substantially zero while the color and antisuits of this treatment are again tabulated beknock value had been restored the same as in low: Example I.
4 Example III Properties B81256 em- A Mid-Continent cracked gasoline which had been stored for a considerable time was found Peroxide number as 0.00 to have deteriorated considerably in respect to 8g{,' ggggg;;;; gum content, anti-knock value and color. It
had a peroxide number of 6.3. This deteriorated gasoline was treated at ordinary temperatures with about 10% by volume of a saturated solution of ferrous sulfate. The significant properties before and after treatment are again given in the following table:
In this case the same deteriorated gasoline used in Example III was treated with about 5% by' volume of a saturated solution of stannous chlov ride which contained no stannic salt. The re- The features and advantages of the present process are obvious from a consideration of the preceding specification and numerical data pre-p peroxides, and separating any unconsumed quantity of said salt and the reaction products from the thus treated gasoline.
JACQUE C. MORREIL'.
said process comprising
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US752707A US2115781A (en) | 1934-11-12 | 1934-11-12 | Process for the treatment of stored cracked gasoline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US752707A US2115781A (en) | 1934-11-12 | 1934-11-12 | Process for the treatment of stored cracked gasoline |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2115781A true US2115781A (en) | 1938-05-03 |
Family
ID=25027451
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US752707A Expired - Lifetime US2115781A (en) | 1934-11-12 | 1934-11-12 | Process for the treatment of stored cracked gasoline |
Country Status (1)
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| US (1) | US2115781A (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2427212A (en) * | 1944-12-02 | 1947-09-09 | Pure Oil Co | Removal of peroxides from hydrocarbon oils |
| US2433033A (en) * | 1942-11-13 | 1947-12-23 | Standard Oil Dev Co | Stabilization of motor fuels |
| US2445367A (en) * | 1944-05-26 | 1948-07-20 | Standard Oil Dev Co | Method of stabilizing hydrocarbons |
| US2523549A (en) * | 1946-06-10 | 1950-09-26 | Phillips Petroleum Co | Deoxygenation of hydrocarbons |
| US2542471A (en) * | 1946-06-15 | 1951-02-20 | Standard Oil Dev Co | Removal of peroxides from cracked gasoline by catalytic hydrogenation |
| US2545199A (en) * | 1947-12-13 | 1951-03-13 | Shell Dev | Removal of peroxides from hydrocarbons |
| US2552670A (en) * | 1951-05-15 | Purification of cyclic ketones | ||
| US2563598A (en) * | 1951-08-07 | Removal of peroxides from hydro | ||
| US2565354A (en) * | 1948-01-14 | 1951-08-21 | Standard Oil Dev Co | Chemical process for removal of organic peroxides |
| DE958328C (en) * | 1952-12-09 | 1957-02-14 | Siemens Ag | Antioxidant for insulating oils |
| US3306846A (en) * | 1964-01-03 | 1967-02-28 | Shell Oil Co | Peroxide removal using lead dioxide or manganese dioxide |
-
1934
- 1934-11-12 US US752707A patent/US2115781A/en not_active Expired - Lifetime
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2552670A (en) * | 1951-05-15 | Purification of cyclic ketones | ||
| US2563598A (en) * | 1951-08-07 | Removal of peroxides from hydro | ||
| US2433033A (en) * | 1942-11-13 | 1947-12-23 | Standard Oil Dev Co | Stabilization of motor fuels |
| US2445367A (en) * | 1944-05-26 | 1948-07-20 | Standard Oil Dev Co | Method of stabilizing hydrocarbons |
| US2427212A (en) * | 1944-12-02 | 1947-09-09 | Pure Oil Co | Removal of peroxides from hydrocarbon oils |
| US2523549A (en) * | 1946-06-10 | 1950-09-26 | Phillips Petroleum Co | Deoxygenation of hydrocarbons |
| US2542471A (en) * | 1946-06-15 | 1951-02-20 | Standard Oil Dev Co | Removal of peroxides from cracked gasoline by catalytic hydrogenation |
| US2545199A (en) * | 1947-12-13 | 1951-03-13 | Shell Dev | Removal of peroxides from hydrocarbons |
| US2565354A (en) * | 1948-01-14 | 1951-08-21 | Standard Oil Dev Co | Chemical process for removal of organic peroxides |
| DE958328C (en) * | 1952-12-09 | 1957-02-14 | Siemens Ag | Antioxidant for insulating oils |
| US3306846A (en) * | 1964-01-03 | 1967-02-28 | Shell Oil Co | Peroxide removal using lead dioxide or manganese dioxide |
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