US2379228A - Diesel fuel - Google Patents

Diesel fuel Download PDF

Info

Publication number
US2379228A
US2379228A US432629A US43262942A US2379228A US 2379228 A US2379228 A US 2379228A US 432629 A US432629 A US 432629A US 43262942 A US43262942 A US 43262942A US 2379228 A US2379228 A US 2379228A
Authority
US
United States
Prior art keywords
hypochlorite
oil
fuel
sulfur
ignition
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US432629A
Inventor
George R Gilbert
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to US432629A priority Critical patent/US2379228A/en
Application granted granted Critical
Publication of US2379228A publication Critical patent/US2379228A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2493Organic compounds containing sulfur, selenium and/or tellurium compounds of uncertain formula; reactions of organic compounds (hydrocarbons, acids, esters) with sulfur or sulfur containing compounds
    • 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

Definitions

  • an inorganic hypochlorite ostensibly reacts' with mercaptans and forms ignition accelerating com-pounds which are more potent than organic di-. and polysulfides.
  • the reaction, of the hypochlorite agent gave results far superior to those obtained by treating mercaptan-enriched Diesel fuels with a doctor solution (sodium plumbite) or its modifications.
  • the process of the present invention is suitably applied to petroleum gas oil which meets requirements of'Diesel fuel specifications and with very little mercaptan sulfur present before the treatment with the hypochlorite solution.
  • the hypochlorite treating solution may be prepared by chlorination of a causticalkali solution, but other convenient methods may be used. In a satisfactory treatment, the treating solution is maintained alkaline, the hypochlorite solution is intimately mixed in a minor proportion with the fuel at a suitably elevated temperature until the desired improvement of iging aremarkably improved cetane rating is obtallied.
  • I have chemical analysis of the product treated in accordance with .my invention that very-little, if am, chlorination of the fuel takes place but that aoertain change in chemical properties is effected.
  • hypochlorite, solution . was prepared by bubbling chlorine gas thru approximately 20 B. aqueous NaOH solution which was cooled in an ice bath to prevent an excessive rise in temperature.
  • the anlysis of the. prepared solution showed about 4.66 weight per cent available chlorine, 7.40 weight per cent NaOH, and 8.88 weight per cent total sodium content.
  • Teri liters of gas oil hydrocarbons containing about 3 mg. of mercaptan sulfur per ml. of oil and having a total sulphur content of 0.22% by weight by bomb analysis were agitated with two liters of the hypochlorite solutionfor30min.atabout200'-1".to 210 F.in a closed iron agitator. (turbo-miner). After separating the oil from the partially spent hypochlorite solution by settling, the oil product was washed with two 10 liter batches of hot water and wasthen nltered thru paper.
  • Thefuel oil was memcauy analysed before and after thetreatment to determine the action of the hypoohlorite agent on the composition.
  • the active ignition promoting compound formed gave a much-higher octane number creasethan could be'acoounted foronabasis is also possible that other reactive components 0! the 11181, ll hydrocarbons.
  • Example I The hypochlorite solution described in Example I was employed to treat three separate portions of gas oil whose physical and chemical characteristics have also been described therein. Ten liter portions of gas oil were agitated with two liter portions of hypochlorite solution while maintaining all conditions, except temperature, exactly as hasbeen outlined in the preceding example. In this case, one 10 liter portion of oil was treated with hypochlorite at'80' 1'. The second 10 liters were treated at temperatures between about I". and 1". and the third 10 liter portion at temperatures of about 200 I. to 210' F. After separating the oil from the partially spent hypochlorite solution by settlins, each treated 10 liter portion was washed separately with 10 liter batches of hot water and then iiltered through paper.
  • Diesel fuels treated in the at high temperatures with the presence of mercaptan of high octane ratin manner described solution may be used as such or may be blended with an untreated Diesel fuel stock to form a blend having improved ignition quality.
  • gas oils which are practically sweet, or which have been partly desulfurized or sweetened by any suitable refining method even though the hypochlorite is capable of eflecting some elimination of mercaptan sulfur when accomplishing the desired improvement in ignition quality.
  • the present process was found to effect a substantial ignition quality of gas oils which contained practically no reactive sulfur (free sulfur or polysulfide sulfur), and also, it was found eflective for increasing the cetane numbers of sour and cracked gas oils having high sulfur contents without making any decided desulfurization.
  • a preferred starting oil for the ignition quality improving treatment is a gas oil that while treating the or similar high boiling petroleum fractionboilin: mainly above 450 F. with an end point below 150' E. with a sulfur content within specification limits, such as below 1%, and with a mercaptan suigiglc zntent less than 0.05%, e. g., about 0.001% to
  • caustic soda is preferred for use in the hypochlorite solution, being the most practical, other metals may be used in the reagent, e. g., aluminum, zinc, magnesium. iron, copper, potassium, or calcium.
  • One of the additional modifications which may be carried out is to use with the hypochlorlte treating agent a small amount of an oxidizing agent or a chlorinating sc such as chlorine gas. hypwmorous acid,
  • the treating conditions may be influenced by exposure of the reaction mixture-to light, varying the intensity of agitation and varying the time of coming within the scope of be included therein.
  • reaction may be purification treatments, such with adsorbents. or the, like.
  • the method ofimproving a Diesel fuel which comprises reacting a mercaptan with an inorganic hypochlorite to form an oil-soluble ignition accelerator possessing oxidizing potency of incorporating said accelerator fuel oil adapted for operation active oxygen and into a petroleum followed bxvariousthe invention are to GEORGE R. GILBERT.

Description

patented a... as, ices entree snares mist.
. DESELFUM;
George h. Gilbert, hiaytown, 'lem, assig'nor to Standard @ii Development Company,
ration of Delaware Ne Drawing. Application February 27,1942,
Serial No; 432,629
1 Claim. (oi. 44- 57) This'invention isconcerned with improving combustion characteristics of high boiling fuel oils, more particularly with improving the ignition quality of Diesel fuel oils by a reaction of an inorganic hypochlorite.
It has the object of providing a method for,
efiectively increasing the ignition quality of Diesel fuels with some elimination of objectionable mercaptans from the fuel oils.
Other objects and advantages of the invention tvivill be made apparent by the following descrippolysulfide compounds were found to be fairly efiective ignition accelerators in Diesel fuels and that it has been proposed to use a doctor sweetening treatment on sour Diesel fuels having a high mercaptan content with an excess of added It is known that elementary sulfur and certain clearly understood; but it is believed that the active ingredients of the solution (oxygen and chlorine) react with mercaptans and possibly other components of the fuel to form a product insitu which contributes to the superior ignition qualities observed. However, it is to be clearly understood that nay-invention is not to be limited to any theory advanced in explanation thereof.
In the presentinvention, an inorganic hypochlorite ostensibly reacts' with mercaptans and forms ignition accelerating com-pounds which are more potent than organic di-. and polysulfides. The reaction, of the hypochlorite agent gave results far superior to those obtained by treating mercaptan-enriched Diesel fuels with a doctor solution (sodium plumbite) or its modifications.
' It does, not require addition of free sulfur. It
sulfur to convert the mercaptans into ignition accelerating organic polysulfldes. Howeventhe practical use-of thesetreatments is hampered by (1) common fuel specifications limiting the total sulfur content of the fuels, and (2) the corrosive action of the sulfur incorporated into the fuel. It has also been Mom to subject certain mineral oil fractions, primarilystraight run gasoline and similar light non-cracked products, to the treating action of an aqueous alkaline hypochlorite solution. In sweetening such petroleum oil fractions with hypochlorite solutions, particularly solutions of sodium and calcium hypochlorite,
'forbcst results it was considered necessary to became regarded as entirely unjustifiable.
Now I have found that if a Diesel fuel oil is treated with an aqueous alkaline hypochlorite solution at elevated temperatures,.a product havhas given satisfactory results when applied to fuels containing very low concentrations of mer-' captans. It has been found to work wellon fu'els of low sulfur content. If desired, the hypochlo rite may be reacted with a. mercaptan to form an ignitionaccelerator compound soluble in Diesel fuel and the reaction product incorporated in a Diesel fuel.
As a specific embodiment, the process of the present invention is suitably applied to petroleum gas oil which meets requirements of'Diesel fuel specifications and with very little mercaptan sulfur present before the treatment with the hypochlorite solution. The hypochlorite treating solution may be prepared by chlorination of a causticalkali solution, but other convenient methods may be used. In a satisfactory treatment, the treating solution is maintained alkaline, the hypochlorite solution is intimately mixed in a minor proportion with the fuel at a suitably elevated temperature until the desired improvement of iging aremarkably improved cetane rating is obtallied. Furthermore, I have chemical analysis of the product treated in accordance with .my invention that very-little, if am, chlorination of the fuel takes place but that aoertain change in chemical properties is effected.
The reason forthls unexpected result is not 36- determined by nition quality is obtained, and thereafter, the treated fuel is water-washed.
The process is illustrated by the followinggspecific examples: v A
'The hypochlorite, solution .was prepared by bubbling chlorine gas thru approximately 20 B. aqueous NaOH solution which was cooled in an ice bath to prevent an excessive rise in temperature. 'The anlysis of the. prepared solution showed about 4.66 weight per cent available chlorine, 7.40 weight per cent NaOH, and 8.88 weight per cent total sodium content. Teri liters of gas oil hydrocarbons containing about 3 mg. of mercaptan sulfur per ml. of oil and having a total sulphur content of 0.22% by weight by bomb analysis were agitated with two liters of the hypochlorite solutionfor30min.atabout200'-1".to 210 F.in a closed iron agitator. (turbo-miner). After separating the oil from the partially spent hypochlorite solution by settling, the oil product was washed with two 10 liter batches of hot water and wasthen nltered thru paper.
Inspections of the oil before and after the treat ment are summarized in the following table:
, Table 1 W Hypochlorite I on treate t l gas ' Octane n -J. 66.4 (60 62.6 64
0rsvity,A.P T 81 37.3. I. B. P "I All 446. was}. 'r m m. I. 2.. 630 636. Via. 100' l". (B. U. 8.) 1, 871 88.0. Glen .4. B. 'i.-M., '1 14. Pour, I 10 10. M, PM, F m 218. Bomb sultunpccent 0.22 0.20.
. Cu strip corrosion, 8 hrs. 0 212 '11..-. Barely pass. Pass.
Chlorine content per cen 0 0. Odor Mercaptaus. Sweet. Doctor test N. G Essa.
Msrosptsn sultur, mg./10o ml 3.0- 0. s.
Thefuel oil was memcauy analysed before and after thetreatment to determine the action of the hypoohlorite agent on the composition.
The results aresummarised as follows:
These analytical results indicate that the treatment can be carried out without appreciable chlorination of the fuel components and without making any substantial change of the sulphur content'in giving the fuel the remarkably good increase of about 7 oetane number units. The high order of ignition quality improvement thus obtained can be appreciated by comparison with aavaaas which is indicative of the formation of substances similar to peroxides in potent oxidising properties. The peroxide number is a well known test mmin parenthesis are results obtained at a diiimntlsbon- Y the eifectiveness ofvarious s tion accelerator additions, even' the outstanding alkyl nitrates.
Moreover, this extraordinary octane number increase doesnotentailanymaterialreductionin heating value, since the hydrogen and as in the use of previously contsntisnot-lowered known additives.
The active ignition promoting compound formed gave a much-higher octane number creasethan could be'acoounted foronabasis is also possible that other reactive components 0! the 11181, ll hydrocarbons. parti ipate in reactionto form the ignition promoting sub- Itisofmteresttonotethatthetreatmeptmade a significant increase in the peroxide number,
such as of the order of 0.01%, which does not show up in ordinary chemical analyses. Thus, it is possible that active oxygen or some other active oxidizing function is introduced into the fuel in extremely smallamounts. In gasoline motor fuels, low peroxide numbers of 1-3 are obtained when such fuels are very unstable and undergo rapid deterioration with gum formation, but high peroxide number Diesel fuel products prepared in accordance with the presmt invention, i. e., with peroxide numbers above 3, were found to be satisfactorily stable. The mercury number'increase may also be regarded as indicating the same change as shown by the peroxide number increase. Taking these changes into consideration it is evident that the amount of the active ignition acelerating'ingredient formed in'the fuel to make a cetane number increase of 6 to 7 is less than about 0.1%.
The hypochlorite solution described in Example I was employed to treat three separate portions of gas oil whose physical and chemical characteristics have also been described therein. Ten liter portions of gas oil were agitated with two liter portions of hypochlorite solution while maintaining all conditions, except temperature, exactly as hasbeen outlined in the preceding example. In this case, one 10 liter portion of oil was treated with hypochlorite at'80' 1'. The second 10 liters were treated at temperatures between about I". and 1". and the third 10 liter portion at temperatures of about 200 I. to 210' F. After separating the oil from the partially spent hypochlorite solution by settlins, each treated 10 liter portion was washed separately with 10 liter batches of hot water and then iiltered through paper.
Cetane numbers of the several portions of oil after treatment at the varying temperatures tures, as compared with usual pracflce for sw eningnaphtha, the cetane rating was raised approximately 7 units over that of the original oil.
' Whentreatingoilsatrelativeiy-low 'e.g.,80'i".,anincreaseofonly1unitwaseffected. Therefore, it is omchlded that treating Diesel fuel oils in accordance with'my invmtion 'IsresultsinamarkedbsuperlornoductirtnetegnJ- with an alkaline hypochlorite improvement in the Since with the present ment of ignition'quality is not essentialiy.ac-
elevated to above 80' E, and the range of about 125'1'.
peratures (80 F), a product the doctor test but with only a neglibile rise in cetane numher was obtained. when employing my invention, i. e., treatment lrvpochlorite and in sulfur, a sweet product results.
Diesel fuels treated in the at high temperatures with the presence of mercaptan of high octane ratin manner described solution may be used as such or may be blended with an untreated Diesel fuel stock to form a blend having improved ignition quality.
within the contemplation of this invention It is to treat gas oils which are practically sweet, or which have been partly desulfurized or sweetened, by any suitable refining method even though the hypochlorite is capable of eflecting some elimination of mercaptan sulfur when accomplishing the desired improvement in ignition quality. The present process was found to effect a substantial ignition quality of gas oils which contained practically no reactive sulfur (free sulfur or polysulfide sulfur), and also, it was found eflective for increasing the cetane numbers of sour and cracked gas oils having high sulfur contents without making any decided desulfurization.
procedure the improvecompanied by substantial desulfurization, it is preferred to apply the described treatment to Diesel fuel oils which do not have extremely-high sulfur contents. A preferred starting oil for the ignition quality improving treatment is a gas oil that while treating the or similar high boiling petroleum fractionboilin: mainly above 450 F. with an end point below 150' E. with a sulfur content within specification limits, such as below 1%, and with a mercaptan suigiglc zntent less than 0.05%, e. g., about 0.001% to Although caustic soda is preferred for use in the hypochlorite solution, being the most practical, other metals may be used in the reagent, e. g., aluminum, zinc, magnesium. iron, copper, potassium, or calcium. One of the additional modifications which may be carried out is to use with the hypochlorlte treating agent a small amount of an oxidizing agent or a chlorinating sc such as chlorine gas. hypwmorous acid,
hydrogen chloride, or other halogens. Also, the treating conditions may be influenced by exposure of the reaction mixture-to light, varying the intensity of agitation and varying the time of coming within the scope of be included therein.
I of a Diesel engine.
contact. The reaction may be purification treatments, such with adsorbents. or the, like. A While the invention has been described in terms of preferred embodiments thereof, the examples given are not intended to be taken as a limitation on the scope of the invention but only illustrative, and all modifications or variations as filtering, contact I claim:
The method ofimproving a Diesel fuel which comprises reacting a mercaptan with an inorganic hypochlorite to form an oil-soluble ignition accelerator possessing oxidizing potency of incorporating said accelerator fuel oil adapted for operation active oxygen and into a petroleum followed bxvariousthe invention are to GEORGE R. GILBERT.
US432629A 1942-02-27 1942-02-27 Diesel fuel Expired - Lifetime US2379228A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US432629A US2379228A (en) 1942-02-27 1942-02-27 Diesel fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US432629A US2379228A (en) 1942-02-27 1942-02-27 Diesel fuel

Publications (1)

Publication Number Publication Date
US2379228A true US2379228A (en) 1945-06-26

Family

ID=23716939

Family Applications (1)

Application Number Title Priority Date Filing Date
US432629A Expired - Lifetime US2379228A (en) 1942-02-27 1942-02-27 Diesel fuel

Country Status (1)

Country Link
US (1) US2379228A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2472152A (en) * 1944-08-05 1949-06-07 Union Oil Co Diesel engine fuel
US2631121A (en) * 1949-08-13 1953-03-10 Standard Oil Dev Co Hypochlorite sweetening process

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2472152A (en) * 1944-08-05 1949-06-07 Union Oil Co Diesel engine fuel
US2631121A (en) * 1949-08-13 1953-03-10 Standard Oil Dev Co Hypochlorite sweetening process

Similar Documents

Publication Publication Date Title
US2772211A (en) Treatment of hydrocarbon stocks with sodium
US2020661A (en) Process for treating hydrocarbon oils
US2912313A (en) Diesel fuel
US2379228A (en) Diesel fuel
US2028998A (en) Method of sweetening hydrocarbon oils
US2721166A (en) Treatment of distillates with hypochlorite solution
US2560374A (en) Treatment of sour petroleum distillates
US2471108A (en) Treatment of sulfur containing hydrocarbons
US2903422A (en) Process for sweetening hydrocarbons with alkali hypochlorites, alkali hydroxides and alkali mercaptides
US2022942A (en) Method of sweetening hydrocarbon oils
US2034837A (en) Method of sweetening hydrocarbon oils with alkali polysulphides
US3052626A (en) Treatment of petroleum products
US2174810A (en) Process for sweetening of hydrocarbon oils
US2784057A (en) Process for treating spent hypochlorite solutions
US2031972A (en) Sweetening process
US2149035A (en) Process for sweetening of hydrocarbon oils
US2503486A (en) Method of desulfurization by treatment with elemental halogens
US1950739A (en) Refining treatment of hydrocarbon oils
US1805444A (en) Desulphurizing liquid hydrocarbon
US2766182A (en) Hypochlorite and caustic oil treating process
US2915461A (en) Multi-stage sweetening process employing an alkaline hypochlorite solution
US2080365A (en) Treatment of petroleum distillates
US1945121A (en) Process for refining petroleum oil
US3449239A (en) Diazine in a hydrocarbon sweetening process
US2288401A (en) Method of treating diesel fuel