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Publication numberUS1938672 A
Publication typeGrant
Publication dateDec 12, 1933
Filing dateJul 5, 1929
Priority dateJul 5, 1929
Publication numberUS 1938672 A, US 1938672A, US-A-1938672, US1938672 A, US1938672A
InventorsRobert F Ruthruff
Original AssigneeStandard Oil Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Desulphurizing hydrocarbon oils
US 1938672 A
Abstract  available in
Previous page
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Claims  available in
Description  (OCR text may contain errors)

Patented Dec. 12, 1933 DESULPHURIZING nYnRocAaBoN or s Robert F. Ruthruff, Hammond, Ind, assignor to Standard'Oil Company, Whiting, Ind., a corporation of Indiana No Drawing. Application July 5, 1929 Serial No; 376,290 1 9 Claims.

The present invention relates to improvements in desulphurizing hydrocarbon oils, and more particularly the lower boiling point distillates such as distillates in the gasoline and kerosene boiling point range. It has been found particularly suited for use in connection with cracked distillates from high sulphur oil, such as Lander and Winkler oils which distillates contain sulphur bodies of a highly refractory type and which are diflicult to remove.

In accordance with the present invention, the alkali metals such as sodium and potassium are preferably employed to effect the desulphurizing. The metal used may be employed in lumps (massive) in operating in accordance with the present invention, and metals fusible at the temperature of operation are then preferred.

In carrying out the invention, the active metal is employed in a proportion equal to or substantially exceeding the atomic equivalent of the amount of sulphur present. In general, the atomic proportion of the metal to the sulphur should exceed 1 to 1, and proportions in excess of 3 to 1 are preferred. The distillate and the active metal are heated together to a temperature of at least 400 F. and preferably not exceeding 650 F. In general a temperature of at least 500 F. is preferred. The operation is conducted under pressure, generally in excess of 150 lbs. per sq. in. and preferably from 200 'to 300 lbs. per sq. in. Higher pressures are employed when lower boiling constituents are present. Under these temperature and pressure conditions the distillate is of course substantially in the liquid state and the alkali metal is in the molten condition.

As an example of the operation, a gasoline derived by a vapor phase cracking operation from a high sulphur crude oil was treated with lump sodium, the atomic ratio of sodium to sulphur being 4 to 1 at a temperature of 575 F. and a pressure of 290 lbs. per sq. in. for three hours with vigorous agitation, the percentage of sulphur being reduced from an initial value of 0.182 to 0.087. The same gasoline treated with a higher proportion of sodium, the atomic proportion of sodium to sulphur being 6.3 to l, at 575 F. under 300 lbs. per sq. in. pressure, the sulphur was reduced to 0.016%.

To further illustrate the invention, the 225 to 420 F. cut of another distillate derived by an ordinary cracking process from a sulphur-containing crude was treated in the presence of an inert substantially sulphur-free heavy oil having an initial boiling point above 600 F. with sodium in an atomic ratio to the sulphur of 4.65 to 1 at a temperature of 560 F. and a pressure of 175 lbs., the sulphur content being reduced from 0.473% to about 0.1%. It is thus apparent that the admixture of a heavy oil which, has an initial boiling point substantially above the end point of the distillate oil and is therefore readily separable from the low boiling distillate, improves the effectiveness of the action of the active metal.

Other alkali metals, such as lithium, potassium and the like are similarly efiective.

When sodium or other active alkali metal is employed in lump form, it may be screened or otherwise separated out of the treated oil and reused for the treatment of fresh sulphurcontaining distillate, suflicient additional fresh metal being supplied to bring the atomic ratio of metal to sulphur to the desired figure. However, since more sodium is apparently used up in the reaction than that calculated from the amount of sulphur removed, an excess over such calculated amount should be supplied for replenishment or the amount of sodium present will be insufficient to effect the desired desulphurization. Thus, in an operation conducted with sodium in lump form in an atomic ratio relative to the sulphur of 4 to 1 on a sulphurcontaining pressure distillate out having an approximate boiling range of from 225 to 420 F., at a temperature of 575 F. and a pressure of 235 lbs. per sq. in. for three hours, in the first use of the sodium, the sulphur was reduced from an initial percentage of 0.764 to 0.067. On the second use, it was reduced from 0.764 to 0.092, and on third use from 0.764 to 0.186. Thus the sodium or other active metal may be reused as long as the amount present is sufficient for effective reaction, additional metal being added as required to maintain effectiveness.

The operation may be conducted in an atmosphere of a gas inert to the oil and alkali metal under the conditions of the process, such as hydrogen or nitrogen. This serves to increase the effectiveness of sulphur removal with a given ratio of metal to sulphur.

I claim:

1. In a process of desulphurizing a low boiling hydrocarbon distillate lying substantially within the gasoline-kerosene boiling point range the step which consists in coagitating said distillate, in substantially liquid state, and an alkali metal in molten form at a temperature substantially within the range of 450 F. to 650 F. under a pressure of at least about 150 pounds per square inch.

2. The process as in claim 1 in which the alkali metal is metallic sodium.

3. The process as in claim 1 wherein the distillate prior to treatment with the alkali metal, is admixed with a low sulphur oil, the initial boiling point of which is substantially above the end point of said distillate.

4. The process as in claim 1 wherein the distillate and alkali metal are coagitated in an atmosphere of a gas inert to the oil and alkali metal under the conditions of the process.

5. The process as in claim 1 wherein the excess alkali metal is separated from the treated distillate, and coagitated with a fresh portion of untreated distillate and a fresh portion of alkali metal under said conditions of temperaa ture and pressure. p

6. The process as in claim 1 in which at 7 .inch.

8. The process as in claim '7 in which the alkali metal is metallic sodium.

9. The process as in claim 7 in which at least three atoms of alkali metal are used for every atom of sulphur in the distillate to be desulphurized.


Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US2772211 *May 28, 1953Nov 27, 1956Ethyl CorpTreatment of hydrocarbon stocks with sodium
US2879241 *Mar 10, 1955Mar 24, 1959Petrolite CorpProcess of oxidizing mixture of microcrystalline wax, an ester of monocarboxylated polyethylene and polyethylene, and product produced thereby
US2960546 *Mar 11, 1957Nov 15, 1960Nat Distillers Chem CorpDesulfurization of aromatic hydrocarbons
US3755149 *Jun 9, 1971Aug 28, 1973Sun Oil Co PennsylvaniaProcess for desulfurizing petroleum resids
US4076613 *Apr 28, 1975Feb 28, 1978Exxon Research & Engineering Co.Combined disulfurization and conversion with alkali metals
US4119528 *Aug 1, 1977Oct 10, 1978Exxon Research & Engineering Co.Hydroconversion of residua with potassium sulfide
US4366045 *May 29, 1981Dec 28, 1982Rollan SwansonProcess for conversion of coal to gaseous hydrocarbons
US4468316 *Mar 3, 1983Aug 28, 1984Chemroll Enterprises, Inc.Hydrogenation of asphaltenes and the like
US4545891 *Mar 30, 1982Oct 8, 1985Trw Inc.Extraction and upgrading of fossil fuels using fused caustic and acid solutions
US5059307 *Oct 11, 1989Oct 22, 1991Trw Inc.Process for upgrading coal
US5085764 *Dec 19, 1989Feb 4, 1992Trw Inc.Process for upgrading coal
US6053963 *May 21, 1998Apr 25, 2000Gnb Technologies, Inc.Method for treating rotary slag
US6210564 *May 28, 1997Apr 3, 2001Exxon Research And Engineering CompanyProcess for desulfurization of petroleum feeds utilizing sodium metal
US8951491Jan 3, 2014Feb 10, 2015Council Of Scientific & Industrial ResearchProcess for the adsorption of toxic sulphur bearing gases
DE3114766A1 *Apr 11, 1981Jun 16, 1982Rollan Dr SwansonVerfahren zum umwandeln von kohle oder torf in gasfoermige kohlenwasserstoffe oder fluechtige destillate oder gemische hiervon
WO1997046638A1 *Jun 4, 1997Dec 11, 1997Exxon Research Engineering CoProcess for desulfurization of petroleum feeds
U.S. Classification208/230, 208/208.00R, 208/208.00M, 208/213
International ClassificationC10G19/00
Cooperative ClassificationC10G29/02, C10G29/04, C10G19/00
European ClassificationC10G29/04, C10G29/02, C10G19/00