US2970104A - Method for improving the odor of hydrocarbon distillates with lead dioxide - Google Patents

Method for improving the odor of hydrocarbon distillates with lead dioxide Download PDF

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Publication number
US2970104A
US2970104A US667992A US66799257A US2970104A US 2970104 A US2970104 A US 2970104A US 667992 A US667992 A US 667992A US 66799257 A US66799257 A US 66799257A US 2970104 A US2970104 A US 2970104A
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odor
lead dioxide
naphtha
improving
hydrocarbon distillates
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US667992A
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Robert W Snyder
Gray Richard J De
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Standard Oil Co
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Standard Oil Co
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/06Metal salts, or metal salts deposited on a carrier
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/16Metal oxides

Definitions

  • the present invention relates to a method of improving the odor of hydrocarbon distillates. More particularly, the invention relates to a method wherein the odor of certain petroleum fractions is ameliorated by contacting such fractions with lead dioxide.
  • Certain hydrocarbon distillates derived from crude petroleum oil are widely employed as solvents in a variety of industries. That fraction of crude petroleum oil boiling in the range of 100 F. to 400 F. which is known to the art as naphtha has been used extensively as a solvent in the dry cleaning of clothing and other textiles. Another important use of this naphtha fraction is as a solvent in the manufacture of paint and related products. In these applications it is obviously important that the naphtha be free of any obnoxious odor, and where possible it is desirable that the odor of the naphtha not have an unpleasant reaction upon the human olfactory nerve.
  • naphthas do not possess a pleasant odor as produced since they contain mercaptans and other odoriferous organic compounds. Consequently, some method of treating naphthas is generally resorted to in the solvent manufacturing industry to improve their odors. Various methods are known to the art for accomplishing this purpose.
  • lead dioxide may be mixed with the stock to be treated and the mixture is then passed to a settling zone.
  • a portion of the lead dioxide may be continuously withdrawn from the settling zone and admixed with fresh feed.
  • the operation is carried out at ambient temperatures but temperature is not critical and other temperatures have been found to be operable. Temperatures above the boiling point of the stock are preferably avoided in order that the process can be carried out without pressure apparatus.
  • the method of the invention may be conducted under super-atmospheric pressure, but pressure is in no way critical and the process is usually conducted at atmospheric pressure. There appears to be 2,970,104 Patented Jan. 31, 1961 very little deterioration in the effectiveness of the lead dioxide upon continued use. However, periodic replacement of the lead dioxide is contemplated within the scope of this invention.
  • the lead dioxide which is employed in the process of this invention should be in a solid particle form. Particle size is not critical and any convenient size may be employed in this process.
  • contact times of about 60 to about 120 minutes are effective to improve the odor of most stocks.
  • the contact time is defined herein as the total free volume of lead dioxide divided by the volume of hydrocarbon passing thereover per minute. Longer contact times may be employed but there is generally no advantage to this since the odor will be improved to only a small extent upon such continued treatment. 7
  • a virgin naphtha solvent boiling from 300 F. to 400 F. obtained by distillation from crude Mid-Continent petroleum was percolated through a bed of lead dioxide at the rate of 0.011 gaL/min. at a temperature of F. and atmospheric pressure.
  • the lead dioxide bed was contained in a conventional steel treating vessel having inlets and outlets as is well known to the art and it was composed of 1 lb. of lead dioxide having a bulk density of 92.4 lbs./cu. ft.
  • the naphtha fed to the process had a distinct unpleasant odor, but after treatment no unpleasant odor was detected.
  • a total of 17.5 gal. of the naphtha were treated with no apparent decrease in the efiectiveness of the lead dioxide.
  • a process for improving the odor of a petroleum naphtha, boiling in the range between about to about 400 F. and having a normally unpleasant odor consisting of the step of contacting said naphtha in the liquid phase at a temperature of about 70 F. with a bed of lead dioxide in solid particle form so that the contact time is about 60 to about minutes, whereby the odor of said naphtha is ameliorated.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

nited States Patent METHOD FOR IIVIPROVING THE ODOR OF HY- lgylggfiiARBoN DISTILLATES WITH LEAD DI- Robert W. Snyder, Sheflield Lake, and Richard J.
De Gray, Shaker Heights, Ohio, assignors to The Stand- Oil Company, Cleveland, Ohio, a corporation of No Drawing. Filed June 25, 1957, Ser. No. 667,992
1 Claim. (Cl. 208-295) The present invention relates to a method of improving the odor of hydrocarbon distillates. More particularly, the invention relates to a method wherein the odor of certain petroleum fractions is ameliorated by contacting such fractions with lead dioxide.
Certain hydrocarbon distillates derived from crude petroleum oil are widely employed as solvents in a variety of industries. That fraction of crude petroleum oil boiling in the range of 100 F. to 400 F. which is known to the art as naphtha has been used extensively as a solvent in the dry cleaning of clothing and other textiles. Another important use of this naphtha fraction is as a solvent in the manufacture of paint and related products. In these applications it is obviously important that the naphtha be free of any obnoxious odor, and where possible it is desirable that the odor of the naphtha not have an unpleasant reaction upon the human olfactory nerve.
Most naphthas do not possess a pleasant odor as produced since they contain mercaptans and other odoriferous organic compounds. Consequently, some method of treating naphthas is generally resorted to in the solvent manufacturing industry to improve their odors. Various methods are known to the art for accomplishing this purpose.
We have now discovered that the odor of a petroleum naphtha may be appreciably improved by contacting the naphtha with lead dioxide (PbO This discovery is quite surprising since other lead compounds have no elfect whatever on the odor of naphtha under similar treating conditions. For example, litharge (PbO) has been found to have no appreciable effect on the odor of a petroleum naphtha.
In carrying out the process of this invention, we prefer to conduct the process in a vessel packed with solid lead dioxide by percolating the stock to be treated therethrough. Alternately lead dioxide may be mixed with the stock to be treated and the mixture is then passed to a settling zone. In the latter embodiment of the invention, a portion of the lead dioxide may be continuously withdrawn from the settling zone and admixed with fresh feed.
In general, the operation is carried out at ambient temperatures but temperature is not critical and other temperatures have been found to be operable. Temperatures above the boiling point of the stock are preferably avoided in order that the process can be carried out without pressure apparatus. The method of the invention may be conducted under super-atmospheric pressure, but pressure is in no way critical and the process is usually conducted at atmospheric pressure. There appears to be 2,970,104 Patented Jan. 31, 1961 very little deterioration in the effectiveness of the lead dioxide upon continued use. However, periodic replacement of the lead dioxide is contemplated within the scope of this invention.
The lead dioxide which is employed in the process of this invention should be in a solid particle form. Particle size is not critical and any convenient size may be employed in this process.
It has been found that contact times of about 60 to about 120 minutes are effective to improve the odor of most stocks. The contact time is defined herein as the total free volume of lead dioxide divided by the volume of hydrocarbon passing thereover per minute. Longer contact times may be employed but there is generally no advantage to this since the odor will be improved to only a small extent upon such continued treatment. 7
The following example is illustrative of the preferred embodiment of our invention:
A virgin naphtha solvent boiling from 300 F. to 400 F. obtained by distillation from crude Mid-Continent petroleum Was percolated through a bed of lead dioxide at the rate of 0.011 gaL/min. at a temperature of F. and atmospheric pressure. The lead dioxide bed was contained in a conventional steel treating vessel having inlets and outlets as is well known to the art and it was composed of 1 lb. of lead dioxide having a bulk density of 92.4 lbs./cu. ft. The naphtha fed to the process had a distinct unpleasant odor, but after treatment no unpleasant odor was detected. A total of 17.5 gal. of the naphtha were treated with no apparent decrease in the efiectiveness of the lead dioxide.
While this invention has been described particularly with reference to petroleum naphthas, this was done merely for the purposes of illustration and the invention is not intended to be limited thereto. Other petroleum fractions such as coker overhead gas oil, catalytic cycle stocks and kerosene may be treated by the method of our invention with efficacy. Accordingly, we desire this application for Letters Patent to cover all such embodirnents of the invention as will reasonably fall within the scope of the appended claim.
We claim:
A process for improving the odor of a petroleum naphtha, boiling in the range between about to about 400 F. and having a normally unpleasant odor, consisting of the step of contacting said naphtha in the liquid phase at a temperature of about 70 F. with a bed of lead dioxide in solid particle form so that the contact time is about 60 to about minutes, whereby the odor of said naphtha is ameliorated.
References Cited in the file of this patent UNITED STATES PATENTS 564,341 Salathe July 21, 1896 607,017 Colin July 12, 1898 1,767,356 Fischer June 24, 1930 2,338,941 Howard Jan. 11, 1944 2,369,558 Gilbert Feb. 13, 1945 FOREIGN PATENTS 48 Great Britain Ian. 6, 1863 748.267 France July 1, 1933
US667992A 1957-06-25 1957-06-25 Method for improving the odor of hydrocarbon distillates with lead dioxide Expired - Lifetime US2970104A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3306846A (en) * 1964-01-03 1967-02-28 Shell Oil Co Peroxide removal using lead dioxide or manganese dioxide

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US564341A (en) * 1896-07-21 Of same place
US607017A (en) * 1898-07-12 Process of desulfurizing petroleum
US1767356A (en) * 1927-08-19 1930-06-24 Standard Oil Dev Co Process for purification of hydrocarbon oils
FR748267A (en) * 1932-03-23 1933-07-01 Improvements in the purification of hydrocarbons
US2338941A (en) * 1937-10-22 1944-01-11 Petroleum Res Corp Process of refining mineral oils
US2369558A (en) * 1942-12-11 1945-02-13 Standard Oil Dev Co Process for sweetening sour hydrocarbon oil

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US564341A (en) * 1896-07-21 Of same place
US607017A (en) * 1898-07-12 Process of desulfurizing petroleum
US1767356A (en) * 1927-08-19 1930-06-24 Standard Oil Dev Co Process for purification of hydrocarbon oils
FR748267A (en) * 1932-03-23 1933-07-01 Improvements in the purification of hydrocarbons
US2338941A (en) * 1937-10-22 1944-01-11 Petroleum Res Corp Process of refining mineral oils
US2369558A (en) * 1942-12-11 1945-02-13 Standard Oil Dev Co Process for sweetening sour hydrocarbon oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3306846A (en) * 1964-01-03 1967-02-28 Shell Oil Co Peroxide removal using lead dioxide or manganese dioxide

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