US1908273A - Sweetening petroleum distillates - Google Patents

Sweetening petroleum distillates Download PDF

Info

Publication number
US1908273A
US1908273A US445207A US44520730A US1908273A US 1908273 A US1908273 A US 1908273A US 445207 A US445207 A US 445207A US 44520730 A US44520730 A US 44520730A US 1908273 A US1908273 A US 1908273A
Authority
US
United States
Prior art keywords
acid
petroleum distillates
chlorite
sweetening
distillates
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
US445207A
Inventor
Maurice C Taylor
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.)
Mathieson Alkali Works Inc
Original Assignee
Mathieson Alkali Works Inc
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 Mathieson Alkali Works Inc filed Critical Mathieson Alkali Works Inc
Priority to US445207A priority Critical patent/US1908273A/en
Application granted granted Critical
Publication of US1908273A publication Critical patent/US1908273A/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
    • 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
    • C10G27/00Refining of hydrocarbon oils in the absence of hydrogen, by oxidation
    • C10G27/02Refining of hydrocarbon oils in the absence of hydrogen, by oxidation with halogen or compounds generating halogen; Hypochlorous acid or salts thereof
    • 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

Definitions

  • salts of chlorous acid such as sodium chlorite and calcium chlorite
  • sodium chlorite and calcium chlorite are effective refining agents for petroleum distillates and may be used to produce petroleum distillates of good color, odor and stability.
  • degree of acidity is not important, I have found solutions having a pH value of about 4 to be advantageous.
  • the rapidity and extent of reaction between the chlorites and the objectionableconstituents of crude petroleum distillates such as sulfur compounds may be largely controlled by regulating the amount of acid agent, acid or acid salt, used in conjunction with the chlorite. With some distillates a pH of 4 in the treating solution may be sufficient. With other distillates it is preferable to use N/lO acid or stronger.
  • the acidity of the treating solution may be controlled by the additionof an acid or acid salt, such as hydrochloric acid or sulphuric acid or sodium acid sulfate or sodium acid phosphate.
  • an acid or acid salt such as hydrochloric acid or sulphuric acid or sodium acid sulfate or sodium acid phosphate.
  • the amount of the chlorite required for refining varies with and is determined by the character of the distillate being refined.
  • the concentration of the treating solution is not critical; in general lower concentrations of the chlorite are de sirable in conjunction with higher acidity.
  • the refining operation may be carried out as a batch operation or as a continuous operation in any convenient manner.
  • Acid chlorite solutions apparently react with many of the sulphur compounds occurring in petroleum distillates to convert the sulphur of such compounds into reaction products soluble in water and thus susceptible of removal in the water of the treating solu- Application filed April 17,
  • alkali-metal chlorites or alkalineearth-metal chlorites are particularly useful in carrying out my invention, the other salts of chlorous acid and chlorous acid'itself are also useful in carrying out my invention, the
  • chlorite radical being the essential component.
  • the improvement which comprises subjecting the distillate to treatment with an acid aqueous solution of a chlorite of a metal of the group comprising the alkali-metals and the alka line-earth-metals.

Description

Patented May 9, 1933 UNITED STATES MAURICE G. TAYLOR, OF NIAGARA FALLS, NEW YORK, ASSIG-NOR TO THE MATHIESON PATENT OFFICE ALKALI WORKS, INC., OF NEW YORK, N. Y., A CORPORATION OF VIRGINIA SWEETENING PETROLEUM DISTILLATES No Drawing.
of salts of chlorous acid, such as sodium chlorite and calcium chlorite, are effective refining agents for petroleum distillates and may be used to produce petroleum distillates of good color, odor and stability. Although the exact degree of acidity is not important, I have found solutions having a pH value of about 4 to be advantageous. The rapidity and extent of reaction between the chlorites and the objectionableconstituents of crude petroleum distillates such as sulfur compounds may be largely controlled by regulating the amount of acid agent, acid or acid salt, used in conjunction with the chlorite. With some distillates a pH of 4 in the treating solution may be sufficient. With other distillates it is preferable to use N/lO acid or stronger. The acidity of the treating solution may be controlled by the additionof an acid or acid salt, such as hydrochloric acid or sulphuric acid or sodium acid sulfate or sodium acid phosphate. The amount of the chlorite required for refining varies with and is determined by the character of the distillate being refined. The concentration of the treating solution is not critical; in general lower concentrations of the chlorite are de sirable in conjunction with higher acidity. The refining operation may be carried out as a batch operation or as a continuous operation in any convenient manner.
For example: 100 parts of a gasolene distillate are placed in a suitable agitator with 40 parts of N/ 10 hydrochloric acid. The agitator is started and 2 parts of a calcium chlorite solution containing 68 grams of Ca (C10 2 per liter are added every 15 minutes until 24 parts have been added. A gasolene sweet to the Doctor test and of good color is produced.
Acid chlorite solutions apparently react with many of the sulphur compounds occurring in petroleum distillates to convert the sulphur of such compounds into reaction products soluble in water and thus susceptible of removal in the water of the treating solu- Application filed April 17,
1930. Serial No. 445,207.
tion or in the water of subsequent washes. Acid chlorite solutions, however, react to but a very slight extent, if at all, upon those hydrocarbon constituents of the petroleum distillate suitable as components of the refined product."
While alkali-metal chlorites or alkalineearth-metal chlorites are particularly useful in carrying out my invention, the other salts of chlorous acid and chlorous acid'itself are also useful in carrying out my invention, the
chlorite radical being the essential component.
I claim: 1. In sweetening petroleum distillates, the improvement which comprises subjecting the distillate to treatment with an acid aqueous solution of a chlorite of a metal of the group comprising the alkali-metals and the alka line-earth-metals.
2. In sweetening petroleum distillates, the
improvement which comprises subjecting the distillate to treatment with an acid aqueous
US445207A 1930-04-17 1930-04-17 Sweetening petroleum distillates Expired - Lifetime US1908273A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US445207A US1908273A (en) 1930-04-17 1930-04-17 Sweetening petroleum distillates

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US445207A US1908273A (en) 1930-04-17 1930-04-17 Sweetening petroleum distillates

Publications (1)

Publication Number Publication Date
US1908273A true US1908273A (en) 1933-05-09

Family

ID=23767999

Family Applications (1)

Application Number Title Priority Date Filing Date
US445207A Expired - Lifetime US1908273A (en) 1930-04-17 1930-04-17 Sweetening petroleum distillates

Country Status (1)

Country Link
US (1) US1908273A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2527176A (en) * 1946-10-04 1950-10-24 Standard Oil Dev Co Treatment of oils corrosive to copper
EP0389150A1 (en) * 1989-03-21 1990-09-26 Baker Hughes Incorporated Removal of sulphides

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2527176A (en) * 1946-10-04 1950-10-24 Standard Oil Dev Co Treatment of oils corrosive to copper
EP0389150A1 (en) * 1989-03-21 1990-09-26 Baker Hughes Incorporated Removal of sulphides
US5082576A (en) * 1989-03-21 1992-01-21 Bp Chemicals Limites Removal of sulfides using chlorite and an amphoteric ammonium betaine

Similar Documents

Publication Publication Date Title
US1965828A (en) Nitrogen base and method of making same
US1908273A (en) Sweetening petroleum distillates
US2002547A (en) Method of decomposing raw phosphates
US2550668A (en) Hypochlorite sweetening process
US2121845A (en) Process for producing clear lightcolored, water-soluble sulphonation products of mineral oil
US2903422A (en) Process for sweetening hydrocarbons with alkali hypochlorites, alkali hydroxides and alkali mercaptides
US1993140A (en) Process for refining hydrocarbon oils for removing sulphur compounds
GB161581A (en) A process for the manufacture of sulphurous acid
US1357138A (en) Process of treating distillers' slops
US2053752A (en) Art of refining
US2016342A (en) Process of sweetening petroleum oil
US1954887A (en) Treatment of hydrocarbon oils
US747347A (en) Process of desulfurizing oils or distillates.
US2030245A (en) Process for treating mineral oil distillates
US1569872A (en) Process for refining cracked hydrocarbon oil
Wood et al. Desulfurizing Effects of Sodium Hypochlorite on Naphtha Solutions of Organic Sulfur Compounds
US1725068A (en) Process of treating cracked hydrocarbons
US1968089A (en) Method of sweetening hydrocarbon distillates
US543079A (en) Frederick burton
US1788204A (en) Process of bleaching mineral oils and fats
US2027648A (en) Refining of petroleum oil
US1985955A (en) Process for sweetening hydrocarbon oil
US1945121A (en) Process for refining petroleum oil
US1718713A (en) Preparing hydrocarbon products
DE587784C (en) Process for the production of ketones