US1799431A - Refining and purification of hydrocarbon oils - Google Patents

Refining and purification of hydrocarbon oils Download PDF

Info

Publication number
US1799431A
US1799431A US97461A US9746126A US1799431A US 1799431 A US1799431 A US 1799431A US 97461 A US97461 A US 97461A US 9746126 A US9746126 A US 9746126A US 1799431 A US1799431 A US 1799431A
Authority
US
United States
Prior art keywords
oil
refining
purification
hydrocarbon oils
compounds
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
US97461A
Inventor
Jacque C Morrell
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.)
Universal Oil Products Co
Original Assignee
Universal Oil Products 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 Universal Oil Products Co filed Critical Universal Oil Products Co
Priority to US97461A priority Critical patent/US1799431A/en
Priority to US507764A priority patent/US1920270A/en
Application granted granted Critical
Publication of US1799431A publication Critical patent/US1799431A/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
    • C10G29/00Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
    • C10G29/02Non-metals
    • 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
    • C10G17/00Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
    • C10G17/02Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
    • 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
    • C10G17/00Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
    • C10G17/02Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
    • C10G17/04Liquid-liquid treatment forming two immiscible phases
    • C10G17/07Liquid-liquid treatment forming two immiscible phases using halogen acids or oxyacids of halogen
    • 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
    • C10G29/04Metals, or metals deposited on a carrier

Definitions

  • This invention relates to im rovements in refimng and purification of hy rocarbon oils, and refers more articularly tothe desulphurization of hy rocarbon oils for the purpose of providing a product which is free of refractory-sulphur compounds.
  • the present invention contemplates the refining and purification of hydrocarbon oil of any gravity from a crude hydrocarbon of low gravity, up to and including a motor fuel of higher gravity. More speci cally, the invention is peculiarly ap licable to the desulphurization of cracked istillates. Hydrocarbon oils, particularly the overhead condensed products sold commercially and produced in crackin operations sometimes contain an oble amount of refractory sul hur jectiona compounds which are not removable rom the oil by the usual refining agents such as sulphuric-acid, caustic soda, litharge in caustic soda, filter earth and the like.
  • alkyl-disulphides and analogous sulphur compounds present in oils may be converted into compounds which can be removed by subsequent subjection to treatment with the usual refining agents.
  • Either tie metal or the acid can be introduced into the oil initially followed by the other, or they may be introduced slmultaneously.
  • the oil body into which the re fining agents of the present invention have been introduced is preferably heated since it has been found that the reaction proceeds at a much greater rate under heat than in ling of the various constituents.
  • the oil body containing these refimn agents may be agitated for the purpose o securing a more complete interming- It is also preferable that the oil being treated under heat, is preferably refiuxedor distilled with the refining agents for the purpose of extending the period of reaction b preventing the more volatile components rom leaving the system.
  • the desulphurization'as described above may constitute the sole refining action on the oil, or it may constitute but a step in a series of various refining methods. It may be preceded by the usual treatments with refining agents such as sulphuric acid, caustic soda,
  • a step in a method of purifying and refining hydrocarbon oils comprising sub-' jecting the oil to heat in the presence SlIIlllltaneously of added metal and glacial acetic acid to convert the refractory sulphur compounds in the oil.
  • a step in a method of refining and purifyin1 hydrocarbon oils comprising subjecting t e oil to treatment in the resence simultaneously of added metal an acetic acid.

Description

Patented. Apr. 7, 1931 UNITED v STATES A ENT oFFlcs '5 JACQUE C. MORBELL, OF CHICAGO, ILLINOIS, ASSIGNOR TO UNIVERSAL OIL PRODUCTS COMPANY, OF CHICAGO, ILLINOIS, A CORPORATION OF SOUTH DAKOTA BIEEBININCL'AND runmrcarron or nvnnocannon OILS Ho Drawing.
This invention relates to im rovements in refimng and purification of hy rocarbon oils, and refers more articularly tothe desulphurization of hy rocarbon oils for the purpose of providing a product which is free of refractory-sulphur compounds.
The present invention contemplates the refining and purification of hydrocarbon oil of any gravity from a crude hydrocarbon of low gravity, up to and including a motor fuel of higher gravity. More speci cally, the invention is peculiarly ap licable to the desulphurization of cracked istillates. Hydrocarbon oils, particularly the overhead condensed products sold commercially and produced in crackin operations sometimes contain an oble amount of refractory sul hur jectiona compounds which are not removable rom the oil by the usual refining agents such as sulphuric-acid, caustic soda, litharge in caustic soda, filter earth and the like.
I have found that the alkyl-disulphides and analogous sulphur compounds present in oils, may be converted into compounds which can be removed by subsequent subjection to treatment with the usual refining agents.
More specifically, I have found that when oil containing these objectionable and refractory sulphur compounds is treated in the presence of a finely divided metal and an oil soluble acid, that these compounds are converted into compounds such as hydrogen sulphide and the mercaptans which can be subsequently treated so as to reduce the total sulphur content of the resulting product.
I have further found that among the metals which can be used, may be listed zinc, tin, iron or metal having analogous characteristics. Among the oil soluble acids which may be used, may be listed glacial acetic acid and hydro en chloride.
Either tie metal or the acid can be introduced into the oil initially followed by the other, or they may be introduced slmultaneously. The oil body into which the re fining agents of the present invention have been introduced, is preferably heated since it has been found that the reaction proceeds at a much greater rate under heat than in ling of the various constituents.
ing the oil to Application filed March 25, 1926. Serial No. 97,461.
the cold. It is further to be noted that in some instances, the oil body containing these refimn agentsmay be agitated for the purpose o securing a more complete interming- It is also preferable that the oil being treated under heat, is preferably refiuxedor distilled with the refining agents for the purpose of extending the period of reaction b preventing the more volatile components rom leaving the system.
a The following proportions may be as illustrative, it being understood that they may vary within wide limits and not depart from the scope of the invention; From 1 to 2% of acid and 1 to 2% of metal based on the volume of oil being treated. It will be found that the reaction takin place in the oil due to the introduction of tie reagents of the present invention will convert the refractory sulphur compounds, particularly the disulphides, into compounds which can be-subsequently easily treated with the usual refining agents such as plumbite solutions.
The desulphurization'as described above, may constitute the sole refining action on the oil, or it may constitute but a step in a series of various refining methods. It may be preceded by the usual treatments with refining agents such as sulphuric acid, caustic soda,
plumbite, filtering earth or the like, and maybe succeeded by any combination of the above .refining agents followed if desired, by disgiven 1. A step in a method of purifying and refining hydrocarbon oils, comprising sub-' jecting the oil to heat in the presence SlIIlllltaneously of added metal and glacial acetic acid to convert the refractory sulphur compounds in the oil.
2. A step in a process ofrefining and purifying hydrocarbon oils,.comprising subjectheat in the presence simultaneously of zinc and glacial acetic acid to convert refractory sulphur compounds present in the oil.
8. A step in a method of refining and purifyin1 hydrocarbon oils, comprising subjecting t e oil to treatment in the resence simultaneously of added metal an acetic acid.
J ACQUE C. MORRELL.
US97461A 1926-03-25 1926-03-25 Refining and purification of hydrocarbon oils Expired - Lifetime US1799431A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US97461A US1799431A (en) 1926-03-25 1926-03-25 Refining and purification of hydrocarbon oils
US507764A US1920270A (en) 1926-03-25 1931-01-09 Refining and purification of hydrocarbon oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US97461A US1799431A (en) 1926-03-25 1926-03-25 Refining and purification of hydrocarbon oils

Publications (1)

Publication Number Publication Date
US1799431A true US1799431A (en) 1931-04-07

Family

ID=22263475

Family Applications (1)

Application Number Title Priority Date Filing Date
US97461A Expired - Lifetime US1799431A (en) 1926-03-25 1926-03-25 Refining and purification of hydrocarbon oils

Country Status (1)

Country Link
US (1) US1799431A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4810362A (en) * 1987-03-30 1989-03-07 Sutton Energy Corporation Method for cleaning fossil fuel, such as coal and crude oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4810362A (en) * 1987-03-30 1989-03-07 Sutton Energy Corporation Method for cleaning fossil fuel, such as coal and crude oil

Similar Documents

Publication Publication Date Title
US2343841A (en) Removal of aromatics, sulphur, or unsaturates from hydrocarbons
US1998863A (en) Process for desulphurizing mercaptan-bearing oil
US1938672A (en) Desulphurizing hydrocarbon oils
US1882002A (en) Process for refining mineral oil
US2472473A (en) Conversion of hydrosulfides to neutral sulfur substances
US1799431A (en) Refining and purification of hydrocarbon oils
US1973499A (en) Treatment of hydrocarbon oils
US2163227A (en) Process for desulphurizing alkyl phenols
US1920270A (en) Refining and purification of hydrocarbon oils
US2057629A (en) Treatment of hydrocarbon oils
US1980189A (en) Treatment of hydrocarbon oils
US1767356A (en) Process for purification of hydrocarbon oils
US2070627A (en) Oxidation refining of lubricating oil
US1993140A (en) Process for refining hydrocarbon oils for removing sulphur compounds
US1920248A (en) Process for refining gasoline-containing distillates
US2042055A (en) Process of sweetening sour hydrocarbon oil
US2080365A (en) Treatment of petroleum distillates
US2739101A (en) Sweetening of thermally cracked naphthas with alkali phenolate oxygen and sulfur
US1801213A (en) Process of refining mineral oils
US1569871A (en) Process for refining hydrocarbon oil
US1950735A (en) Process for desulphurizing hydrocarbon oils
US1950739A (en) Refining treatment of hydrocarbon oils
US2013083A (en) Process of producing a colorless doctor sweet gasoline
US1949756A (en) Refining of cracked hydrocarbon oils
US2060108A (en) Treatment of blackstrap sludge