[go: up one dir, main page]

US1698471A - Art of handling heavy oil residues - Google Patents

Art of handling heavy oil residues Download PDF

Info

Publication number
US1698471A
US1698471A US613550A US61355023A US1698471A US 1698471 A US1698471 A US 1698471A US 613550 A US613550 A US 613550A US 61355023 A US61355023 A US 61355023A US 1698471 A US1698471 A US 1698471A
Authority
US
United States
Prior art keywords
oil
art
heavy oil
oil residues
handling heavy
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
US613550A
Inventor
Oscar E Bransky
Francis M Rogers
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 Co
Original Assignee
Standard Oil 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 Co filed Critical Standard Oil Co
Priority to US613550A priority Critical patent/US1698471A/en
Application granted granted Critical
Publication of US1698471A publication Critical patent/US1698471A/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
    • 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
    • C10G17/06Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof

Definitions

  • a verylight hydrocarbon oil I product such as naphtha (boiling point range 190 to 330 F.) hexane or other'lightproduct having an end boiling point withln the gasoline boiling point range, and the mixture is then allowed to settle.
  • Suitable proportions are, for example, 10 to parts of a residue 7 to 10 .per cent of the original oil and 70 to 90 parts of naphtha.
  • the naphtha solution of the residue, after femovalof the asphaltines, may" be subjected 40 l to'atreatment with sulfuric acid, forexample,
  • a material particularly suited for use in connection ,with the above process is, for example,'the residue of about 7 per cent produced from mid-continent crude oil by reduction by fire and steam and having a melting point of about 110 F. and a penetration of 77 (A. S. T. M. method).
  • thedilute oil remainin may be treated with from 1 to 1 pounds 0 66 B. sulfuric acid per gallon, the treatment being preferably -car-g ried out in two or three dumps with removal of, sludge after each dump.'
  • the resulting sour .oil may be washed andrneutralized and subjected to filtration .for the removal of petrolatum, if desired.
  • the residual product is, for example,'the residue of about 7 per cent produced from mid-continent crude oil by reduction by fire and steam and having a melting point of about 110 F. and a penetration of 77 (A. S. T. M. method).
  • the method of handling crude oil" residue obtained by distillation from an as- 'phalt bearing-crude oil substantially without cracking which comprises the steps of substantially diluting the residue with a hydrocarbon oil having a boiling point in the gasoline boiling .point range, and removing undissolved asphaltines therefrom.

Landscapes

  • 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Working-Up Tar And Pitch (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

25 amounting to from i Patents Jan. 192a OSCAR E. BRANSKY AND FRANCES M. ROGERS, F WRITING, INDIANA, ASSIGNOBS T0 STANDARD OIL COMPANY,'0F WHITING, INDIANA, CORPORATION- OF INDA;
Aim: or No Drawing.
sulting when such an oil, for example, of the l character of mid-continent crude oil, is'reduced to a bot-tom or residue of high flash and fire test, the distillation being'conducted 1o eithe? with steam or under vacuum, so that substantially no cracking takes place: The
process is particularly advantageous in connectionwith the residues .from asphalt hear-- ing crude oils amounting toper cent-or less of the original oil. A v -In accordance with the present invention,
the resid'ue'of the character described is treated with a verylight hydrocarbon oil I product, such as naphtha (boiling point range 190 to 330 F.) hexane or other'lightproduct having an end boiling point withln the gasoline boiling point range, and the mixture is then allowed to settle. Suitable proportions are, for example, 10 to parts of a residue 7 to 10 .per cent of the original oil and 70 to 90 parts of naphtha.
After settling for a suitable period, say 12 to r 24 hours, the solution of the residue and naphtha'is decanted from the settled asphaltines,
30 which, after removal of any naphtha they 'may contain, may be utilized in the manufacture of asphaltic pitches and the like. In-
stead of removing the asphaltines by settling, it is readily apparent that the solution of pitch in naphtha'may be subjected to cen-.
trifugal action, and the asphaltines thereby separated. I
The naphtha solution of the residue, after femovalof the asphaltines, may" be subjected 40 l to'atreatment with sulfuric acid, forexample,
of 66 B., this treatment being suitably carried out, for example, bytreatment of the r diluted oil with sulfuric acid, as described in the'prior application o'flirancis M. Rogers,
Serial No. 584,863, filed August as, 1922 The treatment is carried out'in accordance with the nature of the'final product desired, the subsequent treatment being varied with the same end inview. Thus, 'after treatme nt with sulfuric acid the diluted oil maybe filtered nuns HEAVY one RESIDUES.
Application filed January 18, 1923. Serial No. 613,550. 7 i
through fullers earth or'other clarifying materlal, or may be chilled'and settled for the removalof petrolatum, a very high flash point bright stockor cylinder stock beingthereby produced. 1
A material particularly suited for use in connection ,with the above process is, for example,'the residue of about 7 per cent produced from mid-continent crude oil by reduction by fire and steam and having a melting point of about 110 F. and a penetration of 77 (A. S. T. M. method). After removal of theasphaltines, in the manner described, thedilute oil remainin may be treated with from 1 to 1 pounds 0 66 B. sulfuric acid per gallon, the treatment being preferably -car-g ried out in two or three dumps with removal of, sludge after each dump.' The resulting sour .oil may be washed andrneutralized and subjected to filtration .for the removal of petrolatum, if desired. The residual product,
after removal of the naphtha, is found to have a flash point of above-500 F. The removal of naphtha is in all cases effected by the usual distillation procedure. V
eclaim:
1. The method 'of handling a crude oil residue obtained by distillation from asphalt' 'bearing oilsubstantially Without cracking which consists in substantially diluting'the' residue with a hydrocarbon oil having an end boiling poifit in the gasoline boiling point range, removing undissolved asphaltines and treating the remaining diluted oil with sulfuric acid.
2'. The method of handling crude oil" residue obtained by distillation from an as- 'phalt bearing-crude oil substantially without cracking which comprises the steps of substantially diluting the residue with a hydrocarbon oil having a boiling point in the gasoline boiling .point range, and removing undissolved asphaltines therefrom.
a'rhe method or handling crude 011 without cracking and representing not more than 10 per cent of the original'crudeoilresidue obtained by distillation substantially range, removing undissolved as phaltines from the resulting solution and subsequently removing the light h ydrocarbon oil.
A. The method of handling a crude oil '5," residueobtained by distillation substantially without tracking and representing not more than 10 per cent of the original crude oil,- which consists in substantially-diluting the I sequently separating the naphthajrom the treated oil.
. OSCAR BRA SKY.
FRANCIS ROGERS.
US613550A 1923-01-18 1923-01-18 Art of handling heavy oil residues Expired - Lifetime US1698471A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US613550A US1698471A (en) 1923-01-18 1923-01-18 Art of handling heavy oil residues

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US613550A US1698471A (en) 1923-01-18 1923-01-18 Art of handling heavy oil residues

Publications (1)

Publication Number Publication Date
US1698471A true US1698471A (en) 1929-01-08

Family

ID=24457738

Family Applications (1)

Application Number Title Priority Date Filing Date
US613550A Expired - Lifetime US1698471A (en) 1923-01-18 1923-01-18 Art of handling heavy oil residues

Country Status (1)

Country Link
US (1) US1698471A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2967818A (en) * 1958-04-21 1961-01-10 Kerr Mc Gee Oil Ind Inc Method for separation of bituminous materials
US3193497A (en) * 1962-01-30 1965-07-06 Sinclair Research Inc Process for making a hydrocarbon extending oil for rubber

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2967818A (en) * 1958-04-21 1961-01-10 Kerr Mc Gee Oil Ind Inc Method for separation of bituminous materials
US3193497A (en) * 1962-01-30 1965-07-06 Sinclair Research Inc Process for making a hydrocarbon extending oil for rubber

Similar Documents

Publication Publication Date Title
US1698471A (en) Art of handling heavy oil residues
US2024106A (en) Preparation of fluorescent and pour point reducing bodies from petroleum residue
US1409590A (en) Sludge treatment process and product
US2200534A (en) Low pour point lubricating oil
US2114796A (en) Petroleum resin and proces of making same
US1521283A (en) Art of refining oils
US2029382A (en) Process for producing high molecular weight compounds from petroleum oil
US1788569A (en) Fractional extraction of mineral oils
US1881643A (en) Dewaxing of petroleum oils
US3247095A (en) Hydrocarbon coking process to produce lubricating oils and waxes
US2076147A (en) Dewaxing of oil
US2210867A (en) Manufacture of lubricating oil
US2058696A (en) Process of stabilizing oils
US1961204A (en) Process of kefining a benzenoid
US2081519A (en) Method of separating wax from oil
US2663673A (en) Desulfurization of petroleum oils
US1999486A (en) Manufacture of heavy lubricating oils
US1859514A (en) Certificate of correction
US1708602A (en) Process for making a fluorescent product
US2027770A (en) Process of treating lubricating oil stock
US2088500A (en) Acetylenization of mineral oils
US2183830A (en) Decolorization of still residue
US2137218A (en) Refining hydrocarbon oils
US2044722A (en) Manufacture of lubricating oil
US2941940A (en) Hydrocarbon treating process