US1698471A - Art of handling heavy oil residues - Google Patents
Art of handling heavy oil residues Download PDFInfo
- 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
Links
- 239000000295 fuel oil Substances 0.000 title 1
- 239000003921 oil Substances 0.000 description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- 239000010779 crude oil Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 238000009835 boiling Methods 0.000 description 7
- 238000004821 distillation Methods 0.000 description 6
- 238000005336 cracking Methods 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 238000007865 diluting Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 239000004264 Petrolatum Substances 0.000 description 2
- 239000010426 asphalt Substances 0.000 description 2
- 229940066842 petrolatum Drugs 0.000 description 2
- 235000019271 petrolatum Nutrition 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 241000501754 Astronotus ocellatus Species 0.000 description 1
- 241000276489 Merlangius merlangus Species 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 229910000286 fullers earth Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000013707 sensory perception of sound Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G17/00—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
- C10G17/02—Refining 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
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/06—Liquid-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.
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)
| 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 |
-
1923
- 1923-01-18 US US613550A patent/US1698471A/en not_active Expired - Lifetime
Cited By (2)
| 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 |
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