US1569872A - Process for refining cracked hydrocarbon oil - Google Patents
Process for refining cracked hydrocarbon oil Download PDFInfo
- Publication number
- US1569872A US1569872A US585551A US58555122A US1569872A US 1569872 A US1569872 A US 1569872A US 585551 A US585551 A US 585551A US 58555122 A US58555122 A US 58555122A US 1569872 A US1569872 A US 1569872A
- Authority
- US
- United States
- Prior art keywords
- oil
- sulphur
- cracked hydrocarbon
- hydrocarbon oil
- solution
- 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
- 238000000034 method Methods 0.000 title description 10
- 239000004215 Carbon black (E152) Substances 0.000 title description 9
- 229930195733 hydrocarbon Natural products 0.000 title description 9
- 150000002430 hydrocarbons Chemical class 0.000 title description 9
- 238000007670 refining Methods 0.000 title description 5
- 239000003921 oil Substances 0.000 description 29
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 13
- 239000005864 Sulphur Substances 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 5
- HTUMBQDCCIXGCV-UHFFFAOYSA-N lead oxide Chemical compound [O-2].[Pb+2] HTUMBQDCCIXGCV-UHFFFAOYSA-N 0.000 description 4
- YEXPOXQUZXUXJW-UHFFFAOYSA-N lead(II) oxide Inorganic materials [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 235000009508 confectionery Nutrition 0.000 description 2
- XCAUINMIESBTBL-UHFFFAOYSA-N lead(ii) sulfide Chemical compound [Pb]=S XCAUINMIESBTBL-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 150000004763 sulfides Chemical class 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 241000370685 Arge Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229960003975 potassium Drugs 0.000 description 1
- 235000007686 potassium Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 239000002699 waste material 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
- C10G19/02—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with aqueous alkaline solutions
- C10G19/06—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment with aqueous alkaline solutions with plumbites or plumbates
Definitions
- This invention relates to improyements in a process for refining cracked hydrocarbon oils, and refers particularly to cracked hydrocarbon oils having a high sulphur content.
- an alkali such as sodium hydoxide or other base, in the arge dissolved in caustic soda,) sodium hydroxide or potassium hydroxide.
- a suitable proportion might be about five barrels of 163() Baum caustic containing from 5 to 30 pounds of litharge for each 100 barrelsof oil treated. After agitating with the plumbite solution, the latter is removed, and itmay be desirable to wash 'out some/of the remaining traces of the plumbite solution. To the oil then is added a small amount say 4 to 20 pounds per 100 barrels of one of the sulphide solutions, previously mentioned.
- the alkali wash between the sulphuric acid and plumbite treatments inay be dispensed with, in some cases. It is understood that the proportions and concentrati'ons of treating agents used may be varied within wide limits.
- A. step in a'process for refining hydrocarbon oil consisting in subjecting the oil to an alkali metal plumbite in water solution, agitating the mixture, in then extracting the plumbite solution from the oil, in then introducing sulphide in water solution solution from the oil, in then introducing to the oil, sulphide 1n Water solution to assist the reaction and precipitate sulphur compounds, removing the separated precipitate and excess sulphide.
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Patented Jan. 19, 1926.
UNITED STATES PATENT OFFICE.
JACQUE Q'MORRELL, OF CHICAGO, ILLINOIS. ASSIGNOR TO THE UNIVERSAL OIL PROD- UCTS COMPANY, OF CHICAGQ, ILLINOIS, A CORPORATION OF SOUTH DAKOTA.
PROCESS FOR REFINING CRACKED HYDROCARBON OIL.
No Drawing.
To all whom it may concern."
Be it known that I, JACQUE C. MonnELL, a citizen of the United State, residing at No. 208 South La Salle Street, in the city of Chicago, county of Cook, and State of Illinois,
have invented certain new and useful 121K1- provements in Processes; for Refining Cracked Hydrocarbon Oil, of which the following is a specification.
This invention relates to improyements in a process for refining cracked hydrocarbon oils, and refers particularly to cracked hydrocarbon oils having a high sulphur content.
Among the objects of the invention are to provide a process in which the sulphur is extracted from the oil in successive stages,
and the oil subjected to a secondary distillation to produce a refined water white sweet odored product.
Heretofore, it has-been common practice in eliminating objectionable sulphur compounds from hydrocarbon oils to treat the oil with a solution of litharge or lead monoxide in sodium hydroxide in conjunction with sulphur. Few variations of this procedure have been tried, and the reaction itself not carefully observed and considered.
It has been found that sulphur is relatively soluble in hydrocarbon oil, and that the practice of agitating a solution of litharge in sodium hydroxide (sodium plumbite) with the oil to be treated, and adding flowers of sulphur has caused the difficulties in that szme of the sulphur would become dissolved the oil. Upon the addition of sulphur a precipitate containing some lead sulphide is formed. Although not generally known, thereis aconsiderable quantity of the sulphur dissolved in the oil, and is not removed by precipitation, nor can it be taken out'by subsequent water washing.
To avoid this objectionable feature, it is the purpose of this invention to substitute vfor the sulphur various water soluble sulphides, especially the sulphides of potas sium, sodium, and ammonium, or their equivalents including hydrogen sulphide or sulphur dissolved in certain alkalies.
, In treating the oil by'this improved process, one method of procedure may be adopted: The oil may be agitated in the presence of sulphuric acid for say, 15 to 20 minutes,
in the proportion of say, 500 to 650 pounds of acid per 190 barrels of oil, and may then i Application filed August 31, 1922. Serial No. 585,551.
be subjected to treatemcnt with an alkali such as sodium hydoxide or other base, in the arge dissolved in caustic soda,) sodium hydroxide or potassium hydroxide. A suitable proportion might be about five barrels of 163() Baum caustic containing from 5 to 30 pounds of litharge for each 100 barrelsof oil treated. After agitating with the plumbite solution, the latter is removed, and itmay be desirable to wash 'out some/of the remaining traces of the plumbite solution. To the oil then is added a small amount say 4 to 20 pounds per 100 barrels of one of the sulphide solutions, previously mentioned.
This produces a precipitate containing some lead sulphide. This removing of the plumbite solution, and subsequently adding sul- 'phide is an unusual practice, as heretofore the sulphur has been mixed with the oil while the plumbite is contained therein. The
reason for removing the plumbite solution is' that the sulphide reacts with the plumbite solution causing unnecessary waste, and it has been found that when a cracked hydrocarbon oil is treated with a plumbite solution, .a compound of lead soluble in the oil is formed.
After the percipitate is thrown down, it is removed from the oil, and the oil cleaned by subsequent Water washing.
It is then distilled, preferably by steam producing a clear, water white sweet odored distillate. Satisfactory results have been obtained with Mexican, California and Texas oils having a high sulphur content with uniformly good results.
The alkali wash between the sulphuric acid and plumbite treatments inay be dispensed with, in some cases. It is understood that the proportions and concentrati'ons of treating agents used may be varied within wide limits.
I claim as my invention:
1. A. step in a'process for refining hydrocarbon oil consisting in subjecting the oil to an alkali metal plumbite in water solution, agitating the mixture, in then extracting the plumbite solution from the oil, in then introducing sulphide in water solution solution from the oil, in then introducing to the oil, sulphide 1n Water solution to assist the reaction and precipitate sulphur compounds, removing the separated precipitate and excess sulphide.
J ACQUE C. MORRELL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US585551A US1569872A (en) | 1922-08-31 | 1922-08-31 | Process for refining cracked hydrocarbon oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US585551A US1569872A (en) | 1922-08-31 | 1922-08-31 | Process for refining cracked hydrocarbon oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1569872A true US1569872A (en) | 1926-01-19 |
Family
ID=24341934
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US585551A Expired - Lifetime US1569872A (en) | 1922-08-31 | 1922-08-31 | Process for refining cracked hydrocarbon oil |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1569872A (en) |
-
1922
- 1922-08-31 US US585551A patent/US1569872A/en not_active Expired - Lifetime
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