US1799431A - Refining and purification of hydrocarbon oils - Google Patents
Refining and purification of hydrocarbon oils Download PDFInfo
- 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
Links
- 239000003921 oil Substances 0.000 title description 27
- 238000007670 refining Methods 0.000 title description 12
- 239000004215 Carbon black (E152) Substances 0.000 title description 7
- 229930195733 hydrocarbon Natural products 0.000 title description 7
- 150000002430 hydrocarbons Chemical class 0.000 title description 7
- 238000000746 purification Methods 0.000 title description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000002184 metal Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical class [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 229960000583 acetic acid Drugs 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000012362 glacial acetic acid Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 241001502381 Budorcas taxicolor Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000006025 fining agent Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- HTUMBQDCCIXGCV-UHFFFAOYSA-N lead oxide Chemical compound [O-2].[Pb+2] HTUMBQDCCIXGCV-UHFFFAOYSA-N 0.000 description 1
- YEXPOXQUZXUXJW-UHFFFAOYSA-N lead(II) oxide Inorganic materials [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 239000011135 tin Substances 0.000 description 1
- 229910052718 tin Inorganic materials 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/02—Non-metals
-
- 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
-
- 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
- C10G17/07—Liquid-liquid treatment forming two immiscible phases using halogen acids or oxyacids of halogen
-
- 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/04—Metals, 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.
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)
- Lubricants (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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.
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)
| 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 |
-
1926
- 1926-03-25 US US97461A patent/US1799431A/en not_active Expired - Lifetime
Cited By (1)
| 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 |
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