US1920270A - Refining and purification of hydrocarbon oils - Google Patents
Refining and purification of hydrocarbon oils Download PDFInfo
- Publication number
- US1920270A US1920270A US507764A US50776431A US1920270A US 1920270 A US1920270 A US 1920270A US 507764 A US507764 A US 507764A US 50776431 A US50776431 A US 50776431A US 1920270 A US1920270 A US 1920270A
- Authority
- US
- United States
- Prior art keywords
- refining
- purification
- oil
- hydrocarbon oils
- distillate
- 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 17
- 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 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 7
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 7
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical class [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 6
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- 239000011701 zinc Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000011135 tin Substances 0.000 description 3
- 229910052718 tin Inorganic materials 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- YZCKVEUIGOORGS-IGMARMGPSA-N Protium Chemical compound [1H] YZCKVEUIGOORGS-IGMARMGPSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000446 fuel Substances 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
- 239000007788 liquid Substances 0.000 description 1
- 229910001510 metal chloride Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 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
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
Definitions
- This invention relates to improvements in refining and purification of hydrocarbon oils
- 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 specifically, the invention is peculiarly applicable to the desulphurization of cracked distillates. Hydrocarbon oils, particularly the overhead condensed products sold commercially and produced in cracking operations sometimes c0ntain an objectionable amount of refractory sulphur compounds which are not removable from the oil by the usual refining agents such as suiphuric 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 the metal or the acid can be introduced into the oil initially followed by the other, or they may be introduced simultaneously.
- the oil body into which the refining 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 the cold. It is further to be noted that in some instances, the oil body containing these refining agents may be agitated for the purpose of securing a more complete intermingling of the various constituents. It is also preferable that the oil being treated under heat, is preferably refluxed or distilled with the refining agents for the purpose of extending the period of reaction by preventing the more volatile components from leaving the system.
- de'sulphurizationas 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.
- a process for purifying cracked gasoline distillate which comprises treating the distillate at elevated temperature and while maintained substantially in liquid phase with hydrogen chloride in the presence of zinc.
- a process for purifying gasoline-containing distillates which comprisestreating such distillate at a temperature of at least its normal boiling point with hydrogen chloride in the presence of added metal selected from the group consisting of zinc, tin and iron while maintaining the distillate substantially in liquid phase.
- a process for purifying gasoline-containing distillates which comprises treating such distillate at elevated temperature with hydrogen chloride in the presence of zinc while maintaining the distillate substantially in liquid phase.
- a process for purifying gasoline-containing distillates which comprises contacting such distillate substantially in liquid form simultaneously with hydrogen chloride and zinc at a temperature of at least the normal boiling point of the distillate.
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)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
VII
Patented Aug. 1, 1933.
REFINING AND PURIFICATION OF HYDRO- CARBON OILS Jacque C. Morrell, Chicago, 111., assignor to Universal Oil Products Company, Chicago, Ill., a Corporation of South Dakota No Drawing. Original application March 25,
1926, Serial No. 97,461. Divided and this application January 9, 1931. Serial No. 507,764
5 Claims.
This application is a division of my co-pending application, Serial No. 97,461, filed March 25, 1926, now Patent No. 1,799,431.
This invention relates to improvements in refining and purification of hydrocarbon oils, and
refers more particularly to the desulphurization of hydrocarbon oils for the purpose of providing a product which is substantially 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 specifically, the invention is peculiarly applicable to the desulphurization of cracked distillates. Hydrocarbon oils, particularly the overhead condensed products sold commercially and produced in cracking operations sometimes c0ntain an objectionable amount of refractory sulphur compounds which are not removable from the oil by the usual refining agents such as suiphuric 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 hydrogen chloride, that these compounds are converted into com-- pounds 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.
Either the metal or the acid can be introduced into the oil initially followed by the other, or they may be introduced simultaneously. The oil body into which the refining 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 the cold. It is further to be noted that in some instances, the oil body containing these refining agents may be agitated for the purpose of securing a more complete intermingling of the various constituents. It is also preferable that the oil being treated under heat, is preferably refluxed or distilled with the refining agents for the purpose of extending the period of reaction by preventing the more volatile components from leaving the system.
The following proportions may be given 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% hydrogen chloride and 1 to 2% of metal based on the volume of oil being treated. It will be found that the reaction taking place in the oil due to the introduction of the 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 de'sulphurizationas 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 theusual distillation.
I claim as my invention: 1. A process for purifying gasoline-containing distillates which comprises treating the distillate 'at elevated temperature and while maintained substantially in liquid phase with hydrogen chloride in the presence of added metal selected from the group consisting of zinc, tin and iron.
2. A process for purifying cracked gasoline distillate which comprises treating the distillate at elevated temperature and while maintained substantially in liquid phase with hydrogen chloride in the presence of zinc.
3. A process for purifying gasoline-containing distillates which comprisestreating such distillate at a temperature of at least its normal boiling point with hydrogen chloride in the presence of added metal selected from the group consisting of zinc, tin and iron while maintaining the distillate substantially in liquid phase.
4. A process for purifying gasoline-containing distillates which comprises treating such distillate at elevated temperature with hydrogen chloride in the presence of zinc while maintaining the distillate substantially in liquid phase.
5. A process for purifying gasoline-containing distillates which comprises contacting such distillate substantially in liquid form simultaneously with hydrogen chloride and zinc at a temperature of at least the normal boiling point of the distillate.
J ACQUE C. MORRELL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US507764A US1920270A (en) | 1926-03-25 | 1931-01-09 | Refining and purification of hydrocarbon oils |
Applications Claiming Priority (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 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1920270A true US1920270A (en) | 1933-08-01 |
Family
ID=26793290
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US507764A Expired - Lifetime US1920270A (en) | 1926-03-25 | 1931-01-09 | Refining and purification of hydrocarbon oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1920270A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4806232A (en) * | 1984-10-09 | 1989-02-21 | Environment Protection Engineers Inc. | Method for the desulphurization of sulphur-containing fuels and fuel desulphurized by said method |
-
1931
- 1931-01-09 US US507764A patent/US1920270A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4806232A (en) * | 1984-10-09 | 1989-02-21 | Environment Protection Engineers Inc. | Method for the desulphurization of sulphur-containing fuels and fuel desulphurized by said method |
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