US1940726A - Treatment of hydrocarbon oils - Google Patents
Treatment of hydrocarbon oils Download PDFInfo
- Publication number
- US1940726A US1940726A US507519A US50751931A US1940726A US 1940726 A US1940726 A US 1940726A US 507519 A US507519 A US 507519A US 50751931 A US50751931 A US 50751931A US 1940726 A US1940726 A US 1940726A
- Authority
- US
- United States
- Prior art keywords
- treatment
- oil
- sulfur
- oils
- cracking
- 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 32
- 238000011282 treatment Methods 0.000 title description 21
- 229930195733 hydrocarbon Natural products 0.000 title description 16
- 150000002430 hydrocarbons Chemical class 0.000 title description 16
- 239000004215 Carbon black (E152) Substances 0.000 title description 12
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 13
- 238000000034 method Methods 0.000 description 12
- 229910052717 sulfur Inorganic materials 0.000 description 11
- 239000011593 sulfur Substances 0.000 description 11
- 239000003153 chemical reaction reagent Substances 0.000 description 10
- 238000005336 cracking Methods 0.000 description 10
- 230000008569 process Effects 0.000 description 10
- 230000001476 alcoholic effect Effects 0.000 description 9
- 239000000047 product Substances 0.000 description 9
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 7
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 229910052783 alkali metal Inorganic materials 0.000 description 5
- 150000001340 alkali metals Chemical class 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 5
- 235000019441 ethanol Nutrition 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 229920001021 polysulfide Polymers 0.000 description 4
- 239000005077 polysulfide Substances 0.000 description 4
- 150000008117 polysulfides Polymers 0.000 description 4
- 150000003568 thioethers Chemical class 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- -1 sulfoxy Chemical class 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 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
- 150000001298 alcohols Chemical class 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 150000001342 alkaline earth metals Chemical class 0.000 description 2
- 238000004821 distillation Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 230000008707 rearrangement Effects 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000002019 disulfides Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 125000001183 hydrocarbyl group Chemical group 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 229910052981 lead sulfide Inorganic materials 0.000 description 1
- 229940056932 lead sulfide Drugs 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 229910052976 metal sulfide Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 150000002927 oxygen compounds Chemical class 0.000 description 1
- 229940016373 potassium polysulfide Drugs 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000012261 resinous substance Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003463 sulfur Chemical class 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 150000003577 thiophenes 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
- C10G19/00—Refining hydrocarbon oils in the absence of hydrogen, by alkaline treatment
Definitions
- This invention relatesto the treatment of hydrocarbon oils, and refers more particularly to the treatment of the lighter'distillates produced in the cracking of heavy hydrocarbons.
- the invention contemplates the treatmentof cracked distillates with chemical reagents of a particular nature effective in improving the quality of the distillates as regards their adaptability to commercial uses, particularly as fuels for internal combustion engines.
- cracked hydrocarbon distillates are treated with preferably alkaline alcoholic solutions of sulfides, hydrosulfides and polysulfides of the alkali and/ or akaline earth metals. While the treatment is preferably used as an adjunct to other treatments, in some cases it may constitute the only treatment necessary.
- the various sulfides, hydrosulfides and polysulfides of the metals of the groups mentioned vary in their solubility in absolute or anhydrous alcohols, such as ethyl or methyl alcohols, the
- solubility usually increasing as the alcohols are alkali.
- Treating reagents prepared as mentioned are particularly effective in removing or altering certain types of sulfur derivatives of hydrocarbons,
- the apparent mechanism of the reaction being the polymerizing or condensing of the organic sulfur compounds with the metal sulfides which forms either insoluble precipitates or solublehighboiling compounds which remain behind upon distillation of the lighter fractions of the oils treated.
- the compounds formed may be soluble in the reagent and in other cases precipitates may appear which are removed by sedimentation or other means.
- Reagents of the type comprised in the present invention are particularly efficacious when used following treatment of cracked distillates with sodium plumbite solutions.
- the use of sodium pluinbite forms primarily mercaptides of lead which are more or less soluble in the oils.
- powdered sulfur, such as flowers of sulfur, to oils containing the lead mercaptides 1 5 causes what is known as a break in the treatment which is really the precipitation of the black lead sulfide, the organic residues combining to formcompounds of the type of disulfides.
- oils with reagents characteristic of the invention operations may be conducted in various types of equipment and in a variety of ways, for example, the oil may be treated in a batch agitator by circulating from the bottom of the cone back into the top through distributing means by means of a circulating pump, the reagent being added to the suction side of the pump and being mixed during passage therethrough and through the nozzles or atomizing means on the discharge side.
- Reagents may be injected at suitable points in the travel of oils through continuous treating equipment, consisting of mixing devices of various types followed by set,- tling and washing chambers.
- relatively strong solutions may be added to oils undergoing distillation with fire and/or steam with retention of desirable compounds in the still residues.
- treatment under considerably elevated temperatures and pressures may be advisable, in which case apparatus of requisite strength must be employed.
- cracked distillate containing 0.35% total sulfur in various forms of combination may be treated with 5% by volume of a solution of a potassium polysulfide in 50% ethyl alcohol containing 5% free alkali, treatment being conducted at ordinary temperatures and pressures by circulating from and back to a batch agitator. After suitable supplementary water-washing, it may be found that the sulfur content of the distillate has been reduced to 0.2%. If such a treatment is followed, or in some cases preceded, by supplementary treatment with minimum amounts of 66 B. sulfuric acid, the sulfur content may be found reduced to approximately 0.08%.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkali metal.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkali metal at substantially atmospheric temperature.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alcoholic solution of a polysulfide of an alkali metal.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkaline earth metal.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a sulfidev of an alkali metal.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a polysulfide of an alkali metal.
- a step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a sulfide of an alkaline earth metal.
- a process for refining hydrocarbon oils con taining mercaptans which comprises treating the oil first with plumbite solution and then with an alcoholic solution of a sulphide of an alkalinous metal.
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'Dec. 26, 1933 6 UNITED STATES 1,940,726 TREATMENT OF HYDROCARBQN OILS Jacque C. MorrelL'Chicago, 111., assignor to 'Universal Oil Products Company, Chicago, 111., a j corporation of South Dakota No Drawing. ApplicationJanuary 8, 1931 Serial N- 507,519
8 Claims. (Cl. 196 -24) This invention relatesto the treatment of hydrocarbon oils, and refers more particularly to the treatment of the lighter'distillates produced in the cracking of heavy hydrocarbons.
More specifically the invention contemplates the treatmentof cracked distillates with chemical reagents of a particular nature effective in improving the quality of the distillates as regards their adaptability to commercial uses, particularly as fuels for internal combustion engines.
The chemical nature of the lighter hydrocar' bon fractions produced by the cracking of heavy hydrocarbons under elevated temperatures and pressures is very complex. Representatives of practically all hydrocarbon groups have been identified, such groups being, for example, parafiins, olefines, naphthenes, aromatics, terpenes, et cetera. As-charging oils frequently contain-minor amounts of sulfur, oxygen and nitrogen derivatives of hydrocarbons, the cracked products contain these elements in compounds of altered type due to rearrangements and readjustments during the cracking and subsequent reconversion period. The sulphur originally held in combination in the raw charging stocks'appears as hydrogen sulfide and in such sulfur containing hydrocarbon derivatives as mercaptans, sulfides or sulfur ether, thiophenes, et cetera. Frequently, when the raw cracked distillates are treated with acid or alkaline reagents, such as sulfuric acid or caustic soda, further rearrangements occur, producing compounds of a hybrid nature such as the sulfoxy derivatives. It may be stated generally that the presence of sulfur and/or oxygen compounds is undesirable because of their tendency to render the distillates malodorous and unstable in the presence of polymerizing influences so that frequently the oils go off color and develop gummy or resinous substances during storage. The present invention is concerned with improvements in methods for removing or altering the sulfur compounds in cracked distillates so as to render them either less objectionable from a standpoint of odor and instability or of removing them to a degree required by'oommercial requirements.
In one specific embodiment of the invention, cracked hydrocarbon distillates are treated with preferably alkaline alcoholic solutions of sulfides, hydrosulfides and polysulfides of the alkali and/ or akaline earth metals. While the treatment is preferably used as an adjunct to other treatments, in some cases it may constitute the only treatment necessary. Y
The various sulfides, hydrosulfides and polysulfides of the metals of the groups mentioned vary in their solubility in absolute or anhydrous alcohols, such as ethyl or methyl alcohols, the
. solubility usually increasing as the alcohols are alkali. By proper selection of the'base metal, the
particular sulfide thereof, the strength of alcohol and the free alkali concentration, a wide range of reagents may-be prepared applicable to the treatment of cracked distillates.
Treating reagents prepared as mentioned are particularly effective in removing or altering certain types of sulfur derivatives of hydrocarbons,
the apparent mechanism of the reaction being the polymerizing or condensing of the organic sulfur compounds with the metal sulfides which forms either insoluble precipitates or solublehighboiling compounds which remain behind upon distillation of the lighter fractions of the oils treated. In some instances the compounds formed may be soluble in the reagent and in other cases precipitates may appear which are removed by sedimentation or other means.
Reagents of the type comprised in the present invention are particularly efficacious when used following treatment of cracked distillates with sodium plumbite solutions. The use of sodium pluinbite forms primarily mercaptides of lead which are more or less soluble in the oils. The addition of powdered sulfur, such as flowers of sulfur, to oils containing the lead mercaptides 1 5 causes what is known as a break in the treatment which is really the precipitation of the black lead sulfide, the organic residues combining to formcompounds of the type of disulfides. When sufiicient care is not exercised to avoid 1 0 adding excess of sulfur over that necessary to cause the break a portion of the excess remains dissolved in the oil and apparently oxidizes when the oil is exposed to light and air, causing the a better controlled addition of the amount of sulfur requisite to cause precipitation of the lead as sulfide, assures maximum contact due to easier miscibility and apparently removes some of the sulfides, thus lessening the amount of sulfur left in the oils from both standpoints.
In treating oils with reagents characteristic of the invention operations may be conducted in various types of equipment and in a variety of ways, for example, the oil may be treated in a batch agitator by circulating from the bottom of the cone back into the top through distributing means by means of a circulating pump, the reagent being added to the suction side of the pump and being mixed during passage therethrough and through the nozzles or atomizing means on the discharge side. Reagents may be injected at suitable points in the travel of oils through continuous treating equipment, consisting of mixing devices of various types followed by set,- tling and washing chambers. In some instances relatively strong solutions may be added to oils undergoing distillation with fire and/or steam with retention of desirable compounds in the still residues. In other instances treatment under considerably elevated temperatures and pressures may be advisable, in which case apparatus of requisite strength must be employed.
The foregoing description of the invention has disclosed reagents and methods of operation which are comprised within the scope of the proc ess of the invention, but these have been given for illustrative purposes only and are not to b considered in a limiting sense.
As an example of the results obtainable by the operation of the process of the invention, a
cracked distillate containing 0.35% total sulfur in various forms of combination may be treated with 5% by volume of a solution of a potassium polysulfide in 50% ethyl alcohol containing 5% free alkali, treatment being conducted at ordinary temperatures and pressures by circulating from and back to a batch agitator. After suitable supplementary water-washing, it may be found that the sulfur content of the distillate has been reduced to 0.2%. If such a treatment is followed, or in some cases preceded, by supplementary treatment with minimum amounts of 66 B. sulfuric acid, the sulfur content may be found reduced to approximately 0.08%.
I claim as my invention:
1. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkali metal.
2. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkali metal at substantially atmospheric temperature.
3. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alcoholic solution of a polysulfide of an alkali metal.
4. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alcoholic solution of a sulfide of an alkaline earth metal.
5. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a sulfidev of an alkali metal.
6. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a polysulfide of an alkali metal.
7. A step in a process of desulphurizing the condensed overhead product resulting from the cracking of hydrocarbon oil, which comprises subjecting said oil to treatment with an alkaline alcoholic solution of a sulfide of an alkaline earth metal.
8. A process for refining hydrocarbon oils con taining mercaptans which comprises treating the oil first with plumbite solution and then with an alcoholic solution of a sulphide of an alkalinous metal.
JACQUE C. MORRELL.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US507519A US1940726A (en) | 1931-01-08 | 1931-01-08 | Treatment of hydrocarbon oils |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US507519A US1940726A (en) | 1931-01-08 | 1931-01-08 | Treatment of hydrocarbon oils |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1940726A true US1940726A (en) | 1933-12-26 |
Family
ID=24018950
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US507519A Expired - Lifetime US1940726A (en) | 1931-01-08 | 1931-01-08 | Treatment of hydrocarbon oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1940726A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3354081A (en) * | 1965-09-01 | 1967-11-21 | Exxon Research Engineering Co | Process for desulfurization employing k2s |
| US4248695A (en) * | 1979-10-01 | 1981-02-03 | Rollan Swanson | Desulfurizing a fuel with alkanol-alkali metal hydrosulfide solution |
-
1931
- 1931-01-08 US US507519A patent/US1940726A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3354081A (en) * | 1965-09-01 | 1967-11-21 | Exxon Research Engineering Co | Process for desulfurization employing k2s |
| US4248695A (en) * | 1979-10-01 | 1981-02-03 | Rollan Swanson | Desulfurizing a fuel with alkanol-alkali metal hydrosulfide solution |
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