US1791521A - Process of refining oil - Google Patents
Process of refining oil Download PDFInfo
- Publication number
- US1791521A US1791521A US52683A US5268325A US1791521A US 1791521 A US1791521 A US 1791521A US 52683 A US52683 A US 52683A US 5268325 A US5268325 A US 5268325A US 1791521 A US1791521 A US 1791521A
- Authority
- US
- United States
- Prior art keywords
- gasoline
- alcohol
- hydroxide
- present
- mixture
- 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 23
- 238000007670 refining Methods 0.000 title description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 28
- 239000000203 mixture Substances 0.000 description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 17
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 17
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 14
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 14
- 235000009508 confectionery Nutrition 0.000 description 12
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 10
- 235000011121 sodium hydroxide Nutrition 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 7
- 239000003518 caustics Substances 0.000 description 7
- 150000003138 primary alcohols Chemical class 0.000 description 6
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Inorganic materials [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 5
- 239000011734 sodium Substances 0.000 description 4
- 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 3
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 3
- 230000001627 detrimental effect Effects 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 150000003333 secondary alcohols Chemical class 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 2
- 238000010306 acid treatment Methods 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 229910052788 barium Inorganic materials 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- HTUMBQDCCIXGCV-UHFFFAOYSA-N lead oxide Chemical compound [O-2].[Pb+2] HTUMBQDCCIXGCV-UHFFFAOYSA-N 0.000 description 2
- YEXPOXQUZXUXJW-UHFFFAOYSA-N lead(II) oxide Inorganic materials [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 238000009666 routine test Methods 0.000 description 2
- UUCCCPNEFXQJEL-UHFFFAOYSA-L strontium dihydroxide Chemical compound [OH-].[OH-].[Sr+2] UUCCCPNEFXQJEL-UHFFFAOYSA-L 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000212342 Sium Species 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910001863 barium hydroxide Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- WMFOQBRAJBCJND-UHFFFAOYSA-M lithium hydroxide Inorganic materials [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000009877 rendering Methods 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 229910001866 strontium hydroxide Inorganic materials 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- 235000011149 sulphuric acid Nutrition 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
-
- 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
- C10G53/00—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
- C10G53/02—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only
- C10G53/12—Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes plural serial stages only including at least one alkaline treatment step
Definitions
- gasoline offered for sale shall be non-reactive or sweet to the-sodium plumbite or doctor test.
- gasoline from the still is refined usually by treatment first with sulfuric acid and then either by treatment with litharge and sodium hydroxide or with sodium hypochlerite, the
- gasoline When gasoline is refined according to the present invention, most of the previously known chemicals for treating processes are not required. In fact, some of them are detrimental if combined with the present process.
- a little normal or primary alcohol is added to the sour gasoline preferably in the raw or untreated state, whichis then treated with a hydroxide of alkali metal or of alkali earth of heavier atomic weight than calcium until sweet to the doctor test.
- the gasoline will then be found to be light stable and of good odor requiring no further treatment.
- a methyl alcohol suitable for use in the present process is pure wood alcohol, approximately test, and substantially free from acetone. I have been successful in rendering gasolines, both sweet to the doctor test and light stable when using as little as of 1% by volume of methyl alcohol to gasoline treated.
- the amount of alcohol necessary when using a given primary alcohol and a given gaso-. line can be readily determined by a routine test prior to commercial operation,
- the presence of acetone in the alcohol used according to the present process does not prevent the resulting gasoline from being sweet, but it is not completely light stable. It is, however, improved as to its characteristics toward light in that While it goes off color slowly it does so without production of cloud or gum. Acetone by itself without alcohol is not efiective in making gasoline either sweet to the doctor test or completely light stable.
- the alkaline material or hydroxide used along with or subsequent to the treatment of the gasoline with normal alcohol according to the present invention may be either putas sium, sodium, lithium, barium or strontium hydroxide.
- lithium, barium and strontium hydroxides must remain in contact with the alcohol treated gasoline a longer time than potassium or sodium hydroxide to make it sweet.
- caustic soda is the most available alkaline substance for use according to the present invention. It may be added to the gasoline preferably in a powdered state after or along with the treatment with the alcohol with agitation of the caustic and gasoline till sweet to the doctor test.
- the preferable method is to percolate the alcohol treated gasoline through a mass of granulated caustic soda until sweet to the doctor test.
- a sirupy solution of caustic soda or caustic potash in pure methyl alcohol may be used instead of treatment first with the alcohol and then with the hydroxide, but a dilute solution is not operative.
- As little as 0.2 lb. of powdered caustic soda per barrel of gasoline is often effective in producing a sweet li ht stable gasoline according to the present invention.
- the amount of caustic or other hydroxide required in treating gasoline according to the present invention varies with the gasoline and the hydroxide and may be determined readily for any given gasoline and a given hydroxide by a routine test preliminary to commercial operation.
- the gasoline to be treated by the present process must be substantially free from water throughout the process in order to obtain the desired results. Moreover, the gasoline used must be unsweetened. If the gasoline has been sweetened by either the sodium plumbite or sodium hypochlorite treatment, subsequent treatment according to the present invention is not efi'ective in producing a light stable gasoline.
- Acid treatment with 66 Beaum sulfuric acid may be applied before the treatment according to the present process without detriment but it is not necessary. Acid treatment with Beaum sulfuric acid however is detrimental either before or after treatment of the gasoline according to the present process, and especially detrimental after it..
- the process of refining gasoline according to the present invention is applicable to gasolines direct from the still without any redistillation.
- the major portion of the experimental work done on the present invention has been on a blerd of distillates direct from the pressure still and direct from the crude still.
- Gasoline treated by the process of the present invention is of greatly improved odor and needs no further treatment to improve its odor for sale.
- the rocess of the present invention does not c ange the original color of the gasoline.
- phase caustic alkali hydroxide or alkali hydroxide is used in the following claims, hydroxides of the heavy earth metals, barium and strontium, are intended to be included.
- the alcohol referred to in the claims as high-test alcohol may contain some acetone.
- the acetone is effective along with the alcohol in preventing gum formation as described above and comes within the contemplated scope of the present invention.
- a process of treating gasoline comprising removing water from the gasoline, mixing with the dry gasoline a high test alcohol, mixing the alcohol-gasoline mixture with a dry caustic alkali hydroxide, and separating the alcohol-gasoline mixture from the alkali hydroxide.
- a process of treating gasoline comprising mixing less than one per cent of substantially dry methyl alcohol with the gasoline, treatin the mixture with a caustic alkali hydroxide, and separating the mixture from the alkali hydroxide.
- a process of treating gasoline comprising mixing a small amount of the methyl alco 01 with the gasoline and passing the gasoline-alcohol mixture through a bed of powdered caustic hydroxide.
- a process of treating asoline comprising removing water from t e gasoline, mixing substantially pure methyl alcohol with the dry gasoline, and passing the gasolinealcohol mixture through a bed of powdered sodium hydroxide.
- a process for refining gasoline comprising mixing a dry normal alcohol with substantially dry raw gasoline, contacting the resulting alcohol-gasoline mixture with adry powdered alkali hydroxide, and separating the alcohol-gasoline mixture from the alkali hydroxide.
- the process of treating gasoline comprising forming a mixture of substantially dry gasoline with less than 1% of its volume of substantially dr alcohol, contacting the mixture with dry a ali hydroxide, and separatin the mixture from the alkali hydroxide.
- the process of treating gasoline to render it light stable which comprises formin a solution of dry unsweetened gasoline wit% a relatively small proportion of dry primary alcohol, contacting the resulting gasolinealcohol solution with an alkali hydroxide, and separating the gasoline-alcohol solution from the alkali hydroxide.
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
atented Feb. 10, 1931 PATENT! OFFICE AUGUST P. BJ'ERREGAARD, OF OKMULGEE, OKLAHOMA PROCESS OF REFINING- OIL No Drawing.
One of the present day standard requirements in the gasoline trade is that gasoline offered for sale shall be non-reactive or sweet to the-sodium plumbite or doctor test. As is well known, moreover, gasoline from the still is refined usually by treatment first with sulfuric acid and then either by treatment with litharge and sodium hydroxide or with sodium hypochlerite, the
treatment with litharge and sodium hydroxide or with hypochlorite being necessary to render the gasoline sweet to the doctor test.
It is the custom at present, moreover, at manyretail gasoline or filling stations to exhibit to the customer the product being sold by using filling bowls of glass. Ithas developed that many gasolines refined so as to pass the doctor and other ordinary trade tests are light sensitive, causing the gasoline toturn darker in the glass filling bowls on standing therein and also depositing a film of dark gum that collects on the glass, thus doubly darkening the tint of the gasoline as viewed by the purchaser. According to the present invention, straight-run and cracked gasoline or mixtures of straight-run and cracked gasolines are refined to produce a gasoline which is sweet to the doctor test, non-corrosive, of good odor'and light stable. The term light stable as just used is intended to include both the characteristics of not substantially darkening and of not depositing gum upon exposure to light.
When gasoline is refined according to the present invention, most of the previously known chemicals for treating processes are not required. In fact, some of them are detrimental if combined with the present process. In refining gasoline according to the present invention, a little normal or primary alcohol is added to the sour gasoline preferably in the raw or untreated state, whichis then treated with a hydroxide of alkali metal or of alkali earth of heavier atomic weight than calcium until sweet to the doctor test. The gasoline will then be found to be light stable and of good odor requiring no further treatment.
Application filed August 26, 1925. Serial No. 52,683.
The primary alcohols used according to the whereas normal propyl, normal butyl and higher normal or primary alcohols act more slowly and still more slowly. A methyl alcohol suitable for use in the present process is pure wood alcohol, approximately test, and substantially free from acetone. I have been successful in rendering gasolines, both sweet to the doctor test and light stable when using as little as of 1% by volume of methyl alcohol to gasoline treated. The amount of alcohol necessary when using a given primary alcohol and a given gaso-. line can be readily determined by a routine test prior to commercial operation, The presence of acetone in the alcohol used according to the present process does not prevent the resulting gasoline from being sweet, but it is not completely light stable. It is, however, improved as to its characteristics toward light in that While it goes off color slowly it does so without production of cloud or gum. Acetone by itself without alcohol is not efiective in making gasoline either sweet to the doctor test or completely light stable.
None of the secondary alcohols, if used instead of methyl or other primar alcohol in the present process, makes t e gasoline finally and fully sweet to the doctor test, even after twenty-four hours action. They, however, favorably affect the gasoline as to its reaction when exposed to light, the color of the gasoline after light exposure being less intense if it has been first treated with secondary alcohol and caustic soda or equivalent hydroxide. The secondary alcohols, however, develop a strong yellow tone in the gasoline if attempted to be used according to the present invention.
The alkaline material or hydroxide used along with or subsequent to the treatment of the gasoline with normal alcohol according to the present invention may be either putas sium, sodium, lithium, barium or strontium hydroxide. However, lithium, barium and strontium hydroxides must remain in contact with the alcohol treated gasoline a longer time than potassium or sodium hydroxide to make it sweet. Commercially, caustic soda is the most available alkaline substance for use according to the present invention. It may be added to the gasoline preferably in a powdered state after or along with the treatment with the alcohol with agitation of the caustic and gasoline till sweet to the doctor test. The preferable method, however, is to percolate the alcohol treated gasoline through a mass of granulated caustic soda until sweet to the doctor test. A sirupy solution of caustic soda or caustic potash in pure methyl alcohol may be used instead of treatment first with the alcohol and then with the hydroxide, but a dilute solution is not operative. As little as 0.2 lb. of powdered caustic soda per barrel of gasoline is often effective in producing a sweet li ht stable gasoline according to the present invention. The amount of caustic or other hydroxide required in treating gasoline according to the present invention varies with the gasoline and the hydroxide and may be determined readily for any given gasoline and a given hydroxide by a routine test preliminary to commercial operation.
The use of normal alcohol alone without subsequent treatment with hydroxide does not produce the desired result. The same is true of treatment with caustic alone without treatment with normal alcohol.
The gasoline to be treated by the present process must be substantially free from water throughout the process in order to obtain the desired results. Moreover, the gasoline used must be unsweetened. If the gasoline has been sweetened by either the sodium plumbite or sodium hypochlorite treatment, subsequent treatment according to the present invention is not efi'ective in producing a light stable gasoline.
Acid treatment with 66 Beaum sulfuric acid may be applied before the treatment according to the present process without detriment but it is not necessary. Acid treatment with Beaum sulfuric acid however is detrimental either before or after treatment of the gasoline according to the present process, and especially detrimental after it..
The process of refining gasoline according to the present invention is applicable to gasolines direct from the still without any redistillation. In fact, the major portion of the experimental work done on the present invention has been on a blerd of distillates direct from the pressure still and direct from the crude still.
Gasoline treated by the process of the present invention is of greatly improved odor and needs no further treatment to improve its odor for sale. As to color, the rocess of the present invention does not c ange the original color of the gasoline.
It will be understood that wherever the phase caustic alkali hydroxide or alkali hydroxide is used in the following claims, hydroxides of the heavy earth metals, barium and strontium, are intended to be included.
It will be understood further that the alcohol referred to in the claims as high-test alcohol may contain some acetone. The acetone is effective along with the alcohol in preventing gum formation as described above and comes within the contemplated scope of the present invention.
Having thus described my invention, I claim:
1. A process of treating gasoline comprising removing water from the gasoline, mixing with the dry gasoline a high test alcohol, mixing the alcohol-gasoline mixture with a dry caustic alkali hydroxide, and separating the alcohol-gasoline mixture from the alkali hydroxide.
2. A process of treating gasoline comprising mixing less than one per cent of substantially dry methyl alcohol with the gasoline, treatin the mixture with a caustic alkali hydroxide, and separating the mixture from the alkali hydroxide.
3. A process of treating gasoline comprising mixing a small amount of the methyl alco 01 with the gasoline and passing the gasoline-alcohol mixture through a bed of powdered caustic hydroxide.
4. A process of treating asoline comprising removing water from t e gasoline, mixing substantially pure methyl alcohol with the dry gasoline, and passing the gasolinealcohol mixture through a bed of powdered sodium hydroxide. D
5. A process for refining gasoline comprising mixing a dry normal alcohol with substantially dry raw gasoline, contacting the resulting alcohol-gasoline mixture with adry powdered alkali hydroxide, and separating the alcohol-gasoline mixture from the alkali hydroxide.
t). The process of treating gasoline comprising forming a mixture of substantially dry gasoline with less than 1% of its volume of substantially dr alcohol, contacting the mixture with dry a ali hydroxide, and separatin the mixture from the alkali hydroxide.
7. The process of treating gasoline to render it light stable, which comprises formin a solution of dry unsweetened gasoline wit% a relatively small proportion of dry primary alcohol, contacting the resulting gasolinealcohol solution with an alkali hydroxide, and separating the gasoline-alcohol solution from the alkali hydroxide.
8 The process of treating sour gasolines, which comprises forming a mixture of substantially dry gasoline with a relatively small 1,701,5si r I roportion of substantial dry primary alcool, contacting the resulting mixture with a substantially dry alkali hydroxide, and separating the said mixture from the alkali hydroxide.
9. The process of treating sour gasolines, which comprises contacting the gasoline with concentrated sulphuric acid, thereafter forming a mixture of the gasoline with a small proportion of substantially dry primary alcohol, contacting the resulting mixture with a sub stantially dry alkali hydroxide, and se arating the said mixture from the alkali ydroxlde.
In testimony whereof I aflix my signature.
AUGUST P. BJERREG-AARD.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US52683A US1791521A (en) | 1925-08-26 | 1925-08-26 | Process of refining oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US52683A US1791521A (en) | 1925-08-26 | 1925-08-26 | Process of refining oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1791521A true US1791521A (en) | 1931-02-10 |
Family
ID=21979220
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US52683A Expired - Lifetime US1791521A (en) | 1925-08-26 | 1925-08-26 | Process of refining oil |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1791521A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2445064A (en) * | 1939-10-30 | 1948-07-13 | Tootal Broadhurst Lee Co Ltd | Alkali metal hydroxide liquid reagent |
| US2663674A (en) * | 1950-03-17 | 1953-12-22 | Standard Oil Co | Refining sour hydrocarbon oils |
| US2726993A (en) * | 1951-11-15 | 1955-12-13 | Exxon Research Engineering Co | Process for improving liquid fuels by treating with propanol and a metal passivator |
| US2912374A (en) * | 1955-06-22 | 1959-11-10 | Shell Dev | Sulfuric acid sweetening of straight run petroleum distillates |
| US3258421A (en) * | 1964-11-13 | 1966-06-28 | Standard Oil Co | Desulfurization of hydrocarbon oils |
| US6110237A (en) * | 1995-09-29 | 2000-08-29 | Leonard Bloom | Emergency fuel for use in an internal combustion engine |
| US6113660A (en) * | 1995-09-29 | 2000-09-05 | Leonard Bloom | Emergency fuel for use in an internal combustion engine and a method of packaging the fuel |
-
1925
- 1925-08-26 US US52683A patent/US1791521A/en not_active Expired - Lifetime
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2445064A (en) * | 1939-10-30 | 1948-07-13 | Tootal Broadhurst Lee Co Ltd | Alkali metal hydroxide liquid reagent |
| US2663674A (en) * | 1950-03-17 | 1953-12-22 | Standard Oil Co | Refining sour hydrocarbon oils |
| US2726993A (en) * | 1951-11-15 | 1955-12-13 | Exxon Research Engineering Co | Process for improving liquid fuels by treating with propanol and a metal passivator |
| US2912374A (en) * | 1955-06-22 | 1959-11-10 | Shell Dev | Sulfuric acid sweetening of straight run petroleum distillates |
| US3258421A (en) * | 1964-11-13 | 1966-06-28 | Standard Oil Co | Desulfurization of hydrocarbon oils |
| US6110237A (en) * | 1995-09-29 | 2000-08-29 | Leonard Bloom | Emergency fuel for use in an internal combustion engine |
| US6113660A (en) * | 1995-09-29 | 2000-09-05 | Leonard Bloom | Emergency fuel for use in an internal combustion engine and a method of packaging the fuel |
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