US2131519A - Method of refining cracked oil by using metallic soaps of naphthenic acid - Google Patents
Method of refining cracked oil by using metallic soaps of naphthenic acid Download PDFInfo
- Publication number
- US2131519A US2131519A US136687A US13668737A US2131519A US 2131519 A US2131519 A US 2131519A US 136687 A US136687 A US 136687A US 13668737 A US13668737 A US 13668737A US 2131519 A US2131519 A US 2131519A
- Authority
- US
- United States
- Prior art keywords
- cracked oil
- oil
- refining
- cracked
- thioalcohols
- 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
- 238000007670 refining Methods 0.000 title description 17
- 238000000034 method Methods 0.000 title description 8
- HNNQYHFROJDYHQ-UHFFFAOYSA-N 3-(4-ethylcyclohexyl)propanoic acid 3-(3-ethylcyclopentyl)propanoic acid Chemical compound CCC1CCC(CCC(O)=O)C1.CCC1CCC(CCC(O)=O)CC1 HNNQYHFROJDYHQ-UHFFFAOYSA-N 0.000 title description 4
- 239000000344 soap Substances 0.000 title description 3
- 239000003921 oil Substances 0.000 description 38
- 150000003839 salts Chemical class 0.000 description 16
- 150000001875 compounds Chemical class 0.000 description 8
- HRKQOINLCJTGBK-UHFFFAOYSA-N dihydroxidosulfur Chemical compound OSO HRKQOINLCJTGBK-UHFFFAOYSA-N 0.000 description 7
- 239000003795 chemical substances by application Substances 0.000 description 6
- 150000007524 organic acids Chemical class 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000003208 petroleum Substances 0.000 description 5
- 238000013019 agitation Methods 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 235000005985 organic acids Nutrition 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 2
- 230000000274 adsorptive effect Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229940120693 copper naphthenate Drugs 0.000 description 2
- SEVNKWFHTNVOLD-UHFFFAOYSA-L copper;3-(4-ethylcyclohexyl)propanoate;3-(3-ethylcyclopentyl)propanoate Chemical compound [Cu+2].CCC1CCC(CCC([O-])=O)C1.CCC1CCC(CCC([O-])=O)CC1 SEVNKWFHTNVOLD-UHFFFAOYSA-L 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 229910000286 fullers earth Inorganic materials 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000001117 sulphuric acid Substances 0.000 description 2
- 235000011149 sulphuric acid Nutrition 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 239000000341 volatile oil Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical class CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 241000779819 Syncarpia glomulifera Species 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000001739 pinus spp. Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011269 tar Substances 0.000 description 1
- 229940036248 turpentine Drugs 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc 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
- C10G29/06—Metal salts, or metal salts deposited on a carrier
-
- 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
Definitions
- the present invention is a division of our copending application which has matured into Patent 2,080,087 May 11, 1937, and relates to a method of refining cracked oil, characterized in that by adding to cracked oil at the ordinary temperature or below it one or more of copper, lead, zinc and iron salts of naphthenic acid in solid state or as dissolved in one or mixture of two or more of gasoline, petroleum, benzol, toluol, xylols, or turpentine, all the compounds of oiiensive odor and other impurities contained in cracked oil may not only be combined with metal or metals in dissolved state and be precipitated as insoluble salts together with the compounds of offensive odor, but also even disagreeable smell compounds very difiicult to react may be adsorbed and precipitated at the same time.
- the object thereof is to bring all of principal sources of offensive odor such as thioalcohols contained in cracked oil into intimate contact at a comparatively low temperature with metallic salts of organic acids soluble in cracked oil, to make them react upon each other directly by double decomposition and precipitate as insoluble salts, and at the same time to make compounds, which are very difficult to react with ordinary refining agents, such as disulphides deposited by the astringent and adsorptive actions of these insoluble salts at the moment of their formation, thus removing these sources of disagreeable odor completely from cracked oil without any operation detrimental to volatile oil, such as agitation, stirring, etc.
- ordinary refining agents such as disulphides deposited by the astringent and adsorptive actions of these insoluble salts at the moment of their formation
- This invention relates to a method of refining the cracked oil produced by the cracking process of petroleum oils, the tars manufactured from coal and shale, and other organic matters and is adapted mainly for removing completely the bad smell compounds contained in cracked oil and at the same time for increasing the stability of the product.
- the bad smell sources in cracked oil are chiefly thioalcohols, di-sulphides and unsaturated organic compounds, above all, low boiling thioalcohols. These substances even in the slightest quantity can give offensive smell to volatile oil. For instance, ethyl thiolacohol can still give disagreeable smell to gasoline even with the concentration M0000 or ti 000 by weight.
- Thioalcohol gives out offensive smell lesser with the increase of its molecular weight, but even crystallizable higher member of thioalcohol has bad smell, and thioalcohol is liable to reduce its reactive power gradually with the increase of its molecular weight.
- the known methods all employ refining agents insoluble in the object to be purified, so that even by any violent agitation the intimate contact of a refining agent with the object to be purified is difficult, more so when their difference in the specific gravity is greater. Therefore, only a portion, but not the whole, of these bad smell compounds are removed and consequently the complete removing of the bad smell source cannot be expected.
- the refining operation the oxidation of thioalcohols is accelerated more and more with the violency of agitation in the atmosphere and therefore this agitation operation does not only make thioalcohols stay as disulphides, but also causes the loss of gasoline due to volatilization and consequently the decrease of the yield of the product.
- the inventors have isolated various kinds of thioalcohols from cracked oil and manufactured various kinds of disulphides therefrom, and then studied their reactions with various kinds of metals and metallic salts of organic and inorganic acids and their various properties including solubilities, stabilities etc. Also they have studied the easiness and speed of the formation of metallic salts from the solutions of thioalcohols and disulphides in petroleum hydrocarbons, and'the behavior of these salts in petroleum hydrocarbons.
- Disulphide produced here is mostly adsorbed into metallic salt of thioalcohol the instant it is produced and is deposited with salt if the product is allowed to be settled spontaneously without stirring and presents the appearance as if this refining reaction had occurred according to only the Equation 1.
- the refined cracked oil may be subjected to steam distillation directly. After the part of gasoline fraction is distilled, the residual oil is stirred with alkali solution and thus naphthenic acid may be recovered as alkali soap from the oil.
- gasoline of superior quality which is not only free from disagreeable smell, but also has very great stability.
- the method of refining cracked oil which consists in dissolving oil-soluble heavy metallic soap of naphthenic acid in a volatile organic solvent which will disperse homogeneously in cracked oil; pouring the solution thus obtained slowly into cracked oil while in a cold state to cause same to disperse naturally and homogeneously without heating or stirring in the cracked oil whereby same will react with the intermingling mercaptans and precipitate same by double decomposition as insoluble metallic salts; separating the precipitate; and distilling the remaining liquor to separate it from the organic solvent.
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)
- Liquid Carbonaceous Fuels (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
Patented Sept. 27, 1938 T T STATES "2,131,519 7 METHOD OF REFINING CRACKED on. B
USING METALLIC SO ACID APS OF NAPHTHENIO Masakichi Mizuta, Marunouchi, Kojimachi-ku,
Tokyo, and Teiji Yoshimura, Okubo, K'ashiwazaki-machi, Kariha-gun, Niigata-ken, Japan, assignors to :NipponSekiyu Kabushiki Kaisha, Tokyo, Japan, a corporation of Japan No Drawing. Original application August 11,
1934, Serial No. 739,500. Divided and this application April 13, 1937, SerialNo. 136,687
1 Claim.
The present invention is a division of our copending application which has matured into Patent 2,080,087 May 11, 1937, and relates to a method of refining cracked oil, characterized in that by adding to cracked oil at the ordinary temperature or below it one or more of copper, lead, zinc and iron salts of naphthenic acid in solid state or as dissolved in one or mixture of two or more of gasoline, petroleum, benzol, toluol, xylols, or turpentine, all the compounds of oiiensive odor and other impurities contained in cracked oil may not only be combined with metal or metals in dissolved state and be precipitated as insoluble salts together with the compounds of offensive odor, but also even disagreeable smell compounds very difiicult to react may be adsorbed and precipitated at the same time.
The object thereof is to bring all of principal sources of offensive odor such as thioalcohols contained in cracked oil into intimate contact at a comparatively low temperature with metallic salts of organic acids soluble in cracked oil, to make them react upon each other directly by double decomposition and precipitate as insoluble salts, and at the same time to make compounds, which are very difficult to react with ordinary refining agents, such as disulphides deposited by the astringent and adsorptive actions of these insoluble salts at the moment of their formation, thus removing these sources of disagreeable odor completely from cracked oil without any operation detrimental to volatile oil, such as agitation, stirring, etc.
This invention relates to a method of refining the cracked oil produced by the cracking process of petroleum oils, the tars manufactured from coal and shale, and other organic matters and is adapted mainly for removing completely the bad smell compounds contained in cracked oil and at the same time for increasing the stability of the product.
The bad smell sources in cracked oil are chiefly thioalcohols, di-sulphides and unsaturated organic compounds, above all, low boiling thioalcohols. These substances even in the slightest quantity can give offensive smell to volatile oil. For instance, ethyl thiolacohol can still give disagreeable smell to gasoline even with the concentration M0000 or ti 000 by weight.
Thioalcohol gives out offensive smell lesser with the increase of its molecular weight, but even crystallizable higher member of thioalcohol has bad smell, and thioalcohol is liable to reduce its reactive power gradually with the increase of its molecular weight.
In cracked oil, the quantity of disulphide orig inally present in it is only very small, the majority being produced by the oxidation from thioalcohol and consequently its quantity increases gradually with the lapse of time after the manufacture of cracked oil. This compound is also the cause for giving a kind of burning smell to cracked oil. It is extremely difficult to react'wlth ordinary refining agents for cracked oil and consequently is difficult to remove.
Some unsaturated organic compounds in cracked oil are very unstable. will mostly polymerize at once, but if diluted with gasoline, they will become comparatively more stable. They give a kind of disagreeable odor to crack-ed oil by their oxidation products. However, they may be removed easily by treatment. with sulphuric acid. I
Now, according to the present method which is the result of the study of the constitutions and properties of many such bad smell compounds, these bad smell sources may be removed completely.
The known methods all employ refining agents insoluble in the object to be purified, so that even by any violent agitation the intimate contact of a refining agent with the object to be purified is difficult, more so when their difference in the specific gravity is greater. Therefore, only a portion, but not the whole, of these bad smell compounds are removed and consequently the complete removing of the bad smell source cannot be expected. In the refining operation, the oxidation of thioalcohols is accelerated more and more with the violency of agitation in the atmosphere and therefore this agitation operation does not only make thioalcohols stay as disulphides, but also causes the loss of gasoline due to volatilization and consequently the decrease of the yield of the product.
The inventors have isolated various kinds of thioalcohols from cracked oil and manufactured various kinds of disulphides therefrom, and then studied their reactions with various kinds of metals and metallic salts of organic and inorganic acids and their various properties including solubilities, stabilities etc. Also they have studied the easiness and speed of the formation of metallic salts from the solutions of thioalcohols and disulphides in petroleum hydrocarbons, and'the behavior of these salts in petroleum hydrocarbons. Thus, by applying the results of these studies to cracked oil and studying the best condition with regard to the refining of cracked oil, they have succeeded in discovering the following matters:
If isolated, they pentine, etc., and, when kept as concentrated solutions, they do not change their qualities.
2. If a solution of metallic salts of these organic acids is added to gasoline or petroleum oils containing thioalcohols, it disperses throughout the latter spontaneously, mixes with it and reacts with thioalcohols by double decomposition even at the ordinary temperature or below it, depositing metallic salts of thioalcohols. Thus, by this way it is possible to remove thioalcohols completely from the oil.
3. Disulphide produced here is mostly adsorbed into metallic salt of thioalcohol the instant it is produced and is deposited with salt if the product is allowed to be settled spontaneously without stirring and presents the appearance as if this refining reaction had occurred according to only the Equation 1.
4. It is necessary that the reaction between metallic salt of organic acid and thioalcohol should proceed slowly. Thus, after the completion of the reaction and the deposition of metallic salt of thioalcohol and disulphide, the supernatant oil is filtered gently through fullers earth filtering bed and thus these bad smell sources may be separated from the oil to be purified completely.
5. The refined cracked oil may be subjected to steam distillation directly. After the part of gasoline fraction is distilled, the residual oil is stirred with alkali solution and thus naphthenic acid may be recovered as alkali soap from the oil.
When the result of the above study was applied to the refining of cracked oil, it was possible to produce cracked gasoline entirely free from thioalcohols and the bad smell of disulphides.
The following are a few examples of refining of cracked oil for the preparation of cracked gasoline:--
Add 0.5% (by volume) of 20% caustic soda solution to kilolitres of the cracked oil produced from Dubbs cracking plant and agitate it to remove sulphuretted hydrogen, organic acids and other reactive substances from the cracked oil. This pre-treatment economizes metallic salt of organic acid to be required. Next, after washing it with water enough to remove alkali-residue completely, dehydrate it. Then, add clear extract solution of copper naphthenate in gasoline,
which is prepared by settling and filtering a solution of 200 kilograms of copper naphthenate in 500 litres of gasoline, to the above cracked oll purifiedby alkali solution and leave the mixture for 8 to 12 hours to settle down insoluble salts produced, after which the supernatant oil is filtered through fullers earth filtering bed. Next, subject the filtrated oil to steam distillation in a steam still and distill ofi the gasoline fraction. Put the gasoline fraction in a continuous treating apparatus and wash it with sulphuric acid, alkali and water by turns. The finished gasoline thus produced has an excellent quality free from disagreeable odor.
Thus, it may be possible to obtain gasoline of superior quality which is not only free from disagreeable smell, but also has very great stability.
This invention as stated above has the following advantages:
1. As a refining agent is brought into very intimate contact with the object to be refined easily, it can react with the whole of bad smell sources of cracked oil,
2. It is possible not only to remove disulphides produced during the reaction of this refining, but also to remove disulphides originally contained in the object to be refined by astringent and adsorptive actions.
3. For the above reason, bad smell sources can be removed completely from cracked oil.
4. As the object to be purified is not stirred or agitated, it is possible to prevent the oxidation of thioalcohols and also minimize the vaporization loss of the volatile portion of the object to be refined.
5. The recovery of refining agent is easy.
We claim:
The method of refining cracked oil, which consists in dissolving oil-soluble heavy metallic soap of naphthenic acid in a volatile organic solvent which will disperse homogeneously in cracked oil; pouring the solution thus obtained slowly into cracked oil while in a cold state to cause same to disperse naturally and homogeneously without heating or stirring in the cracked oil whereby same will react with the intermingling mercaptans and precipitate same by double decomposition as insoluble metallic salts; separating the precipitate; and distilling the remaining liquor to separate it from the organic solvent.
MASAKICHI MIZUTA. TEIJI YOSHIMURAA.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US136687A US2131519A (en) | 1934-08-11 | 1937-04-13 | Method of refining cracked oil by using metallic soaps of naphthenic acid |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US739500A US2080087A (en) | 1934-08-11 | 1934-08-11 | Method of refining cracked oils |
US136687A US2131519A (en) | 1934-08-11 | 1937-04-13 | Method of refining cracked oil by using metallic soaps of naphthenic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
US2131519A true US2131519A (en) | 1938-09-27 |
Family
ID=26834546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US136687A Expired - Lifetime US2131519A (en) | 1934-08-11 | 1937-04-13 | Method of refining cracked oil by using metallic soaps of naphthenic acid |
Country Status (1)
Country | Link |
---|---|
US (1) | US2131519A (en) |
-
1937
- 1937-04-13 US US136687A patent/US2131519A/en not_active Expired - Lifetime
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