US597920A - Eric a - Google Patents
Eric a Download PDFInfo
- Publication number
- US597920A US597920A US597920DA US597920A US 597920 A US597920 A US 597920A US 597920D A US597920D A US 597920DA US 597920 A US597920 A US 597920A
- Authority
- US
- United States
- Prior art keywords
- oils
- oil
- california
- illuminating
- treatment
- 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 description 54
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 24
- 238000000034 method Methods 0.000 description 23
- 238000011282 treatment Methods 0.000 description 14
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Substances [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 11
- 238000007670 refining Methods 0.000 description 10
- 235000011121 sodium hydroxide Nutrition 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 239000003518 caustics Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 239000003208 petroleum Substances 0.000 description 5
- 206010001497 Agitation Diseases 0.000 description 4
- 238000013019 agitation Methods 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000001473 noxious effect Effects 0.000 description 3
- 239000000779 smoke Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C10G17/09—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acid salts
Definitions
- My invention relates to a new process of purifying and refining California petroleumoils for illuminating purposes, in which I first remove from said oils the less refractory bodies contained therein by treatingsaid oils with concentrated caustic lye or sulfuric acid.
- My invention is particularly applicable to and particularly concerns that class of petroleum-oils which on account of certain distinctive peculiarities has come to be known commercially and otherwise by the descriptive term of California oils.
- California oils is not used in the geographical sense or to signify geographical limitation to the State of California alone. On the contrary, it is used to designate a certain allied species or class of petroleum-oils occurring in the State of California and also to some extent in the States and Territories bordering upon or adjacent to the Pacific coast of the United States, which oils, by reason of their containing and being saturated with an excessive quantity of refractory bodies and matters of a carbonaceous nature, have hitherto resisted all efforts and attempts to make, manufacture, or in any way produce therefrom an illuminating-oil that would burn in any form of lamp or burner hitherto invented or known to the trade without giving off undue smoke and without emitting noxious vapors in undue quantities. These refractory bodies and matters of a carbonaceous nature so present in these California oils have constantly tended to clog and have clogged from time to time the wicks of any and of all kinds of lamps and burners, and
- I first IOO subject the crude oil to a single distillation, thereby eliminating from it the heavier and non-volatile tarry matters. I then mix with the resultant distillate from five to twenty per cent., by weight, of the ordinary sulfuric acid of about 66 Baum, or from ten to twenty-five per cent., by weight, of concentrated soda-lye or other caustic lye of about 45 Baum, and heat the mass While so mixed to a temperature of about 160 Fahrenheit when sulfuric acid is employed; but in order to facilitate the reaction a temperature exceeding 200 Fahrenheit is preferable when soda-lye or other caustic lye is employed, and I agitate the mass all the 'while with an airblast or other mechanical means for about an -hour7s time, @e length of the time of agita tion dependingon the density of the distillate.
- the amount of sulfuric anhydrid ($0,) I employ depends wholly on the density of the distillate to be purified and also on the purity of the original petroleum.
- WVhen distillates of about 45 Baum are to be treated, five per cent. of sulfuric anhydrid (S0 is generally sufiicient to purify the oil 3 but the oil from some wells requires much more, often as much as fifteen per cent. WVhen a distillate of greater gravity is to be refined, more of the S0 is required, as it seems that the heavier oils contain more of the refractorybodies than the lighter.
- S0 sulfuric anhydrid
- the sulfuric anhydrid is added to a distillate, the reaction is very violent, but of short duration, depending to some extent on the gravity of the oil employed and the form of the sulfuric anhydrid.
- the solid SO can be employed.
- the solid form of sulfuric anhydrid cannot be employed, as the crystals of the S0 are at once completely surrounded with a coating of black tarry matter, which prevents any further action. Therefore an admixture of some other matter is necessary in order to prevent this coating.
- Sulfuric acid (H 80 as an admixture making fuming acid must then be employed, as it is the cheapest method of diluting the SO Phosphoric acid is better than sulfuric acid as a diluent, and boric acid makes a solid form, which gives good results.
- SO Phosphoric acid As a diluent, and boric acid makes a solid form, which gives good results.
- boric acid makes a solid form, which gives good results.
- almost any substance that will not make a stable compound with the S0 will answer the purpose of a diluent. The idea is to get it into the oil and prevent the coating of the crystals with tarry matter. When once in the oil, sulfuric anhydrid seems to attack the refractory bodies, making a tarry mass.
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
UNITED STATES PATENT Ca rion,
ERIC A. STARKE, OF SAN RAFAEL, CALIFORNIA.
PROCESS OF PURIFYING AND REFINING CALIFORNIA PETROLEUM-OILS.
SPECIFICATION forming part of Letters Patent No. 597,920, dated January 25, 1898.
Application filed August 31, 1896. Serial No. 604,484 (No specimens) To all whom it may concern:
Be it known that 1, Euro A. STARKE, a citizen of the United States, residing at San Rafael, county of Marin, State of California, have invented an Improvement in the Processes of Purification and Refining of California Petroleum -Oils for Illuminating Purposes; and I hereby declare the following to be a full, clear, and exact description of the same.
My invention relates to a new process of purifying and refining California petroleumoils for illuminating purposes, in which I first remove from said oils the less refractory bodies contained therein by treatingsaid oils with concentrated caustic lye or sulfuric acid.
and in which I secondly remove from the resulting mass the more refractory bodies by treating said resulting mass with sulfuric anhydrid or such solution of sulfuric anhydrid, as is hereinafter more particularly described.
My invention is particularly applicable to and particularly concerns that class of petroleum-oils which on account of certain distinctive peculiarities has come to be known commercially and otherwise by the descriptive term of California oils.
The term California oils is not used in the geographical sense or to signify geographical limitation to the State of California alone. On the contrary, it is used to designate a certain allied species or class of petroleum-oils occurring in the State of California and also to some extent in the States and Territories bordering upon or adjacent to the Pacific coast of the United States, which oils, by reason of their containing and being saturated with an excessive quantity of refractory bodies and matters of a carbonaceous nature, have hitherto resisted all efforts and attempts to make, manufacture, or in any way produce therefrom an illuminating-oil that would burn in any form of lamp or burner hitherto invented or known to the trade without giving off undue smoke and without emitting noxious vapors in undue quantities. These refractory bodies and matters of a carbonaceous nature so present in these California oils have constantly tended to clog and have clogged from time to time the wicks of any and of all kinds of lamps and burners, and
the said refractory bodies and matters of a carbonaceous nature. 1
All methods and processes heretofore known and used in the treatment, purification, and refining of the said California petroleum-oils, so as to produce from them illuminating-oils, have been carried out by means of a treatment with sulfuric acid of about 66 Baum at temperatures varying from 60 Fahrenheit to 250 Fahrenheit. The said methods and processes heretofore known and used in the treatment, purifying, and refining of California petroleum-oils have never been successful in producing from them an illuminatingoil that Would burn without undue smoke and without emitting noxious vapors in excessive quantities or that could be sold by itself as an illuminating-oil in the regular and ordinary course of trade or commerce. So. refractory have been these bodies and matters of a carbonaceous nature in these California oils that it has been necessary in the production and refining of illuminating-oils from them to resort to three or four separate and successive distillations of the same batches of oil accompanying and as part of the treatment with said sulfuric acid, thereby entailing large outlays and expenses in labor, fuel, loss of time, wear and tear of plant, and diminution by losses arising from successive distillations in percentages of illuminating-oils obtained.
In my invention and process I have overcome these difficulties by, first, removing the less refractory bodies contained in the California petroleum-oils or their distillates by treating the same with concentrated caustic lye or sulfuric acid, and, secondly, and as part of the same invention and process by treatment of the resulting mass with sulfuric anhydrid or such solutions of sulfuric auhydrid as are hereinafter described.
In the application of my invention and process I proceed substantially as follows: I first IOO subject the crude oil to a single distillation, thereby eliminating from it the heavier and non-volatile tarry matters. I then mix with the resultant distillate from five to twenty per cent., by weight, of the ordinary sulfuric acid of about 66 Baum, or from ten to twenty-five per cent., by weight, of concentrated soda-lye or other caustic lye of about 45 Baum, and heat the mass While so mixed to a temperature of about 160 Fahrenheit when sulfuric acid is employed; but in order to facilitate the reaction a temperature exceeding 200 Fahrenheit is preferable when soda-lye or other caustic lye is employed, and I agitate the mass all the 'while with an airblast or other mechanical means for about an -hour7s time, @e length of the time of agita tion dependingon the density of the distillate. The higher the specific gravity of the said distillate the greater would bethe percentage of the said acid or of the said caustic lyes that I would use and also the longer the time I would allow for the agitation. After the completion of this first agitation with ordinary sulfuric acid or with caustic lye, as aforesaid, (and by which treatment all of the less refractory matters are removed, leaving only those of a more stable combination in the said resulting mass,) the said resulting mass is allowed to rest and the tarry residuum (or sludge) is drawn off. There has now been eliminated from the oil all refractory bodies and matters of a carbonaceous nature that are in any way or at all susceptible of elimination by any form or method of treatment with ordinary sulfuric acid or by any form or method of treatment with any alkaline substances; but there are still left in the oil certain other and still more refractory bodies and matters of a carbonaceous nature that cannot be taken away or eliminated in any way or at all by any form or strength of ordinary sulfuric acid, or by any method or kind of treatment therewith, or by any method or kind of treatment with any alkaline sub stances. Up to this point and at this stage of the process said oil could not be successfully burned in any form of lamp or burner hitherto invented or known to the trade. It becomes now, therefore, necessary to use some further and more powerful agent that will act upon and eliminate this class of still more refractory bodies and matters. For this purpose I now use and subject the oil to treatment with sulfuric anhydrid or solutions thereof,
as are hereinafter described.
The amount of sulfuric anhydrid ($0,) I employ depends wholly on the density of the distillate to be purified and also on the purity of the original petroleum.
WVhen distillates of about 45 Baum are to be treated, five per cent. of sulfuric anhydrid (S0 is generally sufiicient to purify the oil 3 but the oil from some wells requires much more, often as much as fifteen per cent. WVhen a distillate of greater gravity is to be refined, more of the S0 is required, as it seems that the heavier oils contain more of the refractorybodies than the lighter.
WVhen the sulfuric anhydrid is added to a distillate, the reaction is very violent, but of short duration, depending to some extent on the gravity of the oil employed and the form of the sulfuric anhydrid. When a light-gravity oil is treated, the solid SO can be employed. When a heavier form of distillate is used, the solid form of sulfuric anhydrid cannot be employed, as the crystals of the S0 are at once completely surrounded with a coating of black tarry matter, which prevents any further action. Therefore an admixture of some other matter is necessary in order to prevent this coating. Sulfuric acid (H 80 as an admixture making fuming acid must then be employed, as it is the cheapest method of diluting the SO Phosphoric acid is better than sulfuric acid as a diluent, and boric acid makes a solid form, which gives good results. In fact, almost any substance that will not make a stable compound with the S0 will answer the purpose of a diluent. The idea is to get it into the oil and prevent the coating of the crystals with tarry matter. When once in the oil, sulfuric anhydrid seems to attack the refractory bodies, making a tarry mass. It also seems to split off from the molecules of the oil some of the carbon and hydrogen sufficient to make a light hyrocarbon and then combine/ therewith, the resulting combination not being soluble in the oil. I have come to this conclusion from the fact that the fire testof oil thus treated is raised from 20 to 40 Fahrenheit. This may possibly be explained also by the fact that light hydrocarbon oils are held in solution by the petroleum and thatsulfuric anhydrid is capable of combining therewith. Be this as it may, ordinary sulfuric acid (H 80 is wholly incapable of effecting its removal. I then agitate the mass, at the same time never allowing the temperature to fall below 80 Fahrenheit. all chemical activity has ceased, which is made evident by the amount of heat required to be applied to the mass in order to maintain the. temperature thereof above 80 Fahrenheit. After all chemical action has ceased the mass is allowed to rest and the black and thick tarry residuev is drawn off, and the oil is then subjected to successive washings with water and soda-lye or otheralkaline substances in the ordinary way. The oil is now ready for use and is fully equal in quality and in illuminating power to the best grades and brands of Eastern water-white illuminating-oils and equally with them will burn in any form of lamp without giving Off smoke or emitting noxious vapors.
Bymy invention and process as above described there is accomplished for the first time that which has never been accomplished or brought about by any other process or method of treatment hitherto invented, used, or employed upon or in connection with the This agitation is continued until' said California oils-that is to say, the production from the said California oils of "an illuminating-oil that will burn in any form of lamp or burner that has ever been invented or known to the trade with equal illuminating power and in all respects as Well as the best brands of eastern water-White illuminating-oils.
Among the other advantages and improvements resulting from the application of my invention and process to the treatment of the said California oils may be mentioned the following: First, the raising of the fire test of said oils; secondly, the ability to refine and produce high grade illuminating-oils from and thereby to utilize California crude petroleum of a higher specific gravity than has ever been susceptible of successful treatment or refining by any other method or process hitherto employed; thirdly, the obtaining from said California crude petroleum of apercentage pf high-grade illuminating-oil greater even than the percentage of poor and inferior illuminating-oil hitherto obtain ed therefrom, and, fourthly, the accomplishing by one distillation of what has never been accomplished with or in regard to California oils even when employing the three or four distillationshitherto always made use of in treating and refining said oils, and from this result large economyand saving in labor,fuel,tin1e,and general Wear and tear of plant andmachinery and in the percentage of loss consequent upon and hitherto regularly ensuing from the repeated and successive distillations that have been necessarily employed.
Having thus described my invention,what I claim as new, and desire to secure by Letters Patent, is
1. The process herein described of treating, purifying and refining California petroleum-oils, so as to produce from them illuminating-oils which process consists,essentially, in first removingthe less refractory substances by treating said oils with a solvent or menstruum and then treating the resulting product vvith sulfuric anhydrid to remove the more refractory substances.
2. The improved process herein described of treating, purifying and refining Califor nia petroleum-oils, so as to produce from them illuminating-oils, which consists, essentially,in first removing the less refractory bodies by treating said oils,with a solvent or menstruuni in the presence of heat and then removing from the resulting mass the more refractory bodies by treating said mass with sulfuric anhydrid.
In witness whereof I have hereunto set my Witnesses Wu. F. Boo'rH, HOLLAND SMITH.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US597920A true US597920A (en) | 1898-01-25 |
Family
ID=2666564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US597920D Expired - Lifetime US597920A (en) | Eric a |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US597920A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2447529A (en) * | 1938-04-05 | 1948-08-24 | Petrolite Corp | Method for removing impurities from hydrocarbons |
-
0
- US US597920D patent/US597920A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2447529A (en) * | 1938-04-05 | 1948-08-24 | Petrolite Corp | Method for removing impurities from hydrocarbons |
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