US537121A - Deodorizing mineral oils - Google Patents
Deodorizing mineral oils Download PDFInfo
- Publication number
- US537121A US537121A US537121DA US537121A US 537121 A US537121 A US 537121A US 537121D A US537121D A US 537121DA US 537121 A US537121 A US 537121A
- Authority
- US
- United States
- Prior art keywords
- oil
- acetylenes
- oils
- odor
- deodorizing
- 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
- 230000001877 deodorizing effect Effects 0.000 title description 6
- 239000002480 mineral oil Substances 0.000 title description 5
- 239000003921 oil Substances 0.000 description 37
- 238000000034 method Methods 0.000 description 22
- 230000008569 process Effects 0.000 description 22
- 125000002534 ethynyl group Chemical class [H]C#C* 0.000 description 17
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 13
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 13
- 239000010949 copper Substances 0.000 description 13
- 229910052802 copper Inorganic materials 0.000 description 13
- BERDEBHAJNAUOM-UHFFFAOYSA-N copper(I) oxide Inorganic materials [Cu]O[Cu] BERDEBHAJNAUOM-UHFFFAOYSA-N 0.000 description 11
- KRFJLUBVMFXRPN-UHFFFAOYSA-N cuprous oxide Chemical compound [O-2].[Cu+].[Cu+] KRFJLUBVMFXRPN-UHFFFAOYSA-N 0.000 description 11
- 229940112669 cuprous oxide Drugs 0.000 description 11
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 10
- 239000005864 Sulphur Substances 0.000 description 9
- 239000000470 constituent Substances 0.000 description 8
- 239000010779 crude oil Substances 0.000 description 6
- 230000006378 damage Effects 0.000 description 6
- 238000004332 deodorization Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 229960004643 cupric oxide Drugs 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 238000010494 dissociation reaction Methods 0.000 description 3
- 230000005593 dissociations Effects 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910044991 metal oxide Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000167854 Bourreria succulenta Species 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000019693 cherries Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 150000001879 copper Chemical class 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
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
Definitions
- This invention relates to the art of deodorizing crude and raw mineral oils, such as Lima oil and Canadian oils, which require a different treatment from the ordinary American oils (generally known as Pennsylvania oil),because of their penetrating and disagreeable odor. It is a well-known fact that these kinds of oil are almost unmarketable on account of this disgusting odor and various processes have been invented and patented, having for their object the removal of the disagreeable odor, either from the crude oil prior to or during distillation or from the distillate.
- My invention therefore, consists in the effectual elimination of the objectionable acetylenes, which results in the purification and deodorization of the oils undergoing treatment by my process.
- the principle which underlies my process is to produce an oxidizing action on the acetylenes at a comparatively low temperature, thereby separating them into carbonic acid and water.
- copper scales which, as above stated, are the medium employed for the dissociation of the constituents of the acetylenes, are a mixture of the cupric oxide and cuprous oxide; but in carrying out my process, the cupric oxide remains practically inert, while the cuprous oxide, at a certain degree of temperature, accomplishes the dissociation, and thereby the destruction of the objectionable acetylenes, resulting in simultaneous deodorization.
- a temperature of 120 Celsius has been reached, and the oil commences to boil, but be fore vaporization has set in, it is removed from the fire and allowed to cool, and the copper scale is removed by drawing off the oil, by
- the copper scale after it has been removed from the deodorized oil, may be regenerated by roasting to a dark cherry red heat, after which it is cooled off, when it is ready for use over again; and in this manner a great quantity of copper scale may be used over and over again for deodorizing purposes with only a nominal waste.
- the batch of oil after undergoing my preliminary process of deodorization, will be found to contain the same percentage of sulphur as the crude oil contained prior to my preliminary treatment;a fact which proves conclusively that the unpleasant odor cannot be due to the presence of sulphur compounds, because if that were so, the test of the deodorized oil would show the entire absence of sulphur, or, at least a greatly reduced percentage thereof.
- the cupric oxide contained in the copper scales would be sufficient to oxidize and neutralize the sulphur, whereas by my improved process, which operates on the acetylenes, the cupric oxide is practically inert, the efiect being wholly due to the chemical action of the cuprous oxide upon the constituent parts, (carbonic acid and water,) of the acetylenes.
- the mixture of oil and copper scale should be heated to (approximately) 120 Celsius in order to produce a reaction of the cuprous oxide.
- the so-called cold processes which aim at the deodorization of the oil simply by mixing it with certain metallic oxides, Without heating the moisture or by heating the moisture up to the point at which distillation begins, are not applicable to my purpose, because unless the mixture is heated to the boiling point, the reaction of the cuprous oxide will not take place, that is to say, the cuprous oxide will not give ofli' its oxygen, by the combination of which with the acetylenes, the constituent parts of the latter, viz., carbonic acid and hydrogen are dissociated.
- deodorizing mineral oils which consists in dissociating the acetylenes contained in said oils by mixing them with cuprous oxide and heating the mixture to a temperature of the boiling point of the oils, substantially as set forth.
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- 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)
- Lubricants (AREA)
- Fats And Perfumes (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
UNITE STATES PATENT Crrrca.
CLEMENS LOSSEN, on HOBOKEN, NEW JERSEY.
DEODORIZING MINERAL OILS.
SPECIFICATION forming part Of Letters Patent No. 537,121, dated April 9, 1895. Application fi September 27, 1892. Renewed February 27, 1895- Serial No. 53 1 (N0 p mena) I To all whom) it may concern:
Be it known that I, CLEMENS LOSSEN, a subject of His Majesty the Emperor of Germany,
residing in Hoboken, in the county of Hudson and State of New Jersey, have invented certain new and useful Improvements in Deodorizing Mineral Oils; and I do hereby declare that the following is a full, clear, and exact description of the invention, which will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to the art of deodorizing crude and raw mineral oils, such as Lima oil and Canadian oils, which require a different treatment from the ordinary American oils (generally known as Pennsylvania oil),because of their penetrating and disagreeable odor. It is a well-known fact that these kinds of oil are almost unmarketable on account of this disgusting odor and various processes have been invented and patented, having for their object the removal of the disagreeable odor, either from the crude oil prior to or during distillation or from the distillate. As far as I am aware, most of these processes employ metallic oxides in some form or other, because it has been supposed that the disagreeable odor, which characterizes these oils, was due to a chemicalcombination of sulphur with certain constituents in the oil, the nature of which has never been definitely ascertained. I have discovered, however, that this is incorrect, and that the disagreeable odor is not due to'any sulphur combination, but owes its existence to the presence of certain hydrocarbons of a nature Wholly different from that of the hydrocarbon which forms the petroleum proper. Inother words, I have ascertained, beyond doubt, that the disagreeable odor, which it is the object of my invention to remove, is due to the presence in the crude oil of one of agroup of hydrocarbons known technically under the collective name of acetylenes. Based upon this knowledge, I have discovered aprocess for removing the odor from the crude oil, which process is in the nature of'a preliminary treatment of the oil, prior to its distillation proper. What is chiefly aimed at-is to remove the disagreeable odor from the raw product, which can then be placed upon the market and sold to much better advantage than prior to its preliminary to a temperature of about 120 Celsius, which treatment, it being left for the purchaser and refiner to buy the deodorized crude oil and afterward distill the same into its various constituents, as he may see fit; when it will be found that each of the distillates will be entirely free from the disagreeable odor which characterizes this group of oils, the deodorization of which is the object sought to be accomplished.
My invention, therefore, consists in the effectual elimination of the objectionable acetylenes, which results in the purification and deodorization of the oils undergoing treatment by my process.
The principle which underlies my process is to produce an oxidizing action on the acetylenes at a comparatively low temperature, thereby separating them into carbonic acid and water. To effect this, the dissociation of the acetylenes into carbonic acid and water, I employ the second grade of the oxide of copper, or the so-called cuprous oxide (Cu O), which is one of the constituents in copper scale, or what is known in German as kupfer hammerschlag. 'lhesecopper scales are the waste product of copper works, where it accumulates in large quantities so'that it is readily obtainable an a small cost. These copper scales, which, as above stated, are the medium employed for the dissociation of the constituents of the acetylenes, are a mixture of the cupric oxide and cuprous oxide; but in carrying out my process, the cupric oxide remains practically inert, while the cuprous oxide, at a certain degree of temperature, accomplishes the dissociation, and thereby the destruction of the objectionable acetylenes, resulting in simultaneous deodorization. Now to carry out my process on this basis, I add from one-half to two per cent. (by weight) of this copper scale, or ku ofer hammerschlag, to the crude oil, which is gradually heated in a suitable vessel is approximately the boiling point of the oil; care being taken to stir the mixture of oil and copper scale during the process of heating. When a temperature of 120 Celsius has been reached, and the oil commences to boil, but be fore vaporization has set in, it is removed from the fire and allowed to cool, and the copper scale is removed by drawing off the oil, by
straining it, or in any other suitable manner.
It will be found that as a result of this preliminary treatment, the oil has become deodorized, and is ready for barreling and shipping to the distiller or refiner, who will then treat the deodorized oil precisely in the same manner as he treats the American or Pennsylvania oils; my process being essentially a preparatory step intended to bring Lima oils, and oils of that category, on a par with the American or Pennsylvania oils, which, owing to the absence of the unpleasant odor which exists in Lima oil, are fit to go to the still of the refiner without such preliminary treatment.
The copper scale, after it has been removed from the deodorized oil, may be regenerated by roasting to a dark cherry red heat, after which it is cooled off, when it is ready for use over again; and in this manner a great quantity of copper scale may be used over and over again for deodorizing purposes with only a nominal waste.
In order to satisfy myself that my theory regarding the cause of the unpleasant odor in the category of Lima oils is due, not to the existence of sulphurin chemical combination with some peculiar constituent of the oil, but is due to the presence of the acetylenes in the oil, I have tested the oil after it has undergone my preliminary treatment, and have invariably found, as a result of such tests, that the percentage of sulphur in the deodorized oil has not been lowered. In other words, the batch of oil, after undergoing my preliminary process of deodorization, will be found to contain the same percentage of sulphur as the crude oil contained prior to my preliminary treatment;a fact which proves conclusively that the unpleasant odor cannot be due to the presence of sulphur compounds, because if that were so, the test of the deodorized oil would show the entire absence of sulphur, or, at least a greatly reduced percentage thereof. Moreover, if the odor was due to sulphur compounds, the cupric oxide contained in the copper scales would be sufficient to oxidize and neutralize the sulphur, whereas by my improved process, which operates on the acetylenes, the cupric oxide is practically inert, the efiect being wholly due to the chemical action of the cuprous oxide upon the constituent parts, (carbonic acid and water,) of the acetylenes.
That my theory is correct is further proved by a test of the residue in the heating vessel, which shows no trace of sulphur, and also shows that the cupric oxide has not been affected by the process, the protoxide and the acetylenes being the only elements which have undergone change by the said process.
One of the most important results of my process, from a commercial standpoint, is the fact that by my process the oil will become permanently deodorized; that is to say, by the destruction of the acetylenes the odor is permanently removed and cannot possibly return, whereas, in deodorizin g processes which are based upon the destruction of the sulphur compounds, it is well-known that the objectionable odor is liable to return to the oil after a time. This is another proof of the correctness of my theory, because, if the objectionable odor was due, as heretofore erroneously supposed, to the presence of sulphur, the effectual removal of sulphur or its compounds would, of course, result in the effec tual and permanent destruction of the dis agreeable odor, the return of which can only be accounted for on the ground that the acetylenes, to which this odor is really due, have not been destroyed,such old processes being directed toward the destruction of the sulphur compounds in the oil and having no reference. whatever to the destruction of the acetylenes.
In view of the fact that the deodorization by my process is wholly due to the action of the cuprous oxide (Cu O), upon the acetylenes, it Will be obvious that I can use the cuprous oxide alone, and that the oxide of copper is added accidentally, simply because it forms one of the constituent parts of the copper scale, which is the cheapest form in which the cuprous oxide can be obtained at the present time.
It is absolutely necessary to the successful carrying out of my process, that the mixture of oil and copper scale should be heated to (approximately) 120 Celsius in order to produce a reaction of the cuprous oxide. The so-called cold processes which aim at the deodorization of the oil simply by mixing it with certain metallic oxides, Without heating the moisture or by heating the moisture up to the point at which distillation begins, are not applicable to my purpose, because unless the mixture is heated to the boiling point, the reaction of the cuprous oxide will not take place, that is to say, the cuprous oxide will not give ofli' its oxygen, by the combination of which with the acetylenes, the constituent parts of the latter, viz., carbonic acid and hydrogen are dissociated.
Having thus described my invention, I claim and desire to secure by Letters Patent of the United States- 1. The process of deodorizing mineral oils, which consists in mixing the oils with enprous oxide and then subjecting the mixture to heat until the acetylenes contained therein are destroyed, substantially as set forth.
2. The process herein described of deodorizing mineral oils, which consists in dissociating the acetylenes contained in said oils by mixing them with cuprous oxide and heating the mixture to a temperature of the boiling point of the oils, substantially as set forth.
In testimony that I claim the foregoing as my own I have hereunto aflixed my signature in presence of two witnesses.
CLEMENS LOSSEN.
Witnesses:
H. BAUR, Gno. O. GLAVIS.
IIO
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US537121A true US537121A (en) | 1895-04-09 |
Family
ID=2605882
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US537121D Expired - Lifetime US537121A (en) | Deodorizing mineral oils |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US537121A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2768932A (en) * | 1952-10-23 | 1956-10-30 | Exxon Research Engineering Co | Treatment of hydrofined petroleum distillates with copper |
-
0
- US US537121D patent/US537121A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2768932A (en) * | 1952-10-23 | 1956-10-30 | Exxon Research Engineering Co | Treatment of hydrofined petroleum distillates with copper |
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