US11205A - Improvement in kerosene burning-fluids - Google Patents
Improvement in kerosene burning-fluids Download PDFInfo
- Publication number
- US11205A US11205A US11205DA US11205A US 11205 A US11205 A US 11205A US 11205D A US11205D A US 11205DA US 11205 A US11205 A US 11205A
- Authority
- US
- United States
- Prior art keywords
- liquid
- kerosene
- fluids
- improvement
- fahrenheit
- 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
- 239000003350 kerosene Substances 0.000 title description 38
- 239000012530 fluid Substances 0.000 title description 14
- 239000007788 liquid Substances 0.000 description 52
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 14
- 235000015450 Tilia cordata Nutrition 0.000 description 14
- 235000011941 Tilia x europaea Nutrition 0.000 description 14
- 239000004571 lime Substances 0.000 description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 238000000034 method Methods 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 239000000047 product Substances 0.000 description 12
- 230000005484 gravity Effects 0.000 description 10
- 230000000694 effects Effects 0.000 description 8
- 239000012535 impurity Substances 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000002253 acid Substances 0.000 description 6
- 239000010426 asphalt Substances 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 238000001704 evaporation Methods 0.000 description 6
- 238000000197 pyrolysis Methods 0.000 description 6
- 240000002027 Ficus elastica Species 0.000 description 4
- 239000003513 alkali Substances 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 238000005286 illumination Methods 0.000 description 4
- 239000012263 liquid product Substances 0.000 description 4
- 229920001195 polyisoprene Polymers 0.000 description 4
- 230000001105 regulatory Effects 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 229910001018 Cast iron Inorganic materials 0.000 description 2
- 241000272184 Falconiformes Species 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 235000011167 hydrochloric acid Nutrition 0.000 description 2
- 230000000266 injurious Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 230000004301 light adaptation Effects 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 2
- 229910052748 manganese Inorganic materials 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 235000014593 oils and fats Nutrition 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 229940072033 potash Drugs 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 235000015320 potassium carbonate Nutrition 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
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
- C10G17/02—Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge with acids or acid-containing liquids, e.g. acid sludge
- C10G17/04—Liquid-liquid treatment forming two immiscible phases
- C10G17/06—Liquid-liquid treatment forming two immiscible phases using acids derived from sulfur or acid sludge thereof
Definitions
- the second or medium-proof fluid Icall B kerosene, and suppose it to be composed of four parts or equivalentsot the heavy and six of the light fluid. Its specific gravity is pipes, and burning @no and its boiling-point 250 Fahrenheit. It is not a solvent of gums, but will soften them very slightly. Seventy-five parts of alcohol ot' specific gravity .844, ata temperature of 00 Fahrenheit, will dissolve twenty. five parts of this liquid. By itself the B kerosene is moderately "olatile and inflammable, but will not, likethe A,'" yield a good light by having a current of air passed through it and burned.
- the third or low-proof fluidlcall' U kerosene and suppose it to be composed of silt parts or equivalentsof the heavy and four of the light liquid. Unlike the A and B, the heavy liquid preponderates in and gives character to the O kerosene. Its specific gravity is .800 and its boiling-point is 3509 Fahrenheit. Unlike A and B, it is not soluble in alcohol, but it is a good solventof gums, as india-rubber dissolves in it readily.
- the first part of the'process consists in submitting the raw material to dry distillation at the lowest temperature at which the kerosene will volatilize, care being taken not to raise the temperature so long as tolerably-rapid evaporation continues, and the heat must not in any case be raised above 800 Fahrenheit, as the heat, if raised to the slightest perceptible red in daylight, would be so high as to defeat the whole object of the process, for a greatly-increased production of gas would take place and the liquid product would be-naptha instead of kerosene. Whatever gas may be generated I employ for illuminating purposes in the ordinary manner, and also as fuel for heating the still.
- the light liquid is then submitted to rcdistillation at the lowest possible heat in a common still and condenser.
- the product of this redistillation is a light volatile liquid, which accumulates in the receiver, and aheavy tarry residuum left in the still, and which may be added to the heavy liquid impurities of the first distillate.”
- the light liquid is transferred from the receiver to a suitable vessel or vat, and mixed thoroughly with from five to ten percent. of strong sulphuric, nitric, or muriatic acid, accordingtothequantit-yof tarpresent. Seven per cent. is about the average quantity required; but any quantity is useful.
- natant liquid is now separated from the impurities, both solid and liquid, that have settled to the bottom of the tank, by drawing oft either the one or the other into a separate vessel.
- the latter by its powerful affinity for water will absorb it thoroughly from the liquid hydrocarbon, which always at this stage of the process contains water in a greater or less quantity. Lime by its alkaline properties will also neutralize any acid in the liquid.
- the quantity of lime I have mentioned is the quantity I have found sufficient in all cases; but any quantity less than tenper cent. would be useful.
- the lime as an alkali appears to exert a specific influence or effect which is indispensable to the good quality of the product. Neither soda nor potash can produce this effect in any form in whichI have tried them, and I have made numerous and special efforts to replace the lime with these alkalies.
- thermometer is not used for the purpose of regulating the temperature, as the observatheliquidhydrocarbon herein described,which tion and judgment of a skillful workman are I I denominate B kerosene.
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- PATE T OFFICE.
ABRAHAM GESNER, OF VVILLIAMSBIIBG, NEW YORK, ASSIGNOR TO THE ASPHALT MINING AND KEROSENE GAS COMPANY.
IMPROVEMENT IN KEROSENEBURNING-FLUIDS.
Specification forming part of Letters Patent No. 1|,205, dated June .27, 1854.
T 0 all whom it may concern:
Be it known that I, ABRAHAM GESNER, late of the city and county of New York, now of I Williamsburg, in the county of Kings and State of New York, have invented or discovered a new and useful manufacture or composition of matter, being a new liquid hyd roearbon, which I denominate Kerosene, and which may be. used for illuminating and other purposes, of which the following is a specification.
I obtain this productfrom petroleum, maltha, or soft mineral pitch, asphaltum, or bitumen, wherever found, by dry distillation and subsequent treatment with powerful reagents and redistillation.
This process, which will presently be described, yields kerosene of three different qualities or proofs, each of which, in my opinion, is a mixture in certain proportions of a spirituous',1ight, and highly volatile and intlam niable liquid, with an oily, heavy, and less volatile and inflammable liquid. 1 have not succeeded in completely separating these liquids in the manufacture, and I see no practically-useful object tobegained by doing so. Neither have I ascertained the exact proportions in which the two liquids are mixed; but I suppose the lightest fluid, which I denominate A kerosene, tobe composed of two parts, by measure or equivalent proportions, of the heavy and eight parts of the light fluid. Its specific gravity is .750, water being 1, and it boils at 150 Fahrenheit. It is not a solvent of such gums as I have tried to dissolve in it, among which Iinay mention india-rubber. Sixty-five parts, by measure, ofalcohol ofspeciflc gravity .844, at a temperature of 60 Fahrenheit, will dissolve thirty-five parts, by measure, of this liquid. By itself the A kerosone is highly volatile and inflammable, so much so that even in cold. winter weather a good light is produced.
by forcing a current of atmospheric air through it, circulating the same in it in jets like gas.
The second or medium-proof fluid Icall B kerosene, and suppose it to be composed of four parts or equivalentsot the heavy and six of the light fluid. Its specific gravity is pipes, and burning @no and its boiling-point 250 Fahrenheit. It is not a solvent of gums, but will soften them very slightly. Seventy-five parts of alcohol ot' specific gravity .844, ata temperature of 00 Fahrenheit, will dissolve twenty. five parts of this liquid. By itself the B kerosene is moderately "olatile and inflammable, but will not, likethe A,'" yield a good light by having a current of air passed through it and burned.
The third or low-proof fluidlcall' U kerosene, and suppose it to be composed of silt parts or equivalentsof the heavy and four of the light liquid. Unlike the A and B, the heavy liquid preponderates in and gives character to the O kerosene. Its specific gravity is .800 and its boiling-point is 3509 Fahrenheit. Unlike A and B, it is not soluble in alcohol, but it is a good solventof gums, as india-rubber dissolves in it readily.
It is not very volatile or inflammable; but in an Argand lamp, wit-ha button over the wick, it burns with a brilliant white light without smoke or the napthalous odor so offensive in many hydrocarbons having some resemblance to this, but possessing very different properties. As burning-fluids for the purposeot artificial illumination these are highly useful and economical, either separately, mixed together, or A and B mixed with alcohol. The O kerosene has also proved very good as a lubricant for machinery where it has been tried; but, being a new thing, the kerosene doubtless has very numerous uses besides its adaptation to illumination and lubrication that will soon bediscovered after it is manufactured on the large scale and put into market as an article of trade. Moreover, as the rocks whence the kerosene is most abundantly obtained are widely disseminated, and the deposits of them are of almost unlimited extent, an immense mass of hitherto useless matter will by meaghs of this invention be rendered available for the uses of mankind as a cheap and convenient substitute for illuminating purposes for the oils and fats which are yearly increasing in scarcity and value.
Theprocess and apparatus Iem ploy in prod uc ing the kerosene I will now proceed to describe, premising that I do not confine myself to any particular form or arrangement of apparatus,
but intend to use whatever may prove most convenient in any given case.
The first part of the'process consists in submitting the raw material to dry distillation at the lowest temperature at which the kerosene will volatilize, care being taken not to raise the temperature so long as tolerably-rapid evaporation continues, and the heat must not in any case be raised above 800 Fahrenheit, as the heat, if raised to the slightest perceptible red in daylight, would be so high as to defeat the whole object of the process, for a greatly-increased production of gas would take place and the liquid product would be-naptha instead of kerosene. Whatever gas may be generated I employ for illuminating purposes in the ordinary manner, and also as fuel for heating the still. For this dry distillation I have used large cast-iron retorts, set in suitable furnaces for the evaporation and metal pipes or chambers surrounded by water for the condensation of the vapor. The liquid products of this-distillation are heavy tar and water or ammoniacal liquor, which lie-at the bottom of the receiver, and alighter liquid, which floats above them. The heavyliquids and the light are separated by drawing 01f one or the other into another vessel by means of a cock, siphon, or otherwise. The heavy liquids may be utili zed or disposed of advantageously; but they have no further connection with this process,
andtherefore I shall not here describe the modem which I propose to utilize them. The light liquid is then submitted to rcdistillation at the lowest possible heat in a common still and condenser. The product of this redistillation is a light volatile liquid, which accumulates in the receiver, and aheavy tarry residuum left in the still, and which may be added to the heavy liquid impurities of the first distillate." The light liquid is transferred from the receiver to a suitable vessel or vat, and mixed thoroughly with from five to ten percent. of strong sulphuric, nitric, or muriatic acid, accordingtothequantit-yof tarpresent. Seven per cent. is about the average quantity required; but any quantity is useful. I have enumerated three acids; but I give the preference to sulphuric, although either of the others'will answer very well. I also mix with the liquid from one to three per cent. of peroxide of manganese, according to the turbidness of the liquid, about two per cent. being the average quantity required. It has the effect of facilitating greatly the precipitation of certain of the impurities which the liquid contains; but although useful 'I do not deem it essential. After these substances have been thoroughly mixed with' the liquid by agitation it is al-' lowed to stand from twelve ,to twcnty four' hdurswithout being disturbed, in order that The clear super-' the impurities may subside. natant liquid is now separated from the impurities, both solid and liquid, that have settled to the bottom of the tank, by drawing oft either the one or the other into a separate vessel. I next mix the distillate with about two per cent., by weight, of powdered and freshly-calcined lime. The latter by its powerful affinity for water will absorb it thoroughly from the liquid hydrocarbon, which always at this stage of the process contains water in a greater or less quantity. Lime by its alkaline properties will also neutralize any acid in the liquid. After the lime has been thoroughly mixed with the liquid by stirring, the mixture is again distilled, care being taken to raise the heat gradually and slowly to about 160 Fahrenheit, where it is kept by regulating the damper until all the vaporhas passed over the receiver that the liquid will yield at this temperature. This product or distillate is the A kerosene, and is drawn off from the receiver into an appropriate vessel. The heat is now raised by again drawing the damper to about 260 Fahrenheit, when vapors will again rise and be condensed'in the receiver. As soon as the distillate'ceases to flow at this temperature it is drawn off from the receiver into a separate vessel, and itconstitntes, the B kerosene. The heat of the still is now raised to about 360 Fahrenheit, when vapors will again rise and condense in the receiver. As soon as the distillate ceases to run at this temperature the processis cor'rr' pleteL This last product is the O 'kerosene.
The quantity of lime I have mentioned is the quantity I have found sufficient in all cases; but any quantity less than tenper cent. would be useful. The lime as an alkali appears to exert a specific influence or effect which is indispensable to the good quality of the product. Neither soda nor potash can produce this effect in any form in whichI have tried them, and I have made numerous and special efforts to replace the lime with these alkalies.
To deprive the liquid of water by freshlycalcined lime is important, because, as I have discovered, water is highly injurious to the process and product, even in very small quantities, as it causes carholic acid to pass over siblc effect upon the quality or character of the product, as no evaporation takes place-at a temperature below that at which the-first distillation'begins, or between the first and second, or second and third distillations, and
a thermometer is not used for the purpose of regulating the temperature, as the observatheliquidhydrocarbon herein described,which tion and judgment of a skillful workman are I I denominate B kerosene.
sufficient. 4 In testimony whereof I have hereunto sub- Having claimed under separate specificascribed myname. V tions the A and O kerosenesg in this I ABRAHAM GESNER. c1aim Witnesses:
As a new manufacture or composition of F. G. DE FONTAINE, matter for illuminating and other purposes, HORATIO EAGLE.
Publications (1)
Publication Number | Publication Date |
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US11205A true US11205A (en) | 1854-06-27 |
Family
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Family Applications (1)
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US11205D Expired - Lifetime US11205A (en) | Improvement in kerosene burning-fluids |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060011136A1 (en) * | 2004-07-15 | 2006-01-19 | Semiconductor Energy Laboratory Co., Ltd. | Manufacturing apparatus |
-
0
- US US11205D patent/US11205A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060011136A1 (en) * | 2004-07-15 | 2006-01-19 | Semiconductor Energy Laboratory Co., Ltd. | Manufacturing apparatus |
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