US426173A - James dewar - Google Patents
James dewar Download PDFInfo
- Publication number
- US426173A US426173A US426173DA US426173A US 426173 A US426173 A US 426173A US 426173D A US426173D A US 426173DA US 426173 A US426173 A US 426173A
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- US
- United States
- Prior art keywords
- retort
- oil
- pipe
- still
- head
- 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.)
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- 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
- C10G7/00—Distillation of hydrocarbon oils
Definitions
- JAMES DEVAR OF CAMBRIDGE, COUNTY OF CAM BRIDGE, AND BOVERTON REDlVOOD, OF FINCIILEY, COUNTY OF MIDDLESEX, ENGLAND.
- Our invention relates to suitable apparatus for a method of conducting the distillation in such a manner that we get the benefit of regular vaporization and condensation under high pressure, and that we may at the same time get such advantage as can be otained from cracking, which method is the subject of a patent application of even date herewith,
- a suitable boiler or retort and a condenser in free communication with one another without int-erposing any valve between them; but we provide a regulated outlet for condensed liquid from the condenser.
- ⁇ Ve charge and keep charged the space in the boiler or retort and condenser that is not occupied by liquid with gas under considerable pressure-it may be with air, or it may be with carbonic-acid gas or other gas that cannot act chemically on the matter treated.
- the distillation and condensation being thus conducted under considerable pressure, which can be regulated at will, we obtain from the heavy residue a quantity of more or less light oil, suitable for illuminating and other purposes-such as heating or lubrication--which cannot be obtained by distillation under atmospheric pressure.
- lVe may also arrange the still-head or upper part of the boiler or retort so as to operate accordin g to the cracking method above referred to, the cracking in this case taking place under high pressure instead of being carried on under atmospheric pressure.
- the apparatus for effecting distillation in the manner described may be arranged in various ways.
- Figure 1 is a longitudinal, and Fig. 2 is a transverse, section.
- Fig. 3 is a sectional plan on the line X X. of Fig. 1.
- A is a fire-place, with fire-door A and ashpit door A suited for regulating admission of air as required.
- any known burners for liquid or gaseous fuel may be employed.
- a metal retort C which is inclosed within a refractory casing C to protect the metal from excessive local heating.
- the incased retort is situated in a heating-chamber B, into which the hot products of combustion ascend by side ports 13*, and from which they pass by central ports 13 into a fiue B communicating with a ated in a tank D, in which circulation of water is maintained.
- the upper end of the coil D communicates by a pipe with the stillhead C and its lower end opens into a hollow column D which is provided with a glass gage D and has at the bottom an outlet-pipe D, furnished with a stop cook or valve.
- E is a pump for forcing the oil to be treated by a pipe E into the retort 0, this pipe preferably extending nearly to the farther end of the retort.
- F is an aircompressing pump, by which air or suitable gas is forced by a pipe F into the still-head C, or it might be into any other part of the apparatus which is in communication with the still-head.
- the retort G being partly charged with oil by the pump E, and the spaces in the retort G in the still-head O and in the condensing-coil D and column D being charged with air or gas to the desired pressure, the retort is heated, vaporizing the oil under pressure.
- the oil-vapor is condensed in passing through the coil D, and the liquid distillate collects in the column D and is drawn off, either continuously or intermittently, into suitable receptacles, in which such gas as may be dissolved in the liquid is liberated and can be collected.
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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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
(No Model.)
J. DEWAR & B. REDWOOD. APPARATUS FOR THE DISTILLATION OP MINERAL OILS AND LIKE PRODUCTS.
0 9 1 8 1 Z 2 TI. L p A d n 6 t N am P l\. 1W I I Nirn STATES PATENT OFFIcE.
JAMES DEVAR, OF CAMBRIDGE, COUNTY OF CAM BRIDGE, AND BOVERTON REDlVOOD, OF FINCIILEY, COUNTY OF MIDDLESEX, ENGLAND.
APPARATUS FOR THE DISTILLATION OF MINERAL OILS AND LIKE PRODUCTS.
SPECIFICATION forming part of Letters Patent No. 426,173, dated April 22, 1890.
Application filed September 3, 1889. Serial No. 822,857. (No model.) Patented in England June 24:, 1889, No. 10,277; in France August 30, 1889, 110,200,495 in Belgium August 80, 1889, No. 87,570; in Switzerland August 30, 1889, No. 1,339; in Italy October 1, 1889, L1, 238, and in Austria-Hungary December 27, 1889, No. 37,712 and No, 63,270.
To all whom it may concern.-
Be it known that we, JAMES DEWAR, professor of chemistry, and BovERroNREnwooD, analytical chemist, citizens of Eugland,residing, respectively, atNo. 1 Scroop Terrace, Cambridge, in the countyof Cambridge, England, and at Ballards Lane, Finchley,in the county of Hiddlesex, England, have invented new and useful Apparatus for the Distillation of Mineral Oils and like Products, (for which we have obtained Letters Patent in France, dated August 80, 1889, No. 200,+i95; in Belgium, dated August 80, 1889, No. 87,570; in Switzerland, dated August 80, 1889, No. 1,339; in Italy, dated October 1, 1889, Vol. LI, 233; in Austria-llungary, dated December 27, 1889, No. 37,712 and No. (53,270, and in Great Britain by an application for patent, which patout when granted will bear date June 24, 1889, N 10,277,) of which the following is a specification.
In distillin mineral. oils-such as natural petroleum or similar oil made from shale coal or other bituminous substances-in order to separate the lighter cils, suitable for lamps and other purposes, from the heavier oils there is frequently a very large residue of heavy oil. Attempts have been made to obtain lighter oils from such residues or from heavy natural. petroleums by causing the vapor generated in the still-boiler to pass a heavilydoaded valve, so that the vaporization takes place under considerable pressure. It has also been proposed to arrange the stillboiler with its upper part cooled, so that the less volatile portions of the vapor may become more or less condensed and fall back into the hot liquid below, this modeof operating being commonly termed cracking. Both these methods are objectionable, the former on account of the irregularity of the distillation and the latter on account of the waste of heat in conducting the cracking process and the slowness and insufficiency of the results.
Our invention relates to suitable apparatus for a method of conducting the distillation in such a manner that we get the benefit of regular vaporization and condensation under high pressure, and that we may at the same time get such advantage as can be otained from cracking, which method is the subject of a patent application of even date herewith, For this purpose we arrange a suitable boiler or retort and a condenser in free communication with one another without int-erposing any valve between them; but we provide a regulated outlet for condensed liquid from the condenser. \Ve charge and keep charged the space in the boiler or retort and condenser that is not occupied by liquid with gas under considerable pressure-it may be with air, or it may be with carbonic-acid gas or other gas that cannot act chemically on the matter treated. The distillation and condensation being thus conducted under considerable pressure, which can be regulated at will, we obtain from the heavy residue a quantity of more or less light oil, suitable for illuminating and other purposes-such as heating or lubrication--which cannot be obtained by distillation under atmospheric pressure. lVe may also arrange the still-head or upper part of the boiler or retort so as to operate accordin g to the cracking method above referred to, the cracking in this case taking place under high pressure instead of being carried on under atmospheric pressure.
The apparatus for effecting distillation in the manner described may be arranged in various ways.
The accompanying drawings show one form of apparatus for this purpose.
Figure 1 is a longitudinal, and Fig. 2 is a transverse, section. Fig. 3 is a sectional plan on the line X X. of Fig. 1.
A is a fire-place, with fire-door A and ashpit door A suited for regulating admission of air as required.
Instead of a fire-place with grate for burning solid fuel, any known burners for liquid or gaseous fuel may be employed.
Above the combustion-chamber B is placed a metal retort C, which is inclosed within a refractory casing C to protect the metal from excessive local heating. The incased retort is situated in a heating-chamber B, into which the hot products of combustion ascend by side ports 13*, and from which they pass by central ports 13 into a fiue B communicating with a ated in a tank D, in which circulation of water is maintained. The upper end of the coil D communicates by a pipe with the stillhead C and its lower end opens into a hollow column D which is provided with a glass gage D and has at the bottom an outlet-pipe D, furnished with a stop cook or valve. E is a pump for forcing the oil to be treated by a pipe E into the retort 0, this pipe preferably extending nearly to the farther end of the retort. By another pipe E furnished with a cook or valve, the contents of the retort can be drawn oif, or this pipe may communicate with a second retort, which in like manner may beconnected with a third, so as to form a series of any required number. F is an aircompressing pump, by which air or suitable gas is forced by a pipe F into the still-head C, or it might be into any other part of the apparatus which is in communication with the still-head. The retort G being partly charged with oil by the pump E, and the spaces in the retort G in the still-head O and in the condensing-coil D and column D being charged with air or gas to the desired pressure, the retort is heated, vaporizing the oil under pressure. The oil-vapor is condensed in passing through the coil D, and the liquid distillate collects in the column D and is drawn off, either continuously or intermittently, into suitable receptacles, in which such gas as may be dissolved in the liquid is liberated and can be collected.
By a pipe and cook or a suitably-loaded safety valve D gas may be withdrawn from the space above the liquid in the column D Although we have shown one retort and condenser, there may be several sets of these in communication with the oil and gas pumps or with each other, suitable cocks or valves being provided in the communicating pipes, so that the several retorts may be worked simultaneously or in rotation. From time to time the cover C of the retort may be removed to clear out residue. During the dis tillation such of the Vapor as may becondensed in the still-head C or such liquid as may prime up into the still-head flows back into the body of liquid in the retort. By regulating the heat and pressure to which the retort is subjected the character of the distillate may be varied, and thus oils more or less light can be obtained to suit various uses;
also, the proportions of the parts may be varied, and, if necessary, means of cooling may be applied to the still-head C Having thus described the nature of our invention and the manner of carrying the same into effect, we claim-- f In an apparatus for distilling oil, the combination of the retort C, the still-head O in free communication with the retort, the con- 7o denser D, in free communication with the still-head and provided with a regulated outlet, the oil-pump E, having a pipe E, leading into the retort and extending nearly its full length, and the air-compressin g pump F, hav- 7 5 ing a pipe F, communicating with the stillhead, substantially as described.
In testimony whereof we have signed our names to this specification, in the presence of two subscribing witnesses, this 13th day of August, A. D. 1889.
JAMES DEXVAR. BOVERTON RED\VOOD. lVitnesses: OLIVER IMRAY, Patent Agent, 28 Southampton Buildings, London, W. O.
J NO. P. M. MiLLARD, Clerk to lllessrs. Abe-l d2 Ionmg, Consulting Engineers and Patent Agents, 28 Southampton Buildings, London, VV. 0.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US426173A true US426173A (en) | 1890-04-22 |
Family
ID=2495083
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US426173D Expired - Lifetime US426173A (en) | James dewar |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US426173A (en) |
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- US US426173D patent/US426173A/en not_active Expired - Lifetime
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