US254871A - Yapoe feom liquid eydbocaebons - Google Patents
Yapoe feom liquid eydbocaebons Download PDFInfo
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- US254871A US254871A US254871DA US254871A US 254871 A US254871 A US 254871A US 254871D A US254871D A US 254871DA US 254871 A US254871 A US 254871A
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- United States
- Prior art keywords
- steam
- liquid
- pipe
- generating
- yapoe
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- 239000007788 liquid Substances 0.000 title description 18
- 150000002430 hydrocarbons Chemical class 0.000 description 20
- 239000004215 Carbon black (E152) Substances 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 4
- 241000590572 Bia <butterfly> Species 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000875 corresponding Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 230000000630 rising Effects 0.000 description 2
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/384—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts the catalyst being continuously externally heated
Definitions
- My invention relates to that class of vaporgenerators in which steam is used for causing the vaporization of liquid hydrocarbons; and the nature thereof consists in certain improvements in the construction of such generators and novel combinations of the parts thereof,
- Figure 1 is a section taken in a vertical '25 plane through the center of the apparatus.
- Fig. 2 is a top view of the apparatus.
- Fig. 3 illustrates in horizontal section the arrangement of the superheating-pipes.
- the cylindrical chamber H inwhich the 0 vapor is generated, is jacketed by an annular steam-space, B, which communicates by means of the pipeA with the steam-supply, and has arranged within'it an interior steam-space, G, communicating with the steam-jacket, through 5 which steam continuously flows.
- the steam admitted through the pipe A is regulated by the valve A, and flows downward to the bottom of the steam-jacket B, heating in itspassage the exterior of the generating-chamber, 0 from whence it rises through the interior steam-space, O.
- This interior steam-space which I prefer should consist of two' or more communicating receivers of spheroidal form, is connected by means of the pipe D with a sys- 4 5 tom or series of superheating-pipes, F, arranged within the masonry which incloses the apparatus.
- These superheating-pipes are arranged within a receptacle, W, which communicates by means of a perforated wall, S, with the furnace, and are arranged, theone above the other, in such a manner as to form a series of communicating superheaters, the uppermost of which is connected by means of the pipe G, having a valve, G, and pyrometer P, with the interior of the generating-chamber H.
- a furnace 0 from. whence the products of combustion rising expand into the space P around the apparatus through the perforated wall S, and finally pass off through the smokepipe Q.
- the liquid hydrocarbon is introduced into the generatingchamber above the interior steam-space, O, by means of the pipe U, which communicates with source of supply, and the hydrocarbon vapor is carried off by the pipe J, which is provided with a pyrometer, P, and valve K. Any residuum which may remain in the generating-chamber may be drawn 011' through the pipe L, which is provided with a suitable valve, M. o
- the pipe A communicating with the steamjacket B, and the pipe D, which connects the interior steam-space, G, with the superheater, are provided with steamgages W W, by which the pressure may he noted. 5
- the operation of the apparatus is as: follows: The requisite amount of steam is admitted by means of the valve A through the pipe A into the annular steam-jacket on the outside of the generator, from whenceittiowsupwardthrough the interior steam-space and pipe D to the .superheater F, where additional heat is imparted to it by the heated gases from the furnace and the hot brick -work R.
- the steam thus superheated flows through the pipe G to the generating-chamber H, where it comes in contact with the liquid hydrocarbon which enters through the pipe U and flows on the surface of spheroidal receivers.
- the arrangement of the spheroidal receivers is such as to cause 0 the evaporation ofthe hydrocarbon flowing over them, accordingto their volatility-thatis to say,themostvolatilehydrocarbons are evap0- rated first and the least volatile last-and to permit the highly-heated steam to attack the 5 carbonaceous residua and form carbonic-oxide and hydrogen gas.
- the steam should flow from the generator under sufficient pressure to carry the hydrocarbons in vaporous form to the point where they are required, and mix the vapor with an air-blast to insure complete combustion.
- the supeiheating-mrface presented by the steam-jacket B is sufiicient to raise the temperature of free steam to about 500, and the continuous flow ofthe steam into the spheroidal receivers transmits to generating-chamber an amount of heat sufficient to prevent any condensation of the superheated steam admitted for the purpose of vaporization.
- the circulation or continuous flow of steam through the apparatus gradually increases its temperature until it passes from the generating-chambers, and no chilling can occur, except that which must always result from the amount of heat absorbed by the liquid hydrocarbon in passing into a state of vapor.
- the generating-chamber provided with internal spheroidal steam-spaces and external steamjacket, as and for the purposes described.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Description
(No Model.) 2 sneets -sneet 1 H. F. HAYDEN. APPARATUS FOR GENERATING VAPOR FROM LIQUID HYDROGARBONS. No. 254,871. Patented Mar.14,1882.
WITNESSES INVENTbR N. PEIERS, Pholo-Lhhognpher, Walhinglan. 0.6.
(No Model.) 2 Sheets-Sheet 2.
H. P. HAYDEN. APPARATUS FOR GENERATING VAPOR FROM LIQUID HYDROGARBONS.
' INVENTOR WITNESSES ATTORNEYS.
- UNITED STATES,
PATENT OFFICE.
HENRY F. HAYDEN, OF W'A SHINGTONfDISTRlOT" OF COLUMBIA, ASSIGNOR TO THE INTERNATIONAL VAPOR FUEL OARBON IRON AND MANUFAC- TUBING COMPANY, OF SAME PLACE.
APPARATUS FOR GENERATING VAPOR FROM LlQ-UlD HYDROCARBONS.
SPECIFICATION forming part of Letters Patent No. 254,871, dated March 14, 1882.
Application filed June 11, 1881. (No model.)
all whom it may concern:
Be it known that I, HENRY F. HAYDEN, a citizen of theUnited States of America, residing at Washington, in the District of Colum- 5 bia, have invented certain new and useful Improvementsin Apparatus forGeneratingV-apor from Liquid Hydrocarbons; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will to enable others skilled in the art to which it appertains to make and use the same, reference being had to the accompanying drawings, and to letters or figures of reference marked thereon, which form a part of this specification.
1 My invention relates to that class of vaporgenerators in which steam is used for causing the vaporization of liquid hydrocarbons; and the nature thereof consists in certain improvements in the construction of such generators and novel combinations of the parts thereof,
hereinafter described.
In the accompanying drawings, in which corresponding parts are designated by similar letters, Figure 1 is a section taken in a vertical '25 plane through the center of the apparatus.
Fig. 2 is a top view of the apparatus. Fig. 3 illustrates in horizontal section the arrangement of the superheating-pipes.
The cylindrical chamber H, inwhich the 0 vapor is generated, is jacketed by an annular steam-space, B, which communicates by means of the pipeA with the steam-supply, and has arranged within'it an interior steam-space, G, communicating with the steam-jacket, through 5 which steam continuously flows. The steam admitted through the pipe A is regulated by the valve A, and flows downward to the bottom of the steam-jacket B, heating in itspassage the exterior of the generating-chamber, 0 from whence it rises through the interior steam-space, O. This interior steam-space, which I prefer should consist of two' or more communicating receivers of spheroidal form, is connected by means of the pipe D with a sys- 4 5 tom or series of superheating-pipes, F, arranged within the masonry which incloses the apparatus. These superheating-pipes are arranged within a receptacle, W, which communicates by means of a perforated wall, S, with the furnace, and are arranged, theone above the other, in such a manner as to form a series of communicating superheaters, the uppermost of which is connected by means of the pipe G, having a valve, G, and pyrometer P, with the interior of the generating-chamber H. Near the base of the apparatus is a furnace, 0, from. whence the products of combustion rising expand into the space P around the apparatus through the perforated wall S, and finally pass off through the smokepipe Q.
The liquid hydrocarbon is introduced into the generatingchamber above the interior steam-space, O, by means of the pipe U, which communicates with source of supply, and the hydrocarbon vapor is carried off by the pipe J, which is provided with a pyrometer, P, and valve K. Any residuum which may remain in the generating-chamber may be drawn 011' through the pipe L, which is provided with a suitable valve, M. o
The pipe A, communicating with the steamjacket B, and the pipe D, which connects the interior steam-space, G, with the superheater, are provided with steamgages W W, by which the pressure may he noted. 5
The operation of the apparatus is as: follows: The requisite amount of steam is admitted by means of the valve A through the pipe A into the annular steam-jacket on the outside of the generator, from whenceittiowsupwardthrough the interior steam-space and pipe D to the .superheater F, where additional heat is imparted to it by the heated gases from the furnace and the hot brick -work R. The steam thus superheated flows through the pipe G to the generating-chamber H, where it comes in contact with the liquid hydrocarbon which enters through the pipe U and flows on the surface of spheroidal receivers. The arrangement of the spheroidal receivers is such as to cause 0 the evaporation ofthe hydrocarbon flowing over them, accordingto their volatility-thatis to say,themostvolatilehydrocarbons are evap0- rated first and the least volatile last-and to permit the highly-heated steam to attack the 5 carbonaceous residua and form carbonic-oxide and hydrogen gas. The steam should flow from the generator under sufficient pressure to carry the hydrocarbons in vaporous form to the point where they are required, and mix the vapor with an air-blast to insure complete combustion.
The supeiheating-mrface presented by the steam-jacket B is sufiicient to raise the temperature of free steam to about 500, and the continuous flow ofthe steam into the spheroidal receivers transmits to generating-chamber an amount of heat sufficient to prevent any condensation of the superheated steam admitted for the purpose of vaporization.
The circulation or continuous flow of steam through the apparatus, as above described, gradually increases its temperature until it passes from the generating-chambers, and no chilling can occur, except that which must always result from the amount of heat absorbed by the liquid hydrocarbon in passing into a state of vapor.
Having thus described my invention, I claim and desire to secure by Letters Patent- 1. In the apparatus for generating vapor from liquid hydrocarbons, herein described, the
generating-chamber having an in ternal'steamspace consisting of two or more communicating spheroidal receivers, as and for the purposes described.
2. In the apparatus for generating vapor from liquid hydrocarbon, herein described, the generating-chamber provided with internal spheroidal steam-spaces and external steamjacket, as and for the purposes described.
3. The combination of the spheroidal rcceivers, the pipe through which the superheated steam enters the generating-chamber, and the oil-supply pipe.
4-. Thecombinationoftheoutersteam-jacket, B, spheroidal receivers 0, connecting pipe D, superheater F, and generatingchamber H, as and for the purposes described.
In testimony whereof I affix my signature in presence of two witnesses.
HENRY F. HAYDEN.
Witnesses! O. S. WHITMAN, F. M. BURNHAM.
Publications (1)
Publication Number | Publication Date |
---|---|
US254871A true US254871A (en) | 1882-03-14 |
Family
ID=2324166
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US254871D Expired - Lifetime US254871A (en) | Yapoe feom liquid eydbocaebons |
Country Status (1)
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2503883A (en) * | 1946-07-24 | 1950-04-11 | William J Miller | Fluid heater |
-
0
- US US254871D patent/US254871A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2503883A (en) * | 1946-07-24 | 1950-04-11 | William J Miller | Fluid heater |
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