US152006A - Improvement in apparatus for carbureting gas and air - Google Patents
Improvement in apparatus for carbureting gas and air Download PDFInfo
- Publication number
- US152006A US152006A US152006DA US152006A US 152006 A US152006 A US 152006A US 152006D A US152006D A US 152006DA US 152006 A US152006 A US 152006A
- Authority
- US
- United States
- Prior art keywords
- gas
- carbureter
- carburetor
- hydrocarbon
- air
- Prior art date
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- Expired - Lifetime
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- 239000007789 gas Substances 0.000 description 36
- 239000004215 Carbon black (E152) Substances 0.000 description 34
- 150000002430 hydrocarbons Chemical class 0.000 description 34
- 239000007788 liquid Substances 0.000 description 24
- 239000012530 fluid Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 12
- 210000001736 Capillaries Anatomy 0.000 description 8
- 150000001875 compounds Chemical class 0.000 description 6
- 238000010276 construction Methods 0.000 description 4
- 239000002657 fibrous material Substances 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 240000005337 Agave sisalana Species 0.000 description 2
- 235000011624 Agave sisalana Nutrition 0.000 description 2
- 241000331231 Amorphocerini gen. n. 1 DAD-2008 Species 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000001771 impaired Effects 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 235000020004 porter Nutrition 0.000 description 2
- 230000000717 retained Effects 0.000 description 2
Images
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
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/10—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/008—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction
- B01J8/0085—Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction promoting uninterrupted fluid flow, e.g. by filtering out particles in front of the catalyst layer
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Definitions
- My invention relates to certain improvements in apparatus for car-bursting gas, air, 650., by means of which I am enabled to keep up the operation of the apparatus until the last drop of hydrocarbon fluid is exhausted without any perceptible change in the quality or brilliancy of the light, and to present an extended surface of the hydrocarbon fluid to the action of the gas so long as any of said hydrocarbon remains in the carburetor; and, also, to more completely and uniformly carburet the gas than has ever been hitherto done, by meansof a new packing or filling for the carbureter, all of which will be fully hereinafter described.
- My invention is designed to overcome these defects, and to make the hydrocarbon liquid go as far as possible.
- My invention consists, first, in constructing the bottom of the carbureter, as hereinafter described, so that the hydrocarbon liquid, as it is evaporated, will be retained at the periphery or sides of the same, the last portion of the said liquid remaining at this point, and in introducing the gas at the bottom and close to the periphery or sides all around the carburetor, so that it will be forced to pass through a quantity of the liquid as long as any remains in the carbureter; second, in a new and im proved packing, consisting of a series of perforated plates, arranged at not more than four inches apart, one above the other, within the carburetor, the spaces between said plates being filled with fibrous or capillary material, the whole combined to operate substantially as hereinafter described; third, in the combination with a carbureter, as described, of a condensing-chamber, constructed and applied as hereinafter set forth; and, fourth, in the combination of the various devices forming my carburetor with each other, and with a hydrogen-
- the drawing represents a vertical section of my carburetor.
- A represents the generator, in which the hydrogen gas is produced in the ordinary manner from dilute acid and metal filings and turnings.
- B represents a pipe leading from the same through the carburetor, and O represents the carbureter.
- Said carburetor is constructed with a concavo-convex bottom, 0,
- a concavo-convex plate, D with convex side up, as shown, said plate extending nearly to the edge or periphery of the bottom 0, and the plate is so suspended or hung in the carburetor as to leave a small space, F, between its periphery and the periphery of the bottom all round.
- the pipe B is stopped or partitioned at 0. From below this partition extends a pipe, G, down through the concavoconvex plate D, where it terminates, as shown.
- This pipe serves to conduct the gas under the said plate D from the pipe 13.
- 1TH represent a series of two or more perforated metal plates arranged at a distance of not more than four inches apart within the carburetor and supported in any convenient manner.
- K represents a condensing-chamber secured to the upper end of the tube B.
- the said tube is provided with an aperture, I1, opening into the carbu reter, as shown, through which the carbureted gas passes to the condenser.
- the service-pipe M extends from the top of the condenser to the various burners.
- the operation of my apparatus is as follows: The carbureter having been charged with any desired quantity of hydrocarbon fluid, and the generator having been properly charged and made ready for use, on opening the burners the gas will begin to be generated, and will pass up through the pipe 13, and then down pipe 0 and under the plate 1), and out through the aperture or space E into the carburetingchamber. It will then pass up through the compound packing, becoming thoroughly carbureted, after which it will pass to the condenser.
- the condenser being packed, as usual, with fibrous material, condenses and returns any superfluous hydrocarbon vapor in the gas.
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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)
- Physics & Mathematics (AREA)
- Fluid Mechanics (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
A. W. PORTER.
Apparatus for Carbureting Gas and Air.
N(),152,006, P atentedlunel6,l874.
UNITED STATES PATENT Orrrcn.
ALONZO Y. PORTER, OF NEW YORK, N. Y.
IMPROVEMENT IN APPARATUS FOR CARBURETING GAS AND A!R.
, Specification formirg part of Letters Patent No. 152.006, dati d June 16, 1874: application filed June 8, 1874.
To all whom it may concern:
Be it known that I, ALoNzo XV. PORTER, of New York city, in the county and State of New York, have invented certain new and useful Improvements in Apparatus for Carbureting Gas, Air, &c., of which the following is a specification:
My invention relates to certain improvements in apparatus for car-bursting gas, air, 650., by means of which I am enabled to keep up the operation of the apparatus until the last drop of hydrocarbon fluid is exhausted without any perceptible change in the quality or brilliancy of the light, and to present an extended surface of the hydrocarbon fluid to the action of the gas so long as any of said hydrocarbon remains in the carburetor; and, also, to more completely and uniformly carburet the gas than has ever been hitherto done, by meansof a new packing or filling for the carbureter, all of which will be fully hereinafter described.
In all apparatus of this class, as hitherto constructed, the hydrocarbon liquid becomes reduced in quantity and gravity at the same time, and when nearly exhausted fails to carburet the gas properly. The liquid being reduced in gravity, and becoming heavier toward the end of the operation of the machine, as stated, it cannot be taken up with the same facility by the gas as when first put in; and, owing to the faulty construction of previous machines, the air can only be made to pass over the full extent of carbureting surface when such machines are first charged, and while filled with the hydrocarbon liquid. Therefore, after such machines have been in operation for awhile, and the charge of hydrocarbon fluid has been partially worked ofl, the brilliancy of the light is impaired, and toward the latter part of the operation of the carbureter, before more than two-thirds of the hydrocarbon fluid has been worked off, such apparatus, in most cases, cease to operate, and the hydrocarbon remaining in the carbureter has to be thrown aside, and the apparatus recharged. In carburetors as heretofore constructed, it has been found impossible to carburet the gas uniformly throughout the entire operation, owing to the fact that no capillary material is known that will conduct or draw the liquid to aheight of more than four inches consequently the carburetin g is less and less effectively done toward the end of the operation.
My invention is designed to overcome these defects, and to make the hydrocarbon liquid go as far as possible. This being the cheapest ingredient in the compound gas formed by this class of machines, the great object is to have the h ydrocarbon in as large a propor tion as possible; or, in other words, to have the gas saturated with the hydrocarbon throughout the entire operation of the apparatus. This I have succeeded in accomplishing, as will be evident from the following description of the construction and operation of my apparatus.
My invention consists, first, in constructing the bottom of the carbureter, as hereinafter described, so that the hydrocarbon liquid, as it is evaporated, will be retained at the periphery or sides of the same, the last portion of the said liquid remaining at this point, and in introducing the gas at the bottom and close to the periphery or sides all around the carburetor, so that it will be forced to pass through a quantity of the liquid as long as any remains in the carbureter; second, in a new and im proved packing, consisting of a series of perforated plates, arranged at not more than four inches apart, one above the other, within the carburetor, the spaces between said plates being filled with fibrous or capillary material, the whole combined to operate substantially as hereinafter described; third, in the combination with a carbureter, as described, of a condensing-chamber, constructed and applied as hereinafter set forth; and, fourth, in the combination of the various devices forming my carburetor with each other, and with a hydrogen-gas generator, as will be hereinafter specified.
The drawing represents a vertical section of my carburetor.
A represents the generator, in which the hydrogen gas is produced in the ordinary manner from dilute acid and metal filings and turnings. B represents a pipe leading from the same through the carburetor, and O represents the carbureter. Said carburetor is constructed with a concavo-convex bottom, 0,
. the convex side upward, as shown.
Above the bottom is a concavo-convex plate, D, with convex side up, as shown, said plate extending nearly to the edge or periphery of the bottom 0, and the plate is so suspended or hung in the carburetor as to leave a small space, F, between its periphery and the periphery of the bottom all round. The pipe B is stopped or partitioned at 0. From below this partition extends a pipe, G, down through the concavoconvex plate D, where it terminates, as shown. This pipe serves to conduct the gas under the said plate D from the pipe 13. 1TH represent a series of two or more perforated metal plates arranged at a distance of not more than four inches apart within the carburetor and supported in any convenient manner. The spaces between these plates I fill with sisal hemp, excelsior, or other capillary material. The plates act as relays or stations for the hydrocarbon liquid, which, even when nearly exhausted, will be uniformly distributed throughout the packing. The first layer of packing conveys the liquid to the first plate, and this seizes and conveys it to the next layer of packing, and so throughout the entire series. K represents a condensing-chamber secured to the upper end of the tube B. The said tube is provided with an aperture, I1, opening into the carbu reter, as shown, through which the carbureted gas passes to the condenser. The service-pipe M extends from the top of the condenser to the various burners.
The operation of my apparatus is as follows: The carbureter having been charged with any desired quantity of hydrocarbon fluid, and the generator having been properly charged and made ready for use, on opening the burners the gas will begin to be generated, and will pass up through the pipe 13, and then down pipe 0 and under the plate 1), and out through the aperture or space E into the carburetingchamber. It will then pass up through the compound packing, becoming thoroughly carbureted, after which it will pass to the condenser. The condenser, being packed, as usual, with fibrous material, condenses and returns any superfluous hydrocarbon vapor in the gas.
From the condenser the gas passes to the burners.
It will be evident that the hydrocarbon fluid will be evaporated from all portions of the carbureter before it can be taken up at the ex treme edge or periphery of the bottom, and that so long as there is a particle of the fluid in the carbureter it will seek this point. The air, being admitted at this point all around the carbureter, is necessarily forced through the whole of the hydrocarbon material, no matter what may be the quantity in the carburetor, and is consequently always thoroughly carbureted. B y my system of packing, with fibrous material and metallic relays, I have the packing material constantly and uniformly saturated during the whole operation of the apparatus.
hat I claim is- 1. A carbureter constructed as described,
so that the last portions of the hydrocarbon liquid will be distributed to the extreme outer edge of the carburetor or to its periphery, at which point the gas is admitted, by which means the last drop of the liquid is taken up by the gas, and the gas at all times thoroughly carbureted, substantially as described.
2. The packing herein described,.consisting of thepert'orated plates or relays an d the fibrous or capillary material, as and for the purposes described.
3. The combination of the carburetor, as described, and condenser attached to the end of the tube B, substantially as specified.
4. The combination of the coi'icavo-convex bottom 0, concavo-convex plate 1), and tubes (r and B, substantially as and for the purpose set forth.
5. The combination of the bottom 0, plate 1), pipes G and B, and the compound packing, as herein described.
6. The combination of the carbureter and generator, communicating with each other by the tubes G and .I), substantially as herein described.
\Viti essi s:
( IIAS. L. )oonns, in. E. CIIAFFEE.
A. w. ronrnn.
Publications (1)
Publication Number | Publication Date |
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US152006A true US152006A (en) | 1874-06-16 |
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US152006D Expired - Lifetime US152006A (en) | Improvement in apparatus for carbureting gas and air |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050099254A1 (en) * | 2003-11-12 | 2005-05-12 | Ohnstein Thomas R. | Robotic member |
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0
- US US152006D patent/US152006A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050099254A1 (en) * | 2003-11-12 | 2005-05-12 | Ohnstein Thomas R. | Robotic member |
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