US254871A - Yapoe feom liquid eydbocaebons - Google Patents

Yapoe feom liquid eydbocaebons Download PDF

Info

Publication number
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
Authority
US
United States
Prior art keywords
steam
liquid
pipe
generating
yapoe
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
Application number
Publication date
Application granted granted Critical
Publication of US254871A publication Critical patent/US254871A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/38Production 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
    • C01B3/384Production 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.

Landscapes

  • 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.
US254871D Yapoe feom liquid eydbocaebons Expired - Lifetime US254871A (en)

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
US254871D Expired - Lifetime US254871A (en) Yapoe feom liquid eydbocaebons

Country Status (1)

Country Link
US (1) US254871A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2503883A (en) * 1946-07-24 1950-04-11 William J Miller Fluid heater

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2503883A (en) * 1946-07-24 1950-04-11 William J Miller Fluid heater

Similar Documents

Publication Publication Date Title
US254871A (en) Yapoe feom liquid eydbocaebons
US746409A (en) Oxyhydrocarbon-burner.
US582655A (en) Apparatus for manufacturing gas
US278792A (en) hiyden
US341625A (en) archer
US751085A (en) Leon p
US279154A (en) Facturing
US169326A (en) Improvement in the manufacture of illuminating-gas
US269929A (en) Gas apparatus
US278793A (en) Heney f
US247980A (en) ambler
US416520A (en) Apparatus for the manufacture of gas
US583915A (en) Apparatus for generating gas
US132266A (en) Improvement in vaporizing hydrocarbons for heating
US273230A (en) hanlo n
US444091A (en) Apparatus for the manufacture of gas
US300752A (en) amblee
US483981A (en) Process of and apparatus for the manufacture of gas
US424700A (en) Peters
US721513A (en) Gas-producer.
US418018A (en) hanlon
US477725A (en) Apparatus for making gas
US417658A (en) babbitt
US199363A (en) g-illen
US726379A (en) Gas-generator.