US259723A - Process of and apparatus for producing illuminating and heating gas - Google Patents
Process of and apparatus for producing illuminating and heating gas Download PDFInfo
- Publication number
- US259723A US259723A US259723DA US259723A US 259723 A US259723 A US 259723A US 259723D A US259723D A US 259723DA US 259723 A US259723 A US 259723A
- Authority
- US
- United States
- Prior art keywords
- generator
- gas
- superheater
- fuel
- pipe
- 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
- 238000010438 heat treatment Methods 0.000 title description 10
- 238000000034 method Methods 0.000 title description 6
- 239000007789 gas Substances 0.000 description 42
- 239000000446 fuel Substances 0.000 description 40
- 239000003575 carbonaceous material Substances 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 10
- 150000002430 hydrocarbons Chemical class 0.000 description 10
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 239000006233 lamp black Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 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
- 238000009826 distribution Methods 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
Images
Classifications
-
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/087—Heating or cooling the reactor
Definitions
- My invention relates to the mode of applying heat to a mixture of water gas andhydr0- carbon vapors for the purpose of fixing and combining the same, also to the'mannerof connecting the generator and the superheater;
- the drawing represents a vertical section of the apparatus, showing the various parts of Heretofore in the manufacture of what known as water-gas two chambers containing fuel were employed, the fuel in one of these being heated by the combustion of the gases produced in the other. This is objectionable for the reason that the body of fuel where the gas is produced becomes too highlyheated before the body of fuel in the other is --sufliciently heated for the decomposition ofsteam, thereby decomposing the hydrocarbons tosuch an extent as to produce lamp-black. Also,'two chambers containing fuel have been employed,
- the fuel in the generator being greater than that in the superheater, requires the largest amountof heat, while the fuel in the superheater, being less, requires less amountof heat, and is consequently more quickly heat ed and by the employment of the independent fires and blasts I am enabled to heat the bodies (No model.)
- the object of the second partot' my invention is to maintain a uniform temperature throughout I the mass of fuel, and thereby prevent the formation of clinker.
- A is the gas-generator, which consists of a casing, B, made ot'Jboiler-iron or other suitable material, and lined with some suitable refractory material, C. v
- D is a space filled with non-conducting materialto prevent radiation.
- E is the 'superheater, and-in construction is similar to the generator.
- G is alever for manipulating thevalveF; HH,the openings for introducing the fuel to :generator and superheater; I I, the-covers for same; J, the cutter-bars for securing the cov 'ers; K, the bearing and grate bars; L, the doors; M, the ash-pans; N, the a r-valve in blast-pipe; O, 0 O and 0 the air and gas valves 5' P, the blast-pipe to superheater; Q, the blast-pipe to and gas-pipe from generator; 1%, the lower gas-outlet from the generator; S,"the upper gas-outlet of generator; T, the gas-inlet to the superheater; W, the oil-pipe; X, the oil-valve; Y' the gas-outlet of superheater; Z, the hydraulic seal; U and V, the valves for supplying steam to the top and bottom of the generator, respectively.
- hydrocarbon-oil or other suitable material containing carbon-for example, petroleum orrosin- is admitted to the inlet pipe T of the snperheater through oil-valve X and oil-pipe N, as indicated by arrows marked 4, where it; comes in contact with and is instantly vaporized by the hot gases from the generator, when the mixed gases, now consisting of hydrocarbon vapors and the gases produced in the generator, are passed down through the incandescent fuelcontained in the superheater, where any carbonicacid which may have escaped through the generator is converted into carbonic oxide and a thorough combination of all the gases effected.
- the proper time for doing so is determined by the appearance of the fuel, which can be seen through the bulls-cycs provided for that purpose.
- the steam-valve V, oil-valve X, and on tlet-valvc 0 of the generator are then closed, and the escape-valve F, air-valve N, also valves 0 and are opened, and the blast passes into the generator and superheater at the bottom, and the products of combustion then escape through valves F until the fuel in the generator and the superheater has again reached the desired temperature.
- the air-valve N and valves 0' and 0 are then closed, also es cape-valves I and steam and hydrocarbon oil are admitted, as before described.
- a heating or illuminating gas which consists in heating independently the carbonaceous materials simnltaneously in a generator and a snperheater by separate blasts, and. the direct-internal combustion of the coal in each generator and superheater, then decomposing steam bypassing it through one of the beds of the carbonaceous material, then carrying the escaping product-water-gas-forward and mingling it with hydrocarbon vapors, then passing the mixed gases through the other bed of carbonaceous material for fixing the gases,and finally conducting the same to the hydraulic main or seal, as hcreinbefore set forth.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
Description
(No Model.)
11.0. SHIELDS. PROOESSOF'AND APPARATUS FORPRODUGING ILLUMINATING AND HEATING GAS.
Nb.259,7-23. Patented June 20, 1882.
Witnesses V Inventor.-
N. PETERS. Photo-Lilhagraphcr. Washington. D. c
UNITE STATES PATENT OFFICE.
HENRY O. SHIELDS,OF TROY, NEW YORK.
PROCESS OF AND APPARATUS FOR PRODUCING lLLUMlNATlNG AND HEATING GAS.
SPECIFICATION, forming art ofjLetters Patent 'No. 259,723, dated June 20, 1882.
Application filed November-'12, 1881.
To all whom it may concern v Be it known that I,HENRY O. SHIELDS, of
the city of Troy, county of Rensselaer, and
' State of New York, haveinvented certain new my device.
and useful Improvements in the Process of and Apparatus for Producing Illuminating and Heating Gas, of which the followingis a specification, reference being bad to the accompanying drawing and letters of reference marked thereon.
My invention relates to the mode of applying heat to a mixture of water gas andhydr0- carbon vapors for the purpose of fixing and combining the same, also to the'mannerof connecting the generator and the superheater;
The drawing represents a vertical section of the apparatus, showing the various parts of Heretofore in the manufacture of what known as water-gas two chambers containing fuel were employed, the fuel in one of these being heated by the combustion of the gases produced in the other. This is objectionable for the reason that the body of fuel where the gas is produced becomes too highlyheated before the body of fuel in the other is --sufliciently heated for the decomposition ofsteam, thereby decomposing the hydrocarbons tosuch an extent as to produce lamp-black. Also,'two chambers containing fuel have been employed,
the incandescent condition of the fuel being chamber, to secure the incandescent condition of the carbonaceous materials in a short period of time. The fuel in the generator, being greater than that in the superheater, requires the largest amountof heat, while the fuel in the superheater, being less, requires less amountof heat, and is consequently more quickly heat ed and by the employment of the independent fires and blasts I am enabled to heat the bodies (No model.)
of carbonaceous material independent of each other, at a great saving of fuel and time, without producing lamp-black or effecting the illuminating property of the illuminating-gas.
The object of the second partot' my invention,-which pertains more tothe manner ofconnectin g the generator and the superheater than "to the apparatus as a whole, is to maintain a uniform temperature throughout I the mass of fuel, and thereby prevent the formation of clinker.
A is the gas-generator, which consists of a casing, B, made ot'Jboiler-iron or other suitable material, and lined with some suitable refractory material, C. v
D is a space filled with non-conducting materialto prevent radiation.
E is the 'superheater, and-in construction is similar to the generator.
F'is an escape-'ralve for passage of the pro "ducts of combustion. r
G is alever for manipulating thevalveF; HH,the openings for introducing the fuel to :generator and superheater; I I, the-covers for same; J, the cutter-bars for securing the cov 'ers; K, the bearing and grate bars; L, the doors; M, the ash-pans; N, the a r-valve in blast-pipe; O, 0 O and 0 the air and gas valves 5' P, the blast-pipe to superheater; Q, the blast-pipe to and gas-pipe from generator; 1%, the lower gas-outlet from the generator; S,"the upper gas-outlet of generator; T, the gas-inlet to the superheater; W, the oil-pipe; X, the oil-valve; Y' the gas-outlet of superheater; Z, the hydraulic seal; U and V, the valves for supplying steam to the top and bottom of the generator, respectively.
When it is desired to put this apparatus in operation I first build a fire on grate-bars K inthegenerator and superheater, the escapewalve F'and-d'oor L being left opento allow a supply of air to the fuel and to permit the products of combustion to escape, as indicated by the dotted-line arrows marked 2. As soon as the fires are properly kindled in the generator and superheater fuel is introduced through the openings H until filled to the required height for the decomposition of steam in the generator A and for fixing and superheating the gases in the superheater E.
the meantime, the doors L having been closed, a blast of air is introduced through the valve N and pipes l. and Q to the ash-pans of the generatorA and superheater E. The air then passes up through the coal, and the products of combustion escape through the valves F, and the blast is continued until the coal or other carbonaceous material attains the proper temperature. The air-valve N, escape'valvcs F, and valves 0 and O are then closed and valve 0 in pipe S opened. Steam perfectly superheated is then admitted to the ash-pan of the generator through steam-valve V and pipe Q, and passes under and up through the grate-bars and fuel, becoming decomposed, and the escaping prod uctswater-gas-pass out of the generator through pipe S and enter the superheater E through pipe T, as indicated by arrows marked 1, at a very high temperature. Just after admitting steam to-the ash-pan of the generator, hydrocarbon-oil or other suitable material containing carbon-for example, petroleum orrosin-is admitted to the inlet pipe T of the snperheater through oil-valve X and oil-pipe N, as indicated by arrows marked 4, where it; comes in contact with and is instantly vaporized by the hot gases from the generator, when the mixed gases, now consisting of hydrocarbon vapors and the gases produced in the generator, are passed down through the incandescent fuelcontained in the superheater, where any carbonicacid which may have escaped through the generator is converted into carbonic oxide and a thorough combination of all the gases effected. In the passage of the gas from the top of the snperheater to the ash-pan and outletpipe Y at the bottom of the superheater every particle of it is brought in direct contact with the incandescent fuel, which insures itagainst condensation and loss of illuminating-power during storage and distribution, and is also a cheaper and much more effective way of applying heat than the methods heretofore employed, such as passing the gas through retorts or brickwork heated by radiation or otherwise. After considerable steam has passed through the generator A and gas through the superhcatcr .E, much heat has been absorbed, and it becomes necessary to restore it to both chambers.
The proper time for doing so is determined by the appearance of the fuel, which can be seen through the bulls-cycs provided for that purpose. The steam-valve V, oil-valve X, and on tlet-valvc 0 of the generator are then closed, and the escape-valve F, air-valve N, also valves 0 and are opened, and the blast passes into the generator and superheater at the bottom, and the products of combustion then escape through valves F until the fuel in the generator and the superheater has again reached the desired temperature. The air-valve N and valves 0' and 0 are then closed, also es cape-valves I and steam and hydrocarbon oil are admitted, as before described. When it is found that the fuel in the generator is at a higher temperature at its top than it isat the bottom the steam is admitted through steamvalve U into pipe S at the top of the gener' ator, and is forced down through the fuel, the gas escaping through pipe Q,, alves O and O, and up through pipe R to inlet-pipe 'I of the superheater, as indicated by the arrows marked 3, when the hydrocarbon oil is introduced, and the balance of the manipulation the same as before described. 7
In reversing the charges of steam from the top to the bottom of the generator the formation of clinker is prevented to a great extent,
.as the temperature is kept equal throughout the entire mass of fuel. The same rule can be applied to advantage to the superheatcr; but for convenience I have only shown one inlet and one outlet.
\Vhat I claim as my invention, anddesire to secure by Letters Patent, is-
l. The process of manufacturing a heating or illuminating gas which consists in heating independently the carbonaceous materials simnltaneously in a generator and a snperheater by separate blasts, and. the direct-internal combustion of the coal in each generator and superheater, then decomposing steam bypassing it through one of the beds of the carbonaceous material, then carrying the escaping product-water-gas-forward and mingling it with hydrocarbon vapors, then passing the mixed gases through the other bed of carbonaceous material for fixing the gases,and finally conducting the same to the hydraulic main or seal, as hcreinbefore set forth.
2. In combination with a gas-generator, the by-pass pipe 1%, pipes S and Q, and connecting steam-pipes U and V, with their connecting-valvcs, for the purpose of reversing the direction of steam into the generator and the escape of gas therefrom, substantially as set forth.
In witness whereof I have hereto set my hand this 1st day of November, 1881.
HENRY O. SHIELDS. Witnesses: WM. H. HOLLISTER, J r.,
N. DAVENPORT.
Publications (1)
Publication Number | Publication Date |
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US259723A true US259723A (en) | 1882-06-20 |
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US259723D Expired - Lifetime US259723A (en) | Process of and apparatus for producing illuminating and heating gas |
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