US396338A - Sylvania - Google Patents
Sylvania Download PDFInfo
- Publication number
- US396338A US396338A US396338DA US396338A US 396338 A US396338 A US 396338A US 396338D A US396338D A US 396338DA US 396338 A US396338 A US 396338A
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- US
- United States
- Prior art keywords
- steam
- chamber
- generator
- gases
- chambers
- Prior art date
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- 239000007789 gas Substances 0.000 description 46
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 36
- 239000000446 fuel Substances 0.000 description 26
- 229910052799 carbon Inorganic materials 0.000 description 24
- 239000003245 coal Substances 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 8
- 239000003830 anthracite Substances 0.000 description 8
- 239000011449 brick Substances 0.000 description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 4
- 235000011613 Pinus brutia Nutrition 0.000 description 4
- 241000018646 Pinus brutia Species 0.000 description 4
- 239000002802 bituminous coal Substances 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 239000011819 refractory material Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- 206010022000 Influenza Diseases 0.000 description 2
- 241000282320 Panthera leo Species 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000006011 modification reaction Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
Definitions
- the obj eet of this invention is the production of water-gas by the use of sawdust, pine wood, bituminous coal, or other comparatively inexpensive carbonaceous materials.
- I employ two controllably-connected chambers. In one of these chambers the more inexpensive fuels above referred to are employed for the decomposition of steam, the resulting gases containing volatile carbon.
- anthracite coal, hard coke, charcoal, or other combustible materials, as free as possible 0 from volatile carbon, (preferring anthracite coal,) are kept in a state of incandescence for the purpose of removing the volatile carbon from the gases produced in the firstnamed chamber or main generator.
- Figure 1 is a vertical section of the complete apparatus on the line X X of Fig. 2, and 40 Fig. 2 a horizontal section of the same on the line Y Y of Fig. 1.-
- the main generator consists of an iron shell lined with fire-bricks or other refractory materials and provided with fire-grate bars or a fire-brick arch over an ash-pit at the bottom.
- the main generator comprises the fuelspace A, steam-superheater B, consisting of several layers of fire-bricks or other refractory materials loosely laid, and a steam-gen- 5-0 erator, 0, consisting ofseveral layers of metal bars crossed and laid loosely, a water-sprayin g nozzle, D, and a pipe, D, leading to a water or steam supply, all as described in my pending application above mentioned.
- E is a chamber consisting of an iron shell lined with firebricks or otherrefractory materials and provided with grate-bars F, of metal or fire-bricks, with an ash-pit below.
- G is a fine connecting the two chambers A and E at the bottom.
- I and J are valves through which an airblast is admitted to the fuel in the respective chambers.
- K K K K K K are flues, of which the fines K K K connect the chamber E with the chamber A at the top, and the fiues K K K confuels in chambers A and E while heating the apparatus.
- N and N are doors through which the chambers A and E are charged with fuels.
- O is a valve for allowing the products of combustion generated while heating up the apparatus to escape to the atmosphere.
- P is a pyrometer for determining the heat in the upper part of the superheater.
- Q is a steam-pipe provided with a cock for conducting superheated steam from the upper 0 part of chamber A into the flue G
- R is another steam-pipe provided with a cock for admitting steam. into the ash-pit of chamber A, both or either of these pipes being used as desired, for the purpose of mixing steam with 5 the gases passing from the generator A before these gases pass through the fuel in chamber E.
- valves H and L are closed and valves L and O are opened.
- An air-blast is then. admitted through valves I and J to the fuels in chambers A and E.
- the unburned gases arising from these chambers are burned by air-blasts admitted at M, heating the firebricks B to a high degree and the metal bars 0 to a considerable degree sufficient, when desired, to generate steam or to evaporate water into steam.
- valves 0 and L are closed, as well as the valves admitting air-blast to various parts of the apparatus, while valves H and L are opened.
- the effect of this operation is to decompose the steam in chamber A, and in so doing, when sawdust, pine wood, bituminous coal, or other materials containing volatile carbon are there employed, the resulting gases containing more or less surplus carbon, which is carried along with the other gases from this chamber into the chamber E,and on passing up through the fuel thereinsuch as anthracite coal, hard coke, or charcoal in a highly-heated condition the effect is that the surplus carbon carried in the gas from chamber A is deposited on the highly-heated surfaces of the more solid carbons in chamber E, thereby producing gas composed of carbon monoxide and hydrogen free from surplus carbon, a product which, for many uses in the arts, is exceedingly desirable.
- the carbon deposited on the surfaces of the hard fuel in chamber E serves to a great ex tent to heat itself again when the air-blast is turned on and to prevent the rapid combustion of the more expensive fuels contained in this chamber.
- Steam for this purpose maybe admitted at will into the ash-pit of either generator or into the passage-way between the generators, where it will be mixed with the gases from generator A, or it may be admitted by so regulatingthe valve Lthat a portion of the superheated steam from the su perheater in generator A may pass in by pipe Q and mix with the gases resulting from the decomposition of the steam passed through the coal in generator A; or, instead of passing the steam down, through the coal in generator A, the valve II. between the generators A and E can be closed and steam admitted to the ash-pit of generator A and passed up through the fuel in this generator, while another supply of steam orspray of water for the generation. of steam may be admitted at the top of the superheater, whereby the steam is brought into contact with the gases from the'fuels and afterward passed together tlnough theincandescent fuel in chamber E.
- a main generator comprising the fuel-chamber A, the stealn-superheaterl3, and the steam-generator 0, all inelosed by a single upright shell having an ash-pit and steam-inlet at the bottom, an air-blast inlet at the upper part of the fuel-space, and a valve, 0, and water-spraying device I) above the steam-generator, a separate generator orfuelehamber, E, a flue, G, connecting the ash-pits of the chambers A and E, the valve H and valved air-inlets I J, located in the flue G, the valved llues K li K connecting the chambers A and E at the top, and a steam-pipe, Q, connecting the fines K and G, substantially as described.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Solid-Fuel Combustion (AREA)
Description
(No Model.)
T. S. G. LOWE.
APPARATUS FOR THE MANUFACTURE OF GAS.
N0. 396,338. Patented Jan. 15, 1889.
UNTTTTn STATES PATENT @rrrcn.
THADDEUS S. O. LOIVE, OF ORRISTOIVN, PENNSYLVANIA, ASSIGNOR TO THE GUARANTEE TRUST AND SAFE DEPOSIT COMPANY,.TRUSTEE, OF PENN- SYLVANIA.
APPARATUS FOR THE MANUFACTURE OF GAS.
SPECIFICATION forming part of Letters Patent No. 396,338, dated January 15, 1889.
Application filed July 2, 1885. Serial No. 170,466. (No model.)
To all whom it may concern.-
Be it known that I, THADDEUS S. C. LOWE,
a citizen of the United States, residing at Norristown, Montgomery county, Pennsylvania, have invented a new and useful Improvement in Apparatus for the Manufacture of ater- Gas, of which invention the following is a specification;
This invention is a modification of the apparatus described in mypending application, filed November 12, 1884, Serial No. 147,764.
In order to obtain the best results in pro ducing light from water-gas by incandescence it is necessary that the water-gas shallbe free of volatile carbon. It is desirable to be able to make water-gas by the use of inexpensive fuels.
The obj eet of this invention is the production of water-gas by the use of sawdust, pine wood, bituminous coal, or other comparatively inexpensive carbonaceous materials. To effect this result I employ two controllably-connected chambers. In one of these chambers the more inexpensive fuels above referred to are employed for the decomposition of steam, the resulting gases containing volatile carbon. In the other chamber anthracite coal, hard coke, charcoal, or other combustible materials, as free as possible 0 from volatile carbon, (preferring anthracite coal,) are kept in a state of incandescence for the purpose of removing the volatile carbon from the gases produced in the firstnamed chamber or main generator.
The apparatus employed in carrying out my process is represented in the annexed drawings, in which Figure 1 is a vertical section of the complete apparatus on the line X X of Fig. 2, and 40 Fig. 2 a horizontal section of the same on the line Y Y of Fig. 1.-
The main generator consists of an iron shell lined with fire-bricks or other refractory materials and provided with fire-grate bars or a fire-brick arch over an ash-pit at the bottom.
The main generator comprises the fuelspace A, steam-superheater B, consisting of several layers of fire-bricks or other refractory materials loosely laid, and a steam-gen- 5-0 erator, 0, consisting ofseveral layers of metal bars crossed and laid loosely, a water-sprayin g nozzle, D, and a pipe, D, leading to a water or steam supply, all as described in my pending application above mentioned.
E is a chamber consisting of an iron shell lined with firebricks or otherrefractory materials and provided with grate-bars F, of metal or fire-bricks, with an ash-pit below.
G is a fine connecting the two chambers A and E at the bottom.
His a valve for closing and opening the flue G.
I and J are valves through which an airblast is admitted to the fuel in the respective chambers.
K K K K are flues, of which the fines K K K connect the chamber E with the chamber A at the top, and the fiues K K K confuels in chambers A and E while heating the apparatus. v
N and N are doors through which the chambers A and E are charged with fuels.
O is a valve for allowing the products of combustion generated while heating up the apparatus to escape to the atmosphere.
P is a pyrometer for determining the heat in the upper part of the superheater.
Q, is a steam-pipe provided with a cock for conducting superheated steam from the upper 0 part of chamber A into the flue G, and R is another steam-pipe provided with a cock for admitting steam. into the ash-pit of chamber A, both or either of these pipes being used as desired, for the purpose of mixing steam with 5 the gases passing from the generator A before these gases pass through the fuel in chamber E.
WVhen it is desired to put this apparatus into operation, valves H and L are closed and valves L and O are opened. An air-blast is then. admitted through valves I and J to the fuels in chambers A and E. The unburned gases arising from these chambers are burned by air-blasts admitted at M, heating the firebricks B to a high degree and the metal bars 0 to a considerable degree sufficient, when desired, to generate steam or to evaporate water into steam. \Vhen the fuels in chambers A and E have become sufficiently heated, valves 0 and L are closed, as well as the valves admitting air-blast to various parts of the apparatus, while valves H and L are opened. Steam, or water-for the production of steam, is then admitted through pipe D, and after the same has passed over the surfaces of the heated materials occupying the upper portion of the chamber A passes as highlyheated steam down through the carbonaceous materials contained in chamber A, and the resulting gas passes out through flue G into chamber E and up through the anthracite coal or other solid carbonaceous materials contained in chamber E, and thence off through :tlues K, K, and K to the washer, scrubber, and holder or directly to the place of consumption, passing in any case, if desired, through a heat-restorer. The effect of this operation is to decompose the steam in chamber A, and in so doing, when sawdust, pine wood, bituminous coal, or other materials containing volatile carbon are there employed, the resulting gases containing more or less surplus carbon, which is carried along with the other gases from this chamber into the chamber E,and on passing up through the fuel thereinsuch as anthracite coal, hard coke, or charcoal in a highly-heated condition the effect is that the surplus carbon carried in the gas from chamber A is deposited on the highly-heated surfaces of the more solid carbons in chamber E, thereby producing gas composed of carbon monoxide and hydrogen free from surplus carbon, a product which, for many uses in the arts, is exceedingly desirable.
The carbon deposited on the surfaces of the hard fuel in chamber E serves to a great ex tent to heat itself again when the air-blast is turned on and to prevent the rapid combustion of the more expensive fuels contained in this chamber.
In cases Where a very large amount of surplus volatile carbon escapes with the gases from generator A it is sometimes desirable to mix with such gases before they pass through the generator E a limited amount of steam, preferably highly superheated, the result of which is the absorption of the surplus volatile carbon and the production of a larger amount of carbonic oxide and hydrogenthe kind of gas most desiredthe resulting gases being thus prevented from containing the obj ectionable volatile carbon. Steam for this purpose maybe admitted at will into the ash-pit of either generator or into the passage-way between the generators, where it will be mixed with the gases from generator A, or it may be admitted by so regulatingthe valve Lthat a portion of the superheated steam from the su perheater in generator A may pass in by pipe Q and mix with the gases resulting from the decomposition of the steam passed through the coal in generator A; or, instead of passing the steam down, through the coal in generator A, the valve II. between the generators A and E can be closed and steam admitted to the ash-pit of generator A and passed up through the fuel in this generator, while another supply of steam orspray of water for the generation. of steam may be admitted at the top of the superheater, whereby the steam is brought into contact with the gases from the'fuels and afterward passed together tlnough theincandescent fuel in chamber E.
Instead of placing the piled materials for generating and superheating steam, or either of these purposes, in the upper part of chamber A, as above described, they may be placed in a separate chamber connected by flue with generator A.
I claim In an apparatus for making water-gas, the combination of a main generator comprising the fuel-chamber A, the stealn-superheaterl3, and the steam-generator 0, all inelosed by a single upright shell having an ash-pit and steam-inlet at the bottom, an air-blast inlet at the upper part of the fuel-space, and a valve, 0, and water-spraying device I) above the steam-generator, a separate generator orfuelehamber, E, a flue, G, connecting the ash-pits of the chambers A and E, the valve H and valved air-inlets I J, located in the flue G, the valved llues K li K connecting the chambers A and E at the top, and a steam-pipe, Q, connecting the fines K and G, substantially as described.
T. S. LOXVE. Witnesses:
J. E. SHAW,
3URroN LooMIs.
Publications (1)
Publication Number | Publication Date |
---|---|
US396338A true US396338A (en) | 1889-01-15 |
Family
ID=2465308
Family Applications (1)
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US396338D Expired - Lifetime US396338A (en) | Sylvania |
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US (1) | US396338A (en) |
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- US US396338D patent/US396338A/en not_active Expired - Lifetime
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