US167847A - Improvement in processes and apparatus for the manufacture of illuminating or - Google Patents
Improvement in processes and apparatus for the manufacture of illuminating or Download PDFInfo
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- US167847A US167847A US167847DA US167847A US 167847 A US167847 A US 167847A US 167847D A US167847D A US 167847DA US 167847 A US167847 A US 167847A
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- US
- United States
- Prior art keywords
- generator
- superheater
- gas
- illuminating
- steam
- Prior art date
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- 238000000034 method Methods 0.000 title description 18
- 238000004519 manufacturing process Methods 0.000 title description 6
- 239000007789 gas Substances 0.000 description 50
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 20
- 238000002485 combustion reaction Methods 0.000 description 18
- 229910052799 carbon Inorganic materials 0.000 description 12
- 239000003921 oil Substances 0.000 description 12
- 235000019198 oils Nutrition 0.000 description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 239000000463 material Substances 0.000 description 10
- 239000004215 Carbon black (E152) Substances 0.000 description 8
- 239000003575 carbonaceous material Substances 0.000 description 8
- 239000003245 coal Substances 0.000 description 8
- 239000000446 fuel Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 150000002430 hydrocarbons Chemical class 0.000 description 8
- 239000007787 solid Substances 0.000 description 8
- 239000011449 brick Substances 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 239000003208 petroleum Substances 0.000 description 6
- 239000011819 refractory material Substances 0.000 description 6
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 4
- 239000010426 asphalt Substances 0.000 description 4
- 239000002802 bituminous coal Substances 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 229940108066 Coal Tar Drugs 0.000 description 2
- 101710025233 LLGL1 Proteins 0.000 description 2
- 241000282320 Panthera leo Species 0.000 description 2
- 239000005864 Sulphur Substances 0.000 description 2
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 2
- 239000003830 anthracite Substances 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 2
- 238000010000 carbonizing Methods 0.000 description 2
- 239000002817 coal dust Substances 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 235000012343 cottonseed oil Nutrition 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 230000001105 regulatory Effects 0.000 description 2
- 230000000284 resting Effects 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 239000002023 wood Substances 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
- Figure 1 represents a vertical section of the complete apparatus
- Fig. 2 a plan of the same.
- a is the primary gas-generator, which consists of a casing, b, made of boiler-iron, or other suitable material, and lined with firebricks c, or other suitable refractory materials.
- d is a superheater, for preparing steam for decomposition. This also consists of a casing of iron or other suitable material, lined with fire-bricks or other suitable refractory materials e, the lDClOSBk]. space being filled with loosely-laid fire-bricks, or other suitable refractory materials, resting on a perforated At the bottom of the superheater d is a combustion-chamber, g. h is a tight-fitting valve, to be raised or lowered at pleasure.
- i is a heat-restorer, which forms the stack for carrying off the products of combustion. This consists of an ordinary iron stack of increased dimension, with beads j at top and bottom, in which heads are inserted ordinary boiler tubes.
- k is a tube through which there is forced into the stack i atmospheric air, which circulates around the tubes in said stack, and issues out at the lower end of the stack in a heated condition, thence passing through tube Z to support combustion in generator at, and in the com bust-ion-chamher ⁇ 1 of the superheater d.
- m is an elevated tank for holding petroleum or other hydrocarbon oils. The tank m is supported by a column, (not shown,) or in any convenient manner.
- a is a hopper, provided with a close- 1y -'fitting bell or cone valve, 0, and also a closely-fitting lid, p.
- q is a tube for conveying gas from generator at to the boiler 1, which is an upright tubular boiler, with chambers s and t at top and bottom, respectively.
- at is a tube for conveying gases from chamber t to the washer o.
- w is a diaphragm, forming an inclined plane in the Washer 12. This inclined plane should be rough or corrugated on its under side.
- a: is a tube for conveying gases from washer o.
- g is an ordinary gas-scrubber, filled with coke or other suitable materials.
- 2 is a tube for conveying gases into holder at, or other points of storage, or directly to any place of consumption.
- b is a well for catching condensed oils or tar, should any exist after leaving the generator.
- 0 is a tank for holding petroleum or other hydrocarbon oils, and d is a pump for forcing the same, as required, into the elevated tank m.
- e is a closely-fitting valve, to be raised or lowered at pleasure for regulating the flow of carbonic oxide through the pipe f into the combustionchamber g.
- the generator a is also provided with a closely-fitting door, (not shown in the drawing,) communicating with the ash-pit 9.
- valves 0 and it being raised to allow of the free es'capeof the products of combustion through the open brick-work in superheater d, and up through the tubes in the heat-restoring stack 1'.
- anthracite or bituminous coals beside which, however, may be mentioned any kind of wood, all kinds of woody rubbish, finely-cut straw, coal-dust or slack, asphaltum, &c.
- a fan-blower or other suitble apparatus is caused to force air through the tube 70 into the heat-restorer i, from which a sufficient quantity of warmed or heated air is admitted through the tubes '1 and h to cause moderate combustion on the grate-bars of the gas-generator a.
- the carbonic acid which is caused by the union of oxygen and carbon, at the bottom of the gen-.
- impure carbons are used for carbonizing the hydrogen, the usual purifiers will be necessary; but when petroleum and other pure carbons are employed, a purifier is not required.
- the heat-restorer c' may, instead of serving to heat the air-blast, as before described, be used as a boiler for generating steam, and may either remain in its present position, or be set adjacent to the superheater, where the hot products of combustion may be conveyed to it in the proper manner.
- I claim 1 For the manufacture of illuminating and heating gas, the process which consists of dropping or otherwise admitting in limited quantities, continuously or intermittently, hydrocarbon oils or other carbonaceous substances, liquid or solid, onto the top of a thick mass of coal or other carbonaceous substance, in a state of incandescence, in a close chamber previously heated'by direct internal combustionflwith or without the introduction of steam, and then, for the purpose of superheating and fixing the gases of said chamber, passing them from said chamber into and through a second chamber, which also has beenpreviously heated by direct internal combustion, substantially as set forth.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
ZSheetv-Sheetf.
Process and Apparatus for the Manufacture of Mlgl All
, arch, f, of like materials.
THADDEUS S. O. LOWE, OF NORRISTOWN, PENNSYLVANIA.
. IMPROVEMENT IN PROCESSES AND APPARATUS FOR THE MANUFACTURE OF ILLUMINATING 0R HEATING GAS.
Specification forming part of Letters Patent No. 161,847, dated September 21, 1875; application filed March 10, 187 5.
To all whom it may concern:
Beit known that I, THADDEUS S. O. LOWE, of N orristown, Montgomery county, Pennsylvania, have invented an Improvement in Processes and Apparatus for Producing and Using Hydrocarbon .and other Gas for Heating and Illuminating Purposes, and other purposes, of which the following is a specification:
In the annexed drawings, which form a part of this specification, Figure 1 represents a vertical section of the complete apparatus, and Fig. 2 a plan of the same.
a is the primary gas-generator, which consists of a casing, b, made of boiler-iron, or other suitable material, and lined with firebricks c, or other suitable refractory materials. d is a superheater, for preparing steam for decomposition. This also consists of a casing of iron or other suitable material, lined with fire-bricks or other suitable refractory materials e, the lDClOSBk]. space being filled with loosely-laid fire-bricks, or other suitable refractory materials, resting on a perforated At the bottom of the superheater d is a combustion-chamber, g. h is a tight-fitting valve, to be raised or lowered at pleasure. i is a heat-restorer, which forms the stack for carrying off the products of combustion. This consists of an ordinary iron stack of increased dimension, with beads j at top and bottom, in which heads are inserted ordinary boiler tubes. k is a tube through which there is forced into the stack i atmospheric air, which circulates around the tubes in said stack, and issues out at the lower end of the stack in a heated condition, thence passing through tube Z to support combustion in generator at, and in the com bust-ion-chamher {1 of the superheater d. m is an elevated tank for holding petroleum or other hydrocarbon oils. The tank m is supported by a column, (not shown,) or in any convenient manner. a is a hopper, provided with a close- 1y -'fitting bell or cone valve, 0, and also a closely-fitting lid, p. q is a tube for conveying gas from generator at to the boiler 1, which is an upright tubular boiler, with chambers s and t at top and bottom, respectively. at is a tube for conveying gases from chamber t to the washer o. w is a diaphragm, forming an inclined plane in the Washer 12. This inclined plane should be rough or corrugated on its under side. a: is a tube for conveying gases from washer o. g is an ordinary gas-scrubber, filled with coke or other suitable materials. 2 is a tube for conveying gases into holder at, or other points of storage, or directly to any place of consumption. b is a well for catching condensed oils or tar, should any exist after leaving the generator. 0 is a tank for holding petroleum or other hydrocarbon oils, and d is a pump for forcing the same, as required, into the elevated tank m. e is a closely-fitting valve, to be raised or lowered at pleasure for regulating the flow of carbonic oxide through the pipe f into the combustionchamber g. The generator a is also provided with a closely-fitting door, (not shown in the drawing,) communicating with the ash-pit 9.
When it is desired to put this apparatus into operation, I build a fire on the grate-bars.
in generator a, the valves 0 and it being raised to allow of the free es'capeof the products of combustion through the open brick-work in superheater d, and up through the tubes in the heat-restoring stack 1'.
I now gradually introduce into generator at 'anydesired solid carbonaceous substances,
preferring either anthracite or bituminous coals, beside which, however, may be mentioned any kind of wood, all kinds of woody rubbish, finely-cut straw, coal-dust or slack, asphaltum, &c.
In the meantime a fan-blower or other suitble apparatus is caused to force air through the tube 70 into the heat-restorer i, from which a sufficient quantity of warmed or heated air is admitted through the tubes '1 and h to cause moderate combustion on the grate-bars of the gas-generator a. As the thickness of fuel increases in generator at, and while it is being brought into an incandescent state, the carbonic acid which is caused by the union of oxygen and carbon, at the bottom of the gen-.
erator, while passing up through the thickness of incandescent. fuel, becomes recarbonized, and is thus converted into carbonic oxide.
This highly-inflammable gas, in union with the sulphur of the coal and other impurities STATES PATENT Qrrron.
' The forms of apparatus which may be used in carrying out my above-described processes are various, and I have-prepared many drawings of modified forms of apparatus for-carry,- ing out said process; .but I prefer "the form shown, it being in every respect simple and easy of management.
Instead of employing oil in thecarbonizing process, as above described, other substances containing volatile carbon may be employed, such as rich bituminous coal, rosin, cottonseed, ordinary coal-tar, asphaltum, fats of all kinds, residuum from oil-refineries, 8w. Care, however, should be taken when using any kind of solid carbon, that the same is evenly spread on the top surface of the heated fuel or material in the generator at, in such a manner that the hot gases, while emerging from the top of said hot fuel, will come in contact.
with such solid or lumpy carbon, and thereby assist in its volatilization.
In case of using bituminous coal, it would be desirable to use some additional volatile carbon oil, to add to the hydrogen being generated from the steam.
If impure carbons are used for carbonizing the hydrogen, the usual purifiers will be necessary; but when petroleum and other pure carbons are employed, a purifier is not required.
In many cases it will be found advantageous to admit the steam (preferably highly heated) through pipe m at the bottom of generator a, causing it to pass up through the incandescent coals and mingle with the carbon gas in the top of the generator, as before described, and then to pass the mixed mass through connecting-flue f to the bottom of superheater d, and up through the mass of heated brick-work therein contained, and to be discharged through opening a at the top of superheater d, from which opening the gases may be conveyed to the washer 12, either directly or after having been previously passed through the boiler 1", for the purpose of utilizing its heat in the generation of steam, or after having been employed for superheating steam or air, or both.
The principal advantage gained by passing the mass of gases from generator a through the highlyheated fire-bricks in the superheater d, is a more thorough decomposition of the elements which, having been passed up through the incandescent coal in the generator for too long a time, might contain considerable undecomposed vapor, which would be converted into a fixed gas by being'subjected to a higher heat, such as the superheater contains.
When it is desired to superheat the steam preparatory to its decomposition, and at the same time carry on the process of more permanently fixing the mixed gases evolved in the generator, it is necessary to use, in connection with the generator, two of the chambers described as superheater d-to wit, one for the superheating of the steam, and the other for the fixing of the gases, both chambustion of a portion of the gases from generw ator a, and, in this case, the mixed gases from r the generator, instead of being led off to and through the tubes of boiler a", as described, or,
instead ofbeing led off from the genera-tor directly to the washer, are first passed through the additional chamber or superheater last above referred to.
The heat-restorer c' may, instead of serving to heat the air-blast, as before described, be used as a boiler for generating steam, and may either remain in its present position, or be set adjacent to the superheater, where the hot products of combustion may be conveyed to it in the proper manner.
In cases where gas extremely rich in carbon is desired, the same will be best produced by omitting the steam and generating the gas from oils alone, using the generator it either. alone or in conjunction with the superheater.
I claim 1. For the manufacture of illuminating and heating gas, the process which consists of dropping or otherwise admitting in limited quantities, continuously or intermittently, hydrocarbon oils or other carbonaceous substances, liquid or solid, onto the top of a thick mass of coal or other carbonaceous substance, in a state of incandescence, in a close chamber previously heated'by direct internal combustionflwith or without the introduction of steam, and then, for the purpose of superheating and fixing the gases of said chamber, passing them from said chamber into and through a second chamber, which also has beenpreviously heated by direct internal combustion, substantially as set forth.
2. The process for producing an illuminating-gas, which consists of superheating steam, by passing it through a chamber previously heated by direct internal combustion, then causing said steam to pass through a mass of coal or other carbonaceous substance, in a state of incandescence, in a close generatingchamber, to decompose the steam, and afterward, for the purpose of still further heating the gases of said generating-chamber, and therebyproducing a more fixed gas, passing the gases from said generating-chamber into and through another superheating-chamber, which has been previously heated by direct internal combustion, substantially as set forth.
3. The combination of the generator a, superheater d, the heat-restorerj, and means for forcing air through the pipe 70, around the tubes of the heat-restorer '0', through pipes l, h, and j, into the chamber g, for generating and securing intense combustion in said chamber g, substantially as set forth.
4. The combination of the generator a, superheater d, heat-restorer i, elevated oil-tank m, the upright tubular boiler r, with their several connecting-pipes and other appurtenant parts, as described, constituting apparatus for rapidly evolving illuminating-gas, and fixing the same in its gaseous condition, substantially as set forth.
5. The combination of the generator a, superheater d, heat-restorer t, elevated oil-tank m, upright tubular boiler r, wash-box a, scrubber y, with their several connecting-pipes and other appurtenant parts, as described, constituting apparatus for rapidly evolving illuminating and heating gas, fixing the same in its gaseous condition, and purifying the same preparatory to storage or immediate use, substantially as set forth.
T. S. O. LOWE.
Witnesses R. B. SANDERSON, Tnos. A. BURTT.
W. S. MARTIN.
Fog-Signals.
N0, I67,848, Patented Sept.21,l875.
W'TNESSES. I 2/:zt%@
N. PETERS, PHDTO-LITHOGRAPNER. WASHINGTON. D. C.
Publications (1)
Publication Number | Publication Date |
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US167847A true US167847A (en) | 1875-09-21 |
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US167847D Expired - Lifetime US167847A (en) | Improvement in processes and apparatus for the manufacture of illuminating or |
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- US US167847D patent/US167847A/en not_active Expired - Lifetime
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