US434954A - Pottery-kiln - Google Patents

Pottery-kiln Download PDF

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US434954A
US434954A US434954DA US434954A US 434954 A US434954 A US 434954A US 434954D A US434954D A US 434954DA US 434954 A US434954 A US 434954A
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kiln
floor
passages
central
air
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • F23G7/066Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
    • F23G7/068Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator using regenerative heat recovery means

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  • Patented Au 26, 1890 Patented Au 26, 1890.
  • FRANK C ROBERTS, OF PHILADELPHIA, PENNSYLVANIA.
  • My invention relates to an improved system of applying the regenerative principle to use in connection with pottery-kilns; and its chief object is to afford a more thorough distribution of heat throughout the kiln; while preserving all the desirable features which result from maintaining the How of the currents through the kiln permanently in the same direction,the reversal of said currents (for the regenerative action) being effected outside of the kiln proper.
  • Figure 1 represents a horizontal section through the kiln and chimney, showing in plan the kiln-floor and in dotted lines the relation of the various passages thereto.
  • Fig. 2 is a vertical central section through the kiln on a plane passing through the kiln on the line y y
  • Fig. 3 is a vertical section on the two radial planes indicated by the lines 00 a: and looking in the direction of the arrows.
  • A represents the exterior wall of the kiln proper, which is preferably circular and provided with a dome-shaped roof B and horizontal floor O.
  • a series of symmetricallyarranged permanent outletpassages d In said floor, and preferably midway between the center of the kiln and the inner surface of its wall, is a series of symmetricallyarranged permanent outletpassages d, which lead downward into an annular flue I-I beneath the floor.
  • valve L leads from said flue to the valvechamber Z of an ordinary reversing-valve L, which chamber communicates on each side with a pair of regenerator-passages P P, which may be filled with fire-brick p or any other material adapted to regenerative purposes, said passages being preferably arranged circumferentially, as shown, with reduced portions I 1', respectively leading to the chamber m of a second reversing-valve M, which communicates on the one hand with an airinlet Q and on the other with a chimney N.
  • regenerators may be of any ordinary construction, and of course are adapted to alternate the outflow of the products of combustion and inflow of air-through the regenerators.
  • the valve L also controls communication between the regenerators and the horizontal air-passage K, which leads inward to a central point beneath the kiln, and there rises vertically, as indicated at F, nearly to the level of the floor 0.
  • the main inlet for gas is indicated by the dotted lines at T, (see Fig. 1,) and communicates with an annular flue J, arranged around the outer periphery of the kiln-wall, from which flue J inwardly-projecting passages g lead to the jets b, above referred to as being formed in the central part of the brick-work E.
  • Branch passages 12, of considerably smaller transverse area than the passages I) lead from the ends of the passages g through the floor of the kiln to a central discharge-orifice S in said floor, immediately above the vertical air-passage F.
  • a series of small vertical air-ducts a rise from the top of the passage f through the floor of the kiln, and are symmetrically disposed around the central gas-orifice S, so as to distribute the air necessary for proper combustion throughout the gas which issues from said opening.
  • the operation of the apparatus is as follows: Gas admitted at the inlet 'I flows into the annular passage J, and thence into the circumferential jets b and central orifice S. The products of combustion pass. out through the openings (1, and thence to one of the regenerators P or P. Assuming the other regenerator to have been previously heated by the outgoing products of combustion, the air admitted at Q passes through said regenerator, and thence, after becoming heated to the proper degree, flows through thepassages K,
  • the operation of the device is continuous, the proper reversal of the currents being of course effected by the reversing-valves L M, and the direction of the currents Within the kiln proper being constant.
  • the arrangement of the outlets for products of combustion at points intermediate between the central and circumferential air and gas inlets gives the best possible distribution of heatin a uniform manner throughout the kiln.
  • the gas can also be heated by the regenerative system, it being only necessary to divide the regenerator passages longitudinally so as to permit the separate heating of air and gas, and to provide controlling-valves at the points of communication between the gas-inlets and regenerators. I do not deem it necessary, however, to describe such modification in detail, as it will be readily understood.
  • I claim- The combination, in a kiln, of an annular gas-passage around the same provided with a main gas-inlet, a series of gas-inlet jets communicating with the said passage and arranged circumferentially within the kiln, a centralorifice in the kiln-floor, a series of converging branch passages leading through the kiln-floor from said jets to said orifice, a series of air-inlet jets circumferentially arranged within the kiln, a central air-passage, a series of radial passages leading through the kiln-floor from the central passage to the air-inlet jets, air-ducts leading from said central passage to the central orifice, a series of permanent outlet-passages for products of combustion arranged in the kiln-floor intermediate between the center and circumference thereof, a chimney, a pairof regenerators communicating with said central air-passage, said outlet-passages, and said chimney, and a pair of re

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Description

3 Sheets-Sheet 1.
(No Model.)
'1". O. ROBERTS.
POTTERY KILN.
No. 434,954. Patented Aug. 26', 1890.
me "ohms raYz ns ca, mom-mun wAsHmmcN, n, c.
(No Model.) 3 sheets sheet 2. F. O. ROBERTS.
POTTERY KILN.
Patented Au 26, 1890.
Inventor fim XV $1 itnesses:
(No Model.) 3 Sheets-Sheet 3. F. 0. ROBERTS.
POTTERY KILN.
No. 434,954. Patented Aug. 26, 1890.
Inventor WKW I UNITED STATES PATENT OFFICE.
FRANK C. ROBERTS, OF PHILADELPHIA, PENNSYLVANIA.
POTTERY-KILN.
SPECIFICATION forming part of Letters Patent No. 434,954, dated August 26, 1890.
Application filed April 2, 1890. Serial No, 346,271. (No model.)
To all whom it may concern.-
Be it known that I, FRANK G. ROBERTS, of Philadelphia, in the State of Pennsylvania, have invented certain new and useful Improvements in Pottery-Kilns, whereof the following is a specification, reference being had to the accompanying drawings.
My invention relates to an improved system of applying the regenerative principle to use in connection with pottery-kilns; and its chief object is to afford a more thorough distribution of heat throughout the kiln; while preserving all the desirable features which result from maintaining the How of the currents through the kiln permanently in the same direction,the reversal of said currents (for the regenerative action) being effected outside of the kiln proper.
In the drawings, Figure 1 represents a horizontal section through the kiln and chimney, showing in plan the kiln-floor and in dotted lines the relation of the various passages thereto. Fig. 2 is a vertical central section through the kiln on a plane passing through the kiln on the line y y, and Fig. 3 is a vertical section on the two radial planes indicated by the lines 00 a: and looking in the direction of the arrows.
A represents the exterior wall of the kiln proper, which is preferably circular and provided with a dome-shaped roof B and horizontal floor O. In said floor, and preferably midway between the center of the kiln and the inner surface of its wall, is a series of symmetricallyarranged permanent outletpassages d, which lead downward into an annular flue I-I beneath the floor. A horizontal passage 71. leads from said flue to the valvechamber Z of an ordinary reversing-valve L, which chamber communicates on each side with a pair of regenerator-passages P P, which may be filled with fire-brick p or any other material adapted to regenerative purposes, said passages being preferably arranged circumferentially, as shown, with reduced portions I 1', respectively leading to the chamber m of a second reversing-valve M, which communicates on the one hand with an airinlet Q and on the other with a chimney N. These reversing-valves may be of any ordinary construction, and of course are adapted to alternate the outflow of the products of combustion and inflow of air-through the regenerators. The valve L also controls communication between the regenerators and the horizontal air-passage K, which leads inward to a central point beneath the kiln, and there rises vertically, as indicated at F, nearly to the level of the floor 0.
From the upper portion of the passage F a series of radial passages f lead through the kiln-floor to discharge-jets c, circumferentially arranged around the inner surface of the kiln and wall. I prefer to form said jets e in each side of the upwardly-projecting pieces of brick-work E, rising a short dis tance above the floor, so as to give a better distribution of the heat, the central portion of said brick-work being occupied by the gasinlet jets 1), whose arrangement will now be described.
The main inlet for gas is indicated by the dotted lines at T, (see Fig. 1,) and communicates with an annular flue J, arranged around the outer periphery of the kiln-wall, from which flue J inwardly-projecting passages g lead to the jets b, above referred to as being formed in the central part of the brick-work E. Branch passages 12, of considerably smaller transverse area than the passages I), lead from the ends of the passages g through the floor of the kiln to a central discharge-orifice S in said floor, immediately above the vertical air-passage F. A series of small vertical air-ducts a rise from the top of the passage f through the floor of the kiln, and are symmetrically disposed around the central gas-orifice S, so as to distribute the air necessary for proper combustion throughout the gas which issues from said opening.
The operation of the apparatus is as follows: Gas admitted at the inlet 'I flows into the annular passage J, and thence into the circumferential jets b and central orifice S. The products of combustion pass. out through the openings (1, and thence to one of the regenerators P or P. Assuming the other regenerator to have been previously heated by the outgoing products of combustion, the air admitted at Q passes through said regenerator, and thence, after becoming heated to the proper degree, flows through thepassages K,
F, and f into the jets e, arranged on each side of the circumferential gas-jets b. A small portion of said air also rises through the passages 0, around the central gas-orifice S.
The operation of the device is continuous, the proper reversal of the currents being of course effected by the reversing-valves L M, and the direction of the currents Within the kiln proper being constant. The arrangement of the outlets for products of combustion at points intermediate between the central and circumferential air and gas inlets gives the best possible distribution of heatin a uniform manner throughout the kiln. It desired, the gas can also be heated by the regenerative system, it being only necessary to divide the regenerator passages longitudinally so as to permit the separate heating of air and gas, and to provide controlling-valves at the points of communication between the gas-inlets and regenerators. I do not deem it necessary, however, to describe such modification in detail, as it will be readily understood.
I claim- The combination, in a kiln, of an annular gas-passage around the same provided with a main gas-inlet, a series of gas-inlet jets communicating with the said passage and arranged circumferentially within the kiln, a centralorifice in the kiln-floor, a series of converging branch passages leading through the kiln-floor from said jets to said orifice, a series of air-inlet jets circumferentially arranged within the kiln, a central air-passage, a series of radial passages leading through the kiln-floor from the central passage to the air-inlet jets, air-ducts leading from said central passage to the central orifice, a series of permanent outlet-passages for products of combustion arranged in the kiln-floor intermediate between the center and circumference thereof, a chimney, a pairof regenerators communicating with said central air-passage, said outlet-passages, and said chimney, and a pair of reversing-valves controlling such communication, substantially as set forth.
FRANK O. ROBERTS. Witnesses;
W. H. B. TEAMER, THEo. TOPLIN.
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