WO2005092583A1 - Swinging agitator for a gypsum calcining apparatus and the like - Google Patents

Swinging agitator for a gypsum calcining apparatus and the like Download PDF

Info

Publication number
WO2005092583A1
WO2005092583A1 PCT/US2005/004796 US2005004796W WO2005092583A1 WO 2005092583 A1 WO2005092583 A1 WO 2005092583A1 US 2005004796 W US2005004796 W US 2005004796W WO 2005092583 A1 WO2005092583 A1 WO 2005092583A1
Authority
WO
WIPO (PCT)
Prior art keywords
housing
gypsum
agitator frame
agitation mechanism
section
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.)
Ceased
Application number
PCT/US2005/004796
Other languages
French (fr)
Other versions
WO2005092583A8 (en
Inventor
Michael L. Bolind
Michael J. Porter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
United States Gypsum Co
Original Assignee
United States Gypsum Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from US10/788,871 external-priority patent/US7175426B2/en
Priority claimed from US10/788,864 external-priority patent/US7121713B2/en
Priority to NZ548798A priority Critical patent/NZ548798A/en
Priority to EP05713604.6A priority patent/EP1718445B1/en
Priority to AU2005225374A priority patent/AU2005225374B2/en
Priority to DK05713604.6T priority patent/DK1718445T3/en
Priority to CA2554983A priority patent/CA2554983C/en
Priority to ES05713604.6T priority patent/ES2619123T3/en
Application filed by United States Gypsum Co filed Critical United States Gypsum Co
Priority to CN2005800060463A priority patent/CN1925958B/en
Priority to JP2007500874A priority patent/JP4848357B2/en
Priority to BRPI0507697A priority patent/BRPI0507697B1/en
Publication of WO2005092583A1 publication Critical patent/WO2005092583A1/en
Priority to IL177176A priority patent/IL177176A/en
Anticipated expiration legal-status Critical
Priority to NO20064371A priority patent/NO338738B1/en
Publication of WO2005092583A8 publication Critical patent/WO2005092583A8/en
Ceased legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B11/00—Calcium sulfate cements
    • C04B11/02—Methods and apparatus for dehydrating gypsum
    • C04B11/028—Devices therefor characterised by the type of calcining devices used therefor or by the type of hemihydrate obtained
    • C04B11/0281—Kettles; Marmites; Autoclaves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
    • B28C5/08—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions using driven mechanical means affecting the mixing
    • B28C5/10—Mixing in containers not actuated to effect the mixing
    • B28C5/12—Mixing in containers not actuated to effect the mixing with stirrers sweeping through the materials, e.g. with incorporated feeding or discharging means or with oscillating stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/44—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement
    • B01F31/441—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement performing a rectilinear reciprocating movement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90—Heating or cooling systems
    • B01F35/93—Heating or cooling systems arranged inside the receptacle
    • 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
    • B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
    • B01J6/001—Calcining
    • B01J6/004—Calcining using hot gas streams in which the material is moved
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B28—WORKING CEMENT, CLAY, OR STONE
    • B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
    • B28C5/46—Arrangements for applying super- or sub-atmospheric pressure during mixing; Arrangements for cooling or heating during mixing, e.g. by introducing vapour
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00—Compounds of calcium, strontium, or barium
    • C01F11/46—Sulfates
    • C—CHEMISTRY; METALLURGY
    • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B11/00—Calcium sulfate cements
    • C04B11/02—Methods and apparatus for dehydrating gypsum
    • C04B11/028—Devices therefor characterised by the type of calcining devices used therefor or by the type of hemihydrate obtained
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
    • F26B3/084—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed with heat exchange taking place in the fluidised bed, e.g. combined direct and indirect heat exchange
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
    • F26B3/092—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed agitating the fluidised bed, e.g. by vibrating or pulsating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B3/00—Drying solid materials or objects by processes involving the application of heat
    • F26B3/02—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air
    • F26B3/06—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried
    • F26B3/08—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed
    • F26B3/092—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed agitating the fluidised bed, e.g. by vibrating or pulsating
    • F26B3/0923—Drying solid materials or objects by processes involving the application of heat by convection, i.e. heat being conveyed from a heat source to the materials or objects to be dried by a gas or vapour, e.g. air the gas or vapour flowing through the materials or objects to be dried so as to loosen them, e.g. to form a fluidised bed agitating the fluidised bed, e.g. by vibrating or pulsating by mechanical means, e.g. vibrated plate, stirrer
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories or equipment specially adapted for furnaces of these types
    • F27B15/08—Arrangements of devices for charging
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories or equipment specially adapted for furnaces of these types
    • F27B15/09—Arrangements of devices for discharging
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories or equipment specially adapted for furnaces of these types
    • F27B15/10—Arrangements of air or gas supply devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories or equipment specially adapted for furnaces of these types
    • F27B15/14—Arrangements of heating devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D99/00—Subject matter not provided for in other groups of this subclass
    • F27D99/0001—Heating elements or systems
    • F27D99/0033—Heating elements or systems using burners
    • F27D99/0035—Heating indirectly through a radiant surface
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/28—Mixing cement, mortar, clay, plaster or concrete ingredients
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00—Physical properties of inorganic compounds
    • C01P2006/80—Compositional purity
    • C01P2006/82—Compositional purity water content

Definitions

  • Fig.4 is the apparatus of Fig. 1 showing a plurality of access panels attached thereto;
  • Fig. 5 is the apparatus of Fig. 1 with the burner conduit in an uninstalled position;
  • Fig. 6 is a perspective view of the calcining apparatus of Fig. 1 showing the heated gas flow path with arrows;
  • FIG. 7 is a perspective view of a second embodiment of the invention, wherein the agitation mechanism is positioned within a water spray fluid bed stucco cooler;
  • Fig. 8 is a perspective view of a third embodiment of the invention, wherein the agitation mechanism is positioned within a cooling coil fluid bed stucco cooler;
  • Fig. 9 is a perspective view of a fourth embodiment of the invention, wherein the agitation mechanism is positioned within a post stucco treatment device.
  • a housing 12 includes a bottom wall 14, an open top 16, and a plurality of side walls 18 extending between the bottom wall 14 and the open top 16.
  • An inlet fixture 20 is located on the housing 12 for receiving crushed or synthetic raw gypsum from a source (not shown) and for transferring the gypsum into the housing 12.
  • At least one burner 22 is connected to the housing 12.
  • the burner 22 is operable for combusting an air-fuel mixture supplied by a forced air conduit 24 and a fuel conduit 26.
  • the burner 22 can be any type known to those skilled in the art, but will typically burn a hydrocarbon based fuel.
  • the heated exhaust from the burner 22 will flow through at least one serpentine shaped burner conduit 28 that extends through a gypsum support floor 23 adjacent the bottom wall 14 of the housing 12.
  • the hot exhaust flow from the burner 22 is utilized to heat the gypsum material to approximately 300°F.
  • the agitation mechanism 62 includes an agitator frame 64 having a pair of side beams 65.
  • the agitator frame 64 has a plurality of agitation members 66 connected to the agitator frame 64 for agitating the gypsum product adjacent the fluidization pad 54 along the support floor 23.
  • the agitation members 66 can take the form of a cross bar pattern.
  • the agitation mechanism 62 locally chums the heated gypsum product when the agitator frame 64 is set into motion.
  • At least one pivotal support arm 68 pivotally connects the agitation frame 64 to the housing 12 (shown in Fig. 1).
  • connection to the housing 12 can be formed with an angle plate 70 affixed to the housing 12 in a suitable manner such as by welding or mechanically fastening, etc.
  • the support arm 68 can be secured to the angle plate 70 via a threaded fastener 72 or the like.
  • the pivotal support arm 68 is most preferably a cable or similar structure to more easily facilitate a swinging motion by the agitator frame 64 about a common pivot axis when motion is imparted to the agitator frame 64.
  • Alternate moving patterns by the agitator frame 64 are contemplated by the present invention. For example, one skilled in the art would readily understand how to impart motion to the agitator frame 64 in a vertical, horizontal, or arcute pattern, or any combination thereof.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Ceramic Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Structural Engineering (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Microbiology (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Processing Of Solid Wastes (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Accessories For Mixers (AREA)
  • Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
  • Compounds Of Unknown Constitution (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)
  • Sampling And Sample Adjustment (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)

Abstract

An agitation mechanism for a gypsum processing apparatus which includes a housing (12) having a top wall, a bottom wall, and at least one side wall. The housing can be constructed and arranged to receive and process gypsum-based products. An agitator frame (64) having a similarly shaped cross-section to the cross-section of the housing is provided and positioned adjacent the bottom wall (55) of the housing. The agitator frame (64)is pivotally connected (68, 70, 72) internally to the housing for reciprocating movement between first and second positions. The agitation mechanism is operable (74) for preventing fluid channeling to ensure good fluidization of the gypsum products from collecting adjacent the bottom wall of the housing.

Description

SWINGING AGITATOR FOR A GYPSUM CALCINING APPARATUS AND THE LIKE
The present invention relates to a method and apparatus for agitating gypsum product.
BACKGROUND OF THE INVENTION Calcining of gypsum comprises converting calcium sulfate dihydrate by heating into calcium sulfate hemihydrate, better known as stucco. Prior calcining apparatus and methods have taken various forms. Traditionally, the calcining of gypsum has occurred in a large kettle, having a thickened dome-shaped bottom, against which a gas-fired flame is directed, with the kettle and burner flame being enclosed in a suitable refractory structure. There is usually an associated hot pit into which the calcined material is fed. The kettle must withstand temperatures in the 2,000° -2,400°F range, hence requiring expensive fire box steel plate on its domed bottom, which was typically 13/4 inches thick. U.S. Pat. No. 3,236,509 typifies this type construction. This approach had numerous disadvantages, such as the extreme waste of hot burner gases, and the associated refractory brick enclosure which, when repairs or kettle shut-down were needed, first required a lengthy cool-down period. After the gypsum has been calcined, further processing is sometimes required. The calcined gypsum, or stucco, can be placed in a fluid bed stucco cooling apparatus wherein water is sprayed into the apparatus to cool the stucco to a predetermined temperature. In addition, other types of stucco processing apparatus are known such as a cooling coil fluid bed stucco treaters where the stucco is cooled with a cooling coil that is positioned within the apparatus to control the temperature of the stucco. Other processing apparatus such as post-stucco treatment retention devices can be used in the manufacture of gypsum-based products.
SUMMARY OF THE INVENTION The present invention provides for an agitation mechanism for a gypsum processing apparatus which includes a housing having a top wall, a bottom wall, and at least one side wall. The housing can be constructed and arranged to receive and process gypsum-based products. A fluidization mechanism can be provided for delivering fluid to the gypsum-based products. An agitator frame having a similarly shaped cross-section to the cross-section of the housing is provided and positioned adjacent the bottom wall of the housing. The agitator frame is pivotally connected internally to the housing for reciprocating movement between first and second positions. The agitation mechanism is operable for preventing channeling of the fluid through the gypsum, ensuring good fluidization, and preventing gypsum product from collecting adjacent the bottom wall of the housing. The agitation mechanism can include a plurality of agitation members connected to the frame for agitating the gypsum product adjacent the bottom wall when the agitator frame moves. The agitation mechanism can also include at least one pivotal support arm for pivotally connecting the frame to the apparatus. The agitation mechanism can be used in a fluidized stucco cooler utilizing water injection. The agitation mechanism can be used in a fluidized bed stucco cooler utilizing cooling coils. Further, the agitation mechanism can also be used in a post-stucco treatment retention device. A method is provided for agitating gypsum based material in a processing housing. The gypsum based material is delivered to the housing, and an agitation mechanism having a frame with agitation members attached thereto is positioned adjacent the bottom wall of the housing. The agitation mechanism is moved between first and second positions to agitate the fluidized material in the housing to prevent material from coagulating near the bottom of the housing and to prevent fluid channeling and dead zones of non fluidized gypsum. Other applications of the present invention will become apparent to those skilled in the art when the following description of the best mode contemplated for practicing the invention is read in conjunction with the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
Fig. 1 is a perspective view of a high-efficiency calcining apparatus; Fig. 2 is a perspective view of fluidization pad partially cut-away to show the layers; Fig. 3 is a perspective view of an agitation mechanism;
Fig.4 is the apparatus of Fig. 1 showing a plurality of access panels attached thereto; Fig. 5 is the apparatus of Fig. 1 with the burner conduit in an uninstalled position; Fig. 6 is a perspective view of the calcining apparatus of Fig. 1 showing the heated gas flow path with arrows;
Fig. 7 is a perspective view of a second embodiment of the invention, wherein the agitation mechanism is positioned within a water spray fluid bed stucco cooler; Fig. 8 is a perspective view of a third embodiment of the invention, wherein the agitation mechanism is positioned within a cooling coil fluid bed stucco cooler; and Fig. 9 is a perspective view of a fourth embodiment of the invention, wherein the agitation mechanism is positioned within a post stucco treatment device. DETAILED DESCRIPTION OF THE INVENTION Referring to Fig. 1, an apparatus 10 for calcining gypsum is shown therein. A housing 12 includes a bottom wall 14, an open top 16, and a plurality of side walls 18 extending between the bottom wall 14 and the open top 16. An inlet fixture 20 is located on the housing 12 for receiving crushed or synthetic raw gypsum from a source (not shown) and for transferring the gypsum into the housing 12. At least one burner 22 is connected to the housing 12. The burner 22 is operable for combusting an air-fuel mixture supplied by a forced air conduit 24 and a fuel conduit 26. The burner 22 can be any type known to those skilled in the art, but will typically burn a hydrocarbon based fuel. The heated exhaust from the burner 22 will flow through at least one serpentine shaped burner conduit 28 that extends through a gypsum support floor 23 adjacent the bottom wall 14 of the housing 12. The hot exhaust flow from the burner 22 is utilized to heat the gypsum material to approximately 300°F. In known manner, the heating process converts the gypsum into calcium sulfate hemihydrate, or stucco. Alternatively, the heating process can simply heat wet synthetic gypsum to a desired temperature, typically below 300°F in order to dry excess moisture from the wet synthetic gypsum for subsequent calcination in a separate process. Alternatively, the heating process can perform the drying and calcination processes in the same vessel. The burner conduit 28 advantageously includes an elongate linear portion 30 extending away from the burner 22. The linear portion increases the life span of the burner conduit 28. That is, if the flames from the burner 22 were to directly impinge the burner conduit 28 along a curved or angled portion, the flames would overheat the side wall of the conduit causing high stress which shortens the life of the conduit 28. However, due to the presence of the initial elongated linear burner section 30 (which can extend some fifteen to twenty feet in a commercial installation), the burner flames do not directly impinge on the burner conduit, and this is because the flames have converted, along the length of section 30, to hot exhaust gases. Importantly, the burner conduit 28 includes a plurality of curved sections 32 to connect the linear portions 30, 31, and 33, provide the serpentine shape. The burner conduit 28 may include at least one reduced diameter section 34 to provide increased exhaust flow velocity to thereby enhance the heat transfer effectiveness of the conduit 28. The temperature of the exhaust cools proportionally to the distance it moves away from the burner 22, therefore the velocity may be increased to maintain a suitable heat transfer rate. The burner conduit 28 can also include a multi-conduit portion 36 wherein a plurality of relatively smaller diameter conduits 38 are formed to be in fluid communication with relatively larger single conduit portions 32. The smaller diameter conduits 38 provide more surface area for a given effective flow area and thus increase the heat transfer relative to the larger conduit 32. The multi-conduit portions 36 can be connected to the single conduit portions 32 through various means known to those skilled in the art such as welding, brazing, and press fit, mechanical fasteners, etc. The burner conduit 28 can be attached to the burner 22 via a flange 40 with a plurality of threaded fasteners 42. The burner conduit 28 likewise can be attached at the discharge end 44 to an outlet conduit 46 that extends through the support floor 23. The burner conduit 28 can be attached to the outlet conduit 46 via a flange 48 with a plurality of threaded fasteners 50. A fluidization base 52, shown in Figs. 1, 2, 4 and 6, (best seen in Fig. 2) can be positioned in a lower portion of the housing 12 to receive exhaust flow from the burner conduit 28. The fluidization base 52 has a plurality of sidewalls 53 extending upwardly from a bottom 55. The fluidization base 52 can have a fluidization pad 54 positioned above the bottom 55 of the fluidization base 52. The fluidization pad 54 forms at least a portion of the support floor 23 of the housing 12. The fluidization pad 54 is operable for containing the gypsum product along the lower portions of housing 12, and for evenly distributing the exhaust flow as it passes from the fluidization base 52 directly into the gypsum. The fluidization base 52 delivers the aeration, the agitation ensures good fluidization especially of cohesive powders that will not otherwise fluidize. The fluidization pad 54 includes first and second outer perforated plates 56, 58. The plates 56, 58 include a plurality of through apertures 57 that permit the exhaust flow to pass therethrough. A bore hole 59 is formed in the fluidization pad 54 to provide access for the conduit 46 (see Fig. 1) to pass through and deliver the exhaust flow to the fluidization base 52. At least one intermediate porous layer 60, formed of a porous fiber mat or woven stainless steel media, is positioned between the outer plates 56, 58. The intermediate layer 60 of media can be made from compressed silica fiber, woven stainless steel mesh or similar materials suitable for fluidization as known to those skilled in the art to withstand high exhaust gas temperatures. The perforated plates 56, 58 are most preferably made from a metal such as stainless steel or the like. The fluidization pad 54 operates by allowing diffused exhaust gas to bubble out through the generally evenly spaced apertures 57 of perforated plate 56. One advantage to using woven stainless steel media 60 is that the perforated plates 56, 58 are not required except to provide support and protection for the media from punctures. An agitation mechanism 62, shown in Figs. 1, 3, 4, 6, 7, 8, and 9 (best seen in Fig. 3), can be positioned just above the fluidization pad 54. The agitation mechanism 62 includes an agitator frame 64 having a pair of side beams 65. The agitator frame 64 has a plurality of agitation members 66 connected to the agitator frame 64 for agitating the gypsum product adjacent the fluidization pad 54 along the support floor 23. In one embodiment, the agitation members 66 can take the form of a cross bar pattern. The agitation mechanism 62 locally chums the heated gypsum product when the agitator frame 64 is set into motion. At least one pivotal support arm 68 pivotally connects the agitation frame 64 to the housing 12 (shown in Fig. 1). The connection to the housing 12 can be formed with an angle plate 70 affixed to the housing 12 in a suitable manner such as by welding or mechanically fastening, etc. The support arm 68 can be secured to the angle plate 70 via a threaded fastener 72 or the like. The pivotal support arm 68 is most preferably a cable or similar structure to more easily facilitate a swinging motion by the agitator frame 64 about a common pivot axis when motion is imparted to the agitator frame 64. Alternate moving patterns by the agitator frame 64 are contemplated by the present invention. For example, one skilled in the art would readily understand how to impart motion to the agitator frame 64 in a vertical, horizontal, or arcute pattern, or any combination thereof. An actuation power source, such as an electric motor or pneumatic air cylinder 74, can be connected to the agitator frame 64 through an actuator arm 76. An expandable seal 78 is engaged with the actuator arm 76 and the housing 12 (not shown in Fig. 2) to prevent gypsum product from leaking out of the housing 12 about the actuator arm. The seal 78 expands and contracts as the actuator arm 76 moves between first and second positions as the agitator frame 64 swings. Alternatively, the actuator arm 76 can be connected to mechanically leveraged linkages (not shown) that can extend from an actuation power source (not shown) positioned at the top of the housing 12 down to the agitator frame 64 as is known to those skilled in the art. The seal 78 can be made from any suitable material that can withstand temperatures greater than 300 degrees Fahrenheit and pressures up to 10 psig (pounds per square inch gage). Referring again to Fig. 1, an overflow tube 80 is fluidically connected to the housing 12 to allow processed gypsum to egress from the housing 12 into the overflow tube 80. An overflow valve 82 is associated with the overflow tube 80 to prevent gypsum from egressing from the housing 12 prior to being heated to a predetermined condition. A dump port 84 includes a dump valve 86 that permits the selective draining of the contents in the housing 12. The valves 82, 86 can be of any type known to those skilled in the art, but are most preferably electrically or pneumatically actuated. Referring now to Fig. 4, a conduit support 88 is slidingly connected to the housing 12 for supporting the burner conduit 28 during installation. The support 88 is operable for sliding between an outer position at least partially external to the housing 12 (shown in Fig. 4) and the installed position inside the housing 12. The conduit support 88 holds the conduit during installation and removal from the housing 12. The support 88 includes a pair of side rails 90, 92 slidingly connected to slide elements 91 formed on parallel walls 18 of the housing 12. A plurality of cross-bars 94 extend between the side rails 90, 92 to provide support surfaces for the burner conduit 28 to rest thereon. The housing 12 includes a side panel 96 operable to open when installing the burner conduit 28. A plurality of ties 97 structurally connects the side walls 18 of the housing 12 to one another to prevent outward bowing of the walls 18 when the housing 12 is filled with gypsum. The ties 97 can be welded or otherwise affixed by any means that is conventional. Referring now to Fig. 5, the apparatus 10 includes access panels 98 located on the side of the housing 12 for permitting servicing of the internal components, such as the burner 22 and the conduit 28, etc. A disengagement chamber 100 is positioned above the open top 16 of the housing 12 and is constructed to permit access thereto for servicing internal components of the housing 12. A dust collector 102 can be positioned above the disengagement chamber 100 to collect gypsum dust particles and recycle the particles back into the housing 12 for calcining. The dust collector 102 can include a plurality of replaceable filters 104. The filters 104 can be of any desired type such as round cartridge filters, bag filters, or the like. The filters 104 can be periodically cleaned by intermittently injecting air through an opposite side of where the dust is collected or by shaking as is known to those skilled in the art. An exhaust stack 106 permits the exhaust to be removed from the apparatus 10 after the gypsum dust particles have been removed by the filters 104. In operation, gypsum powder is fed into an inlet fixture 20 to fill the housing 12. Air and fuel are supplied by the conduits 24, 26 respectively, to the burner 22. The burner 22 combusts the air-fuel mixture and provides hot exhaust gases which flow in the direction of the arrows shown in Fig. 6. The exhaust flows through the serpentine burner conduit 28 into the fluidization base 52. From the fluidization base 52, the exhaust flows horizontally and then upwardly through the fluidization pad 54 positioned above the base 52. The fluidization pad 54 distributes the exhaust gases through the gypsum product so that the heated exhaust gases are evenly distributed therethrough. The outer surface of the burner conduit 28 provides heat to the gypsum through conduction heat transfer. Thus, the gypsum product is heated both when the exhaust gas flows through the burner conduit 28 and through the gypsum after traveling through the fluidization pad 54. The present invention provides for increased fuel efficiency over the prior art because the dual heating method removes the maximum amount of heat from the exhaust and transfers it into the gypsum. Exhaust gas continues to flow upwardly through the disengagement chamber 100 permitting some of the gypsum particles to separate from the exhaust flow and fall back into the housing 12. The dust collector 102 cleans the airborne gypsum particles from the exhaust gas before exhaust gas egresses through the exhaust stack 106. The gypsum particles can periodically be knocked from the collector filter cartridges (or bags) back into the bed of gypsum. Advantageously, an agitation mechanism 62 is provided to ensure good fluidization by preventing exhaust from channeling directly through gypsum powder. Natural gypsum typically includes a fine powder that may be too cohesive to achieve good fluidization without agitation. The agitation mechanism 62 is operated by swinging between first and second positions to locally mix the gypsum and scrape it away from the fluidized pad 54. The calcining apparatus 10 has a high efficiency because substantially all of the heat produced by the burner 22 is utilized in heating the gypsum and is not lost through the exhaust process. The temperature of the exhaust gas leaving the gypsum product is approximately 300°F, which is the approximate temperature required for the gypsum to be processed into stucco.
Synthetic gypsum that is manufactured with a standard particle size may not require agitation to ensure good fluidization. Referring now to Fig. 7, a water spray fluid bed stucco treater 110 for cooling stucco is shown therein. Hot stucco can enter the water spray treater 110 through an inlet 118. Cooled stucco and fluidization gas can exit through an outlet 119. The water spray stucco treater 110 includes an agitation mechanism 62 having an agitator frame 64. The agitation mechanism 62 includes an agitator frame 64 having a pair of side beams 65. The agitator frame 64 has a plurality of agitation members 66, in the form of cross bar pattern, connected to the frame 64 for agitating the gypsum product adjacent the support base 23. The agitation mechanism 62 locally chums the gypsum product when the frame 64 is set into motion. At least one pivotal support arm 68 pivotally connects the agitation frame 64 to the stucco treater apparatus 110. The connections to the apparatus 110 can be formed with an angle plate 70 affixed to the housing in a suitable manner such as by welding or mechanically fastening, etc. The support arm 68 can be secured to the angle plate 70 via a threaded fastener 72 or the like. The pivotal support arm 68 is most preferably a cable or similar structure to more easily facilitate a swinging motion by the frame 64 about a common pivot axis when motion is imparted to the agitator frame 64. A power source, such as an electric motor 74, can be connected to the agitator frame 64 through an actuator arm 76. The electric motor 74 can be utilized to swing the agitation mechanism 62 about a pivot axis, to agitate the stucco and prevent channeling of the fluidization gases, dead zones, andbuild-up any where in the fluidized bed, especiallyalong the bottom portion of the apparatus 110. A blower (not shown) injects fluid, such as air, or the likethrough an inlet 116 formed on the stucco treater 110 to create a fluidized bed of stucco toprevent the stucco from hardening and coagulating adjacent the fluidization pad 54 of the water spray cooler apparatus 110. The apparatus 110 can also include a fluidization base 52 as described above.The water spray cooler 110 includes a water manifold 112 for delivering water to a plurality of spray nozzles 114. The spray nozzles 114 are operable for spraying water into the apparatus 110 and thus cooling the stucco to a predetermined temperature. Referring now to Fig. 8, a cooling coil fluid bed stucco cooler 120 is shown therein. Hot stucco can enter the water spray treater 110 through an inlet 118. Cooled stucco and fluidization gas can exit through an outlet 119. The cooling coil stucco treater 120 includes an agitation mechanism 62 having an agitator frame 64. The agitation mechanism 62 includes an agitator frame 64 having a pair of side beams 65. The agitator frame 64 has a plurality of agitation members 66 connected to the frame 64 for agitating the gypsum product adjacent the support base 23. The agitation mechanism 62 locally churns the gypsum product when the frame 64 is set into motion. At least one pivotal support arm 68 pivotally connects the agitation frame 64 to the stucco treater apparatus 120. The connections to the apparatus 120 can be formed with an angle plate 70 affixed to the housing in a suitable manner such as by welding or mechanically fastening, etc. The support arm 68 can be secured to the angle plate 70 via a threaded fastener 72 or the like. The pivotal support arm 68 is most preferably a cable or similar structure to more easily facilitate a swinging motion by the frame 64 about a common pivot axis when motion is imparted to the frame 64. A power source, such as an electric motor 74, can be connected to the frame 64 through an actuator arm 76. The electric motor 74 can be utilized to swing the agitation mechanism 62 about a pivot axis, to agitate the stucco and prevent build-up along the bottom portion of the apparatus 120. A blower (not shown) injects fluid, such as air, through an inlet 128 formed on the stucco treater 120 to create a fluidized bed of stucco and the agitation mechanism 62 preventsthe stucco from coagulating adjacent the fluidization pad 54 of the cooling coil stucco treater 120. The apparatus 110 can also include a fluidization base 52 as described above.The cooling coil stucco treater 120 includes a serpentine-like cooling coil 122 designed to transport a suitable cooling fluid such as ethylene glycol, chilled water,orthe like through the stucco. The cooling coil 122 includes a coolant inlet 124 in which the coolant enters from a supply source (not shown). The coolant follows the serpentine coil 122 and exits from a coolant outlet 126. The coolant traverses the cooling coil 122 to cool the stucco to a predetermined temperature. Referring now to Fig. 9, a post stucco treatment retention device 130 is shown therein. Stucco can enter the water spray treater 110 through an inlet 118. Stucco and fluidization gas can exit through an outlet 119. The post stucco treatment retention device 130 includes an agitation mechanism 62 having an agitator frame 64 encompassing a plurality of agitation members 66. The agitation members 66 are connected to the frame 64 and are operable for agitating the gypsum product adjacent the support base 23. The agitation mechanism 62 locally churns the gypsum product when the frame 64 is set into motion. At least one pivotal support arm 68 pivotally connects the agitation frame 64 to the stucco retention apparatus 130. The connections to the apparatus 130 can be formed with an angle plate 70 affixed to the housing in a suitable manner such as by welding or mechanically fastening, etc. The support arm 68 can be secured to the angle plate 70 via a threaded fastener 72 or the like. The pivotal support arm 68 is most preferably a cable or similar structure to more easily facilitate a swinging motion by the frame 64 about a pivot axis when motion is imparted to the frame 64. A power source, such as an electric motor 74, can be connected to the frame 64 through an actuator arm 76. The electric motor 74 can be utilized to swing the agitation mechanism 62 about a pivot axis, to agitate the stucco and prevent build-up along the bottom portion of the apparatus 130. In the illustrative embodiment, the post stucco treatment retention device 130 is shown as having a round cross section, however, various cross sectional geometries can be used with the agitation mechanism 62. The post stucco treatment retention device 130 typically will include a blower (not shown) to provide fluid, such as pressurized air, through an inlet 132 formed on the retention device 130. While the preceding text sets forth a detailed description of numerous different embodiments of the invention, it should be understood that the legal scope of the invention is defined by the words of the claims set forth at the end of this patent. The detailed description is to be construed as exemplary only and does not describe every possible embodiment of the invention since describing every possible embodiment would be impractical, if not impossible. Numerous alternative embodiments could be implemented, using either current technology or technology developed after the filing date of this patent, which would still fall within the scope of the claims defining the invention.

Claims

What is claimed is: 1. An agitation mechanism for a gypsum processing apparatus comprising: a housing having a top wall, a bottom wall, and at least one sidewall, the housing constructed and arranged to receive and process powdered gypsum; a fluidization mechanism for delivering fluid to the gypsum based product, and an agitator frame having a similarly shaped cross section to a cross section of the housing, the agitator fame pivotally connected internally to the housing for reciprocating movement between first and second positions, the agitation mechanism operable for preventing the fluidized gypsum product from collecting along a support base adjacent the bottom wall of the housing.
2. The apparatus of claim 1, wherein the agitation mechanism includes a plurality of agitation members connected to the agitator frame for agitating the gypsum product adjacent the support base when the agitator frame moves.
3. The apparatus of claim 1, wherein the reciprocating movement is a swinging movement.
4. The apparatus of claim 1, wherein the agitation mechanism includes at least one pivotable support arm for pivotally connecting the agitator frame to the apparatus.
5. The apparatus of claim 4, wherein the at least one pivotable support arm is a cable pivotally attached internally to the housing at one end and to the agitator frame at the other end, the agitator frame being operable for swinging about a pivot axis when motion is imparted thereto.
6. The apparatus of claim 1, wherein the agitation mechanism includes a power source to move the agitator frame.
7. The apparatus of claim 6, wherein the power source includes one of an electric motor and a powered air cylinder.
8. The apparatus of claim 7, further comprising: an actuator arm extending through the housing to provide a connection between the motor and the agitator frame.
9. The apparatus of claim 8, wherein the agitator mechanism further comprises: an expandable seal engaged with the actuator arm and the housing to prevent the gypsum product from leaking from the housing.
10. The apparatus of claim 9, wherein the seal expands and contracts as the actuator arm moves between first and second positions.
11. The apparatus of claim 8, wherein the actuator arm slidingly engages through a side wall of the housing to connect the agitation mechanism to the motor.
12. The apparatus of claim 1, wherein the agitator frame corresponds to a housing having a rectangular cross section.
13. The apparatus of claim 1 , wherein the agitator frame corresponds to a housing having a circular cross section.
14. The apparatus of claim 1, wherein the agitator frame corresponds to a housing having one of any geometric cross section constructed and arranged to process a gypsum based product.
15. The apparatus of claim 1, wherein the process includes calcining gypsum.
16. The apparatus of claim 1, wherein the apparatus is a fluidized bed stucco cooler utilizing water injection.
17. The apparatus of claim 1, wherein the apparatus is a fluidized bed stucco cooler utilizing cooling coils.
18. The apparatus of claim 1, wherein the apparatus is a post stucco treatment retention device.
19. An agitation mechanism for a fluidized gypsum processing apparatus comprising: a housing having a top wall, a bottom wall, and at least one sidewall , the housing constructed and arranged to receive and process gypsum based products; an agitator frame having a cross section of generally similar shape to a cross section of the housing, the agitator frame pivotally connected internally to the housing for reciprocating movement between first and second positions, the agitation mechanism operable for preventing fluid channeling, dead pockets of non fluidized gypsum, and for preventing the gypsum product from collecting adjacent the bottom wall of the housing; and at least one pivotable support arm for pivotally connecting the agitator frame to the apparatus, wherein the at least one pivotable support arm is a cable pivotally attached internally to the housing at one end and to the frame at the other end, the agitator frame being operable for swinging about a pivot axis when motion is imparted thereto.
20. The apparatus of claim 1 , wherein the agitation mechanism includes a plurality of agitation members connected to the agitator frame for agitating the gypsum product adjacent the bottom wall when the agitator frame moves.
21. The apparatus of claim 20, wherein the agitation members comprise cross members.
22. The apparatus of claim 19, wherein the agitation mechanism includes a power source to move the agitator frame.
23. The apparatus of claim 22, wherein the power source includes one of an electric motor and a pneumatic actuator.
24. The apparatus of claim 22, further comprising: an actuator arm extending through the housing to provide a connection between the power source and the agitator frame.
25. The apparatus of claim 24, wherein the actuator arm includes a plurality of mechanical linkages to connect the agitation mechanism to the power source.
26. The apparatus of claim 24, wherein the agitation mechanism further comprises: an expandable seal engaged with the actuator arm and the housing to prevent the gypsum product from leaking from the housing.
27. The apparatus of claim 26, wherein the seal expands and contracts as the actuator arm moves between first and second positions.
28. The apparatus of claim 19, wherein a cross-section of the agitator frame corresponds to a housing having a rectangular cross section.
29. The apparatus of claim 19, wherein a cross-section of the agitator frame corresponds to a housing having a circular cross section.
30. The apparatus of claim 19, wherein a cross-section of the agitator frame corresponds to a housing having one of any geometric cross section constructed and arranged to process a gypsum based product.
31. The apparatus of claim 19, wherein the process includes calcining gypsum.
32. The apparatus of claim 19, wherein the apparatus is a fluidized bed stucco cooler utilizing water injection.
33. The apparatus of claim 19, wherein the apparatus is a fluidized bed stucco cooler utilizing cooling coils.
34. The apparatus of claim 19, wherein the apparatus is a post stucco treatment retention device.
35. A method for agitating a gypsum based material comprising the steps of: providing a housing having a bottom wall for processing the gypsum material; transferring the material from a source to the apparatus; fluidizing the material by flowing fluid through the material; and agitating the fluidized material with an agitation mechanism that is movable between first and second positions adjacent the bottom wall.
36. The method of claim 35, further comprising: preventing the material from coagulating along the bottom wall of the housing.
37. The method of claim 35, wherein the agitating step further comprises: positioning an agitator frame having mixing members adjacent a fluidized medium; and moving the agitator frame along a predetermined path and frequency.
38. The method of claim 35, further comprising: removing any stagnant pockets of material.
PCT/US2005/004796 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like Ceased WO2005092583A1 (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
JP2007500874A JP4848357B2 (en) 2004-02-27 2005-02-10 Rocking stirrer for gypsum baking equipment
BRPI0507697A BRPI0507697B1 (en) 2004-02-27 2005-02-10 plaster processing apparatus and method for agitating a plaster-based material
CN2005800060463A CN1925958B (en) 2004-02-27 2005-02-10 Oscillating mixers for gypsum calcining plants and similar plants
AU2005225374A AU2005225374B2 (en) 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like
DK05713604.6T DK1718445T3 (en) 2004-02-27 2005-02-10 SWITCHING PLATE SWITCHING AGENT AND LIKE
CA2554983A CA2554983C (en) 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like
ES05713604.6T ES2619123T3 (en) 2004-02-27 2005-02-10 Rolling stirrer for a plaster calcination apparatus and the like
NZ548798A NZ548798A (en) 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like
EP05713604.6A EP1718445B1 (en) 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like
IL177176A IL177176A (en) 2004-02-27 2006-07-31 Swinging agitator for a gypsum calcining apparatus and the like
NO20064371A NO338738B1 (en) 2004-02-27 2006-09-27 Gipsbehandlingsanording

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US10/788,871 US7175426B2 (en) 2004-02-27 2004-02-27 High efficiency refractoryless kettle
US10/788,864 US7121713B2 (en) 2004-02-27 2004-02-27 Swinging agitator for a gypsum calcining apparatus and the like
US10/788,864 2004-02-27
US10/788,871 2004-02-27

Publications (2)

Publication Number Publication Date
WO2005092583A1 true WO2005092583A1 (en) 2005-10-06
WO2005092583A8 WO2005092583A8 (en) 2006-11-16

Family

ID=35056054

Family Applications (2)

Application Number Title Priority Date Filing Date
PCT/US2005/004796 Ceased WO2005092583A1 (en) 2004-02-27 2005-02-10 Swinging agitator for a gypsum calcining apparatus and the like
PCT/US2005/004797 Ceased WO2005091819A2 (en) 2004-02-27 2005-02-10 High efficiency refractoryless kettle

Family Applications After (1)

Application Number Title Priority Date Filing Date
PCT/US2005/004797 Ceased WO2005091819A2 (en) 2004-02-27 2005-02-10 High efficiency refractoryless kettle

Country Status (17)

Country Link
EP (2) EP1718576B1 (en)
JP (2) JP4926939B2 (en)
KR (2) KR20060135841A (en)
CN (2) CN1925958B (en)
AR (2) AR050319A1 (en)
AU (2) AU2005227119B2 (en)
BR (2) BRPI0507697B1 (en)
CA (2) CA2554983C (en)
DK (2) DK1718576T3 (en)
ES (2) ES2619123T3 (en)
IL (2) IL177176A (en)
MY (2) MY139186A (en)
NO (2) NO338738B1 (en)
NZ (2) NZ548946A (en)
PL (2) PL1718576T3 (en)
RU (2) RU2355570C2 (en)
WO (2) WO2005092583A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010500958A (en) * 2006-08-17 2010-01-14 ユナイテッド・ステイツ・ジプサム・カンパニー Rocking stirrer for gypsum baking equipment
US7718019B2 (en) 2005-04-27 2010-05-18 United States Gypsum Company Methods of and systems for preparing a heat resistant accelerant slurry and adding the accelerant slurry to a post-mixer aqueous dispersion of calcined gypsum
US8016960B2 (en) 2005-04-27 2011-09-13 United States Gypsum Company Methods of and systems for adding a high viscosity gypsum additive to a post-mixer aqueous dispersion of calcined gypsum

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2506227C2 (en) * 2008-02-19 2014-02-10 Юнайтед Стэйтс Джипсум Компани Method and device for calcination of gypsum under pressure
JP5909568B2 (en) * 2014-02-17 2016-04-26 月島機械株式会社 Fluidized bed equipment
WO2016136485A1 (en) * 2015-02-25 2016-09-01 吉野石膏株式会社 Apparatus and method for calcination of gypsum
WO2018030077A1 (en) * 2016-08-10 2018-02-15 吉野石膏株式会社 Apparatus and method for treating gypsum
EP3284723A1 (en) * 2016-08-17 2018-02-21 Claudius Peters Projects GmbH Two-stage calcination method, and plant for same
CN106315654A (en) * 2016-08-25 2017-01-11 广西联壮科技股份有限公司 Soaking device for calcined raw material for producing coarse barium
RU2719155C1 (en) * 2019-03-13 2020-04-17 Федеральное государственное бюджетное образовательное учреждение высшего образования "Тамбовский государственный технический университет" (ФГБОУ ВО "ТГТУ") Method of feeding liquid into a drier with boiling layer of inert bodies and apparatus for its implementation
KR20220011903A (en) 2020-07-22 2022-02-03 삼성전자주식회사 Dishwasher
CN111893292B (en) * 2020-07-31 2021-10-29 天能集团（河南）能源科技有限公司 Lead-acid storage battery cast-weld lead slag recovery device and method
US11892236B2 (en) * 2020-09-30 2024-02-06 Schenck Process Llc System for conditioning stucco in a dust collector
WO2025174619A1 (en) 2024-02-15 2025-08-21 United States Gypsum Company Apparatus and process for post stucco treatment and cooling

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US86002A (en) * 1869-01-19 Improvement in churns
US137496A (en) * 1873-04-01 Improvement in oil-stills
US4457628A (en) * 1981-07-23 1984-07-03 Misawa Home Co., Ltd. Stirring apparatus
US4965031A (en) * 1989-02-24 1990-10-23 The Celotex Corporation Continuous production of gypsum board

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US168510A (en) * 1875-10-05 Improvement in egg-beaters
US3236509A (en) * 1961-11-13 1966-02-22 British Plaster Board Holdings Process and apparatus for continuous calcining of powdered gypsum rock
US3307915A (en) * 1964-01-22 1967-03-07 Georgia Pacific Corp Apparatus for continuous calcination of gypsum
DE1558080B1 (en) * 1967-03-23 1970-02-12 Schilde Ag Gypsum cooker with hot gas injection
US3497184A (en) * 1968-08-14 1970-02-24 Dorr Oliver Inc Agitating apparatus for flocculating treatment of suspensions
US3955532A (en) * 1973-09-10 1976-05-11 Amchem Products, Inc. Agitation of an acidic aqueous coating composition containing dispersed particles of an organic coating-forming material
US4161390A (en) * 1977-06-16 1979-07-17 United States Gypsum Company Calcining kettle having multi-pass heating system
IE49127B1 (en) * 1979-01-08 1985-08-07 Bpb Industries Ltd Calcination method and apparatus
US4626199A (en) * 1985-04-25 1986-12-02 United States Gypsum Company Submerged combustion calcination
GB2185419B (en) * 1986-01-07 1990-04-18 Bpb Industries Plc Improvements in calcination apparatus
US4979830A (en) * 1989-10-02 1990-12-25 Gte Products Corporation/Gte Laboratories, Inc. Method for fluidized bed circulation control
US5333597A (en) * 1993-04-30 1994-08-02 Consolidated Industries Corp. Abatement member and method for inhibiting formation of oxides of nitrogen
US5743954A (en) * 1995-02-02 1998-04-28 United States Gypsum Company Method for continuous refractoryless calcining of gypsum
FR2733496B1 (en) * 1995-04-25 1997-06-27 Christian Dussel PROCESS AND PLANT FOR TREATING A POWDER MATERIAL BASED ON CALCIUM SULFATE, A NEW HYDRAULIC BINDER
SE9502234L (en) * 1995-06-20 1996-09-30 Abb Carbon Ab Method and apparatus for additional power generation in a power plant
US5743728A (en) * 1995-08-15 1998-04-28 Usg Corporation Method and system for multi-stage calcining of gypsum to produce an anhydrite product
US6138377A (en) * 1999-07-21 2000-10-31 United States Gypsum Company Apparatus and process for cooling and de-steaming calcined stucco

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US86002A (en) * 1869-01-19 Improvement in churns
US137496A (en) * 1873-04-01 Improvement in oil-stills
US4457628A (en) * 1981-07-23 1984-07-03 Misawa Home Co., Ltd. Stirring apparatus
US4965031A (en) * 1989-02-24 1990-10-23 The Celotex Corporation Continuous production of gypsum board

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1718445A4 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7718019B2 (en) 2005-04-27 2010-05-18 United States Gypsum Company Methods of and systems for preparing a heat resistant accelerant slurry and adding the accelerant slurry to a post-mixer aqueous dispersion of calcined gypsum
US8016960B2 (en) 2005-04-27 2011-09-13 United States Gypsum Company Methods of and systems for adding a high viscosity gypsum additive to a post-mixer aqueous dispersion of calcined gypsum
US8444787B2 (en) 2005-04-27 2013-05-21 United States Gypsum Company Methods of and systems for adding a high viscosity gypsum additive to a post-mixer aqueous dispersion of calcined gypsum
JP2010500958A (en) * 2006-08-17 2010-01-14 ユナイテッド・ステイツ・ジプサム・カンパニー Rocking stirrer for gypsum baking equipment

Also Published As

Publication number Publication date
BRPI0507697B1 (en) 2017-03-14
NZ548798A (en) 2011-02-25
WO2005092583A8 (en) 2006-11-16
CN1997609B (en) 2011-09-14
EP1718445A4 (en) 2010-04-14
EP1718576A4 (en) 2010-04-14
MY139186A (en) 2009-08-28
EP1718445A1 (en) 2006-11-08
IL177390A (en) 2010-05-31
IL177176A (en) 2010-06-30
CN1925958A (en) 2007-03-07
NO338738B1 (en) 2016-10-17
DK1718445T3 (en) 2017-04-03
JP2007527838A (en) 2007-10-04
IL177176A0 (en) 2006-12-10
CA2554983A1 (en) 2005-10-06
CA2555676A1 (en) 2005-10-06
AU2005225374B2 (en) 2010-06-24
KR20060135841A (en) 2006-12-29
IL177390A0 (en) 2007-07-04
CN1997609A (en) 2007-07-11
DK1718576T3 (en) 2017-04-10
NO20064371L (en) 2006-09-27
PL1718576T3 (en) 2017-07-31
BRPI0507973A (en) 2007-07-24
CN1925958B (en) 2013-08-21
AR050318A1 (en) 2006-10-18
JP4926939B2 (en) 2012-05-09
WO2005091819A2 (en) 2005-10-06
EP1718445B1 (en) 2016-12-21
ES2619123T3 (en) 2017-06-23
RU2375324C2 (en) 2009-12-10
RU2006134284A (en) 2008-04-10
CA2555676C (en) 2014-01-14
EP1718576A2 (en) 2006-11-08
AU2005225374A2 (en) 2005-10-06
JP2007526201A (en) 2007-09-13
WO2005091819A3 (en) 2006-10-12
PL1718445T3 (en) 2017-06-30
AU2005227119A1 (en) 2005-10-06
ES2619124T3 (en) 2017-06-23
BRPI0507697A (en) 2007-07-24
CA2554983C (en) 2013-11-12
KR20060132958A (en) 2006-12-22
EP1718576B1 (en) 2017-01-04
AU2005225374A1 (en) 2005-10-06
NZ548946A (en) 2010-06-25
MY143721A (en) 2011-06-30
JP4848357B2 (en) 2011-12-28
AU2005227119B2 (en) 2010-09-16
AR050319A1 (en) 2006-10-18
RU2355570C2 (en) 2009-05-20
NO20064370L (en) 2006-09-27
RU2006134283A (en) 2008-04-10
BRPI0507973B1 (en) 2016-08-02

Similar Documents

Publication Publication Date Title
CA2554983C (en) Swinging agitator for a gypsum calcining apparatus and the like
US7121713B2 (en) Swinging agitator for a gypsum calcining apparatus and the like
CA2660898A1 (en) Swinging agitator for a gypsum calcining apparatus and the like
US7175426B2 (en) High efficiency refractoryless kettle
MXPA06009637A (en) Swinging agitator for a gypsum calcining apparatus and the like
MXPA06009638A (en) High efficiency refractoryless kettle
HK1135062A (en) Swinging agitator for a gypsum calcining apparatus and the like

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWE Wipo information: entry into national phase

Ref document number: 2005225374

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 548798

Country of ref document: NZ

Ref document number: 2554983

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 177176

Country of ref document: IL

WWE Wipo information: entry into national phase

Ref document number: 2006/06578

Country of ref document: ZA

Ref document number: 4562/DELNP/2006

Country of ref document: IN

Ref document number: 200606578

Country of ref document: ZA

WWE Wipo information: entry into national phase

Ref document number: 2007500874

Country of ref document: JP

WWE Wipo information: entry into national phase

Ref document number: 06081184

Country of ref document: CO

ENP Entry into the national phase

Ref document number: 2005225374

Country of ref document: AU

Date of ref document: 20050214

Kind code of ref document: A

WWP Wipo information: published in national office

Ref document number: 2005225374

Country of ref document: AU

REEP Request for entry into the european phase

Ref document number: 2005713604

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2005713604

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: PA/a/2006/009637

Country of ref document: MX

WWE Wipo information: entry into national phase

Ref document number: 200580006046.3

Country of ref document: CN

WWE Wipo information: entry into national phase

Ref document number: 2006134283

Country of ref document: RU

Ref document number: 1020067020044

Country of ref document: KR

WWP Wipo information: published in national office

Ref document number: 2005713604

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1020067020044

Country of ref document: KR

ENP Entry into the national phase

Ref document number: PI0507697

Country of ref document: BR