The present invention relates to furnaces for high temperature treatment of various materials and, more particularly, to an automatic feed oven.
A number of automatic feeds for ovens are known in the prior art. For example, ovens with a screw feeder are known to allow for the transportation of material into the oven. These types of ovens are provided with a rotating screw that has a pitch that moves material in a given direction with rotation of the screw. Another type of feeder system known is a vibratory feeder system. In these types of systems, the feed mechanism is vibrated at a particular frequency to move the material down a gradient. These types of conveyors or feeders depend on the flowability of the material being conveyed.
With parenthetical reference to corresponding parts, portions or surfaces of the disclosed embodiment, merely for the purposes of illustration and not by way of limitation, the present invention provides an automatic feed oven for material processing (1) comprising an insulated heating chamber (4), the heating chamber having a product discharge outlet (21) and a material inlet (39), a heating source (14) operatively arranged to heat the heating chamber, a chamber feed mechanism (40) operatively arranged to feed material into the chamber through the material inlet, the chamber feed mechanism comprising a receptacle (6) operatively arranged to receive material, a linear actuator (42) operatively arranged to move the receptacle between a fill position (55) outside the chamber and a discharge position (56) within the chamber, and a rotational actuator (43) operatively arranged to rotate the receptacle between a receiving position (57) and a releasing position (58), and a receptacle feed mechanism (44) operatively arranged to feed material into the receptacle when the receptacle is in the fill position.
The heat source may be operatively arranged to selectively heat the heating chamber to at least 600° C. The heating chamber and the chamber feed mechanism may be within an internal atmosphere isolated from an external ambient atmosphere. The fill position and the discharge position may be at least two feet apart. The receiving position and the releasing position may be between about 90° and about 180° apart. The oven may further comprise a spill access port (45) for removal of material spilled between the receptacle and the receptacle feed mechanism. The oven may further comprise a cooling apparatus (46) configured to cool the receptacle.
The receptacle feed mechanism may comprise a screw or vibratory conveyor (7) having an inlet (61) and an outlet (62), a hopper (12) having an outlet in communication with the inlet of the screw or vibratory conveyor, and the outlet of the screw or vibratory conveyor operatively configured to feed material into the receptacle when the receptacle is in the fill position. The receptacle feed mechanism may further comprise a metering control communicating with the conveyor and configured to activate the conveyor when the receptacle is in the fill position and to deactivate the conveyor when the receptacle is not in the fill position.
The receptacle feed mechanism may comprise a funnel (63) having a discharge port (64) and a stopper (65) configured to move from an open position (66) to a closed position (67), wherein the discharge port is substantially blocked by the stopper when the stopper is in the closed position. The receptacle feed mechanism may comprise a metering control configured to provide the stopper in the open position when the receptacle is in the fill position and to provide the stopper in the closed position when the receptacle is not in the fill position, and the metering control may comprise a mechanical trigger.
The oven may further comprise a generally horizontally extending process tube (2) supported for rotation relative to the heating chamber, the process tube having a portion (37) extending into the heating chamber, and the feed mechanism may be configured and arranged to feed product into the process tube. The oven may further comprise a generally horizontally extending process tube supported for rotation relative to the heating chamber, the process tube having a first portion (36) generally arranged outside of the heating chamber and a cantilevered second portion (37) extending from the first portion into the heating chamber and terminating in a discharge end (38) within the heating chamber, the feed mechanism configured and arranged to feed product into the process tube, and a bearing assembly 41 operating between a support member (34) and the first portion of the process tube and configured and arranged to support the process tube and transmit rotational torque to the process tube.
The heating chamber may comprise an outer shell (10), a muffle (15) and an insulation layer (11) between the outer shell and the muffle. The heating element may be a graphite resistance heating element. The heating element may comprise induction coils (30) and a graphite susceptor (31). The heating element may be an exothermic reaction within the heating chamber. The process tube may be graphite or quartz. The chamber feed mechanism may extend through the first portion of the process tube and terminate at a feed discharge position within the heating chamber. The product discharge outlet may comprise a discharge chute (22) and a discharge heating element (25) operatively arranged to selectively heat the discharge shut.
In another aspect, the invention provides an automatic feed oven system for material processing comprising an insulated heating chamber, the heating chamber having a product discharge outlet and a material inlet, a heat source operatively arranged to heat the heating chamber, a chamber discharge operatively arranged to remove product from the chamber through the discharge outlet, a chamber feed mechanism operatively arranged to feed material into the chamber through the material inlet, the chamber feed mechanism comprising a receptacle operatively configured to receive material, a linear actuator operatively arranged to move the receptacle between a fill position outside the chamber and a discharge position within the chamber, and a scrapper operatively arranged to dislodge the material from the receptacle when the receptacle is in the discharge position, and a receptacle feed mechanism operatively arranged to feed material into the receptacle when the receptacle is in the fill position. The scrapper may comprise a linear actuator (105) connected to a member (106) operatively arranged to dislodge material from said receptacle.
One object of the invention is to provide an improved furnace that provides the materials being processed without premature melting.
Another object is to provide an improved furnace that processes materials at high temperatures without the material adhering to the processing equipment.
Another object is to provide an improved furnace where material flow is not blocked by undesired material build-up.
These and other objects and advantages will become apparent from the foregoing and ongoing written specification, the drawings, and the claims.
At the outset, it should be clearly understood that like reference numerals are intended to identify the same structural elements, portions or surfaces consistently throughout the several drawing figures, as such elements, portions or surfaces may be further described or explained by the entire written specification, of which this detailed description is an integral part. Unless otherwise indicated, the drawings are intended to be read (e.g., cross-hatching, arrangement of parts, proportion, degree, etc.) together with the specification, and are to be considered a portion of the entire written description of this invention. As used in the following description, the terms “horizontal”, “vertical”, “left”, “right”, “up” and “down”, as well as adjectival and adverbial derivatives thereof (e.g., “horizontally”, “rightwardly”, “upwardly”, etc.), simply refer to the orientation of the illustrated structure as the particular drawing figure faces the reader. Similarly, the terms “inwardly” and “outwardly” generally refer to the orientation of a surface relative to its axis of elongation, or axis of rotation, as appropriate.
Referring now to the drawings, and more particularly to
As shown in
Thermally insulated heating chamber 4 surrounds the portion of tube 2 being heated with at least one zone of control and at least one element per zone of control. However, while furnace 1 is shown as having a single heating zone, heating chamber 4 may be divided into multiple temperature zones separated by insulation barriers to allow for greater temperature definition. Thus, heating elements 14 may be powered and positioned as desired to provide a constant temperature throughout the heating zone or to provide multiple temperature zones for thermal profiling.
Heating chamber 4 includes a number of ports or vents. Material being processed exits the floor of heating chamber 4 through discharge outlet 21. Discharge outlet 21 comprises a discharge chute 22 and chute heating elements 25 that heat discharge chute 22. A liner may be provided in discharge chute 22 to facilitate movement of material being processed. Accordingly, discharge chute 22 is separately heated to prevent melted material exiting process tube 2 from prematurely cooling and sticking to discharge chute 22. Discharge chute 22 may feed a solidification unit or some other conventional collection device.
Process tube 2 extends into heating chamber 4 through heating chamber inlet 39. Process tube 2 is generally a cylindrical graphite member elongated along axis x-x and adapted to rotate about axis x-x. As shown, process tube 2 extends from the entrance or drive section 47 of furnace 1 into heating chamber 4 of the heating section 48 of furnace 1. While shown as extending horizontally, under normal operating conditions process tube 2 is tilted from horizontal to aid the movement of materials through process tube 2. In addition, while process tube 2 is shown as being formed of a single tubular unit, it may be formed from two or more interconnected sections of tube, depending on various considerations, such as the total length required and the specific requirements of each section of the tube. Also, the materials used to form the sections of tube may vary depending on their position in the furnace, with the sections of tube 2 upstream being metal rather than graphite sections. In this embodiment, tube 2 includes an inner quartz tube liner. However, it is contemplated that this inner or second tube may be formed of graphite or ceramic, such as silicon carbide, alumina or mullite, depending on considerations such as the materials being processed. The liner may also be a second piece of sacrificial graphite. In another alternative, tube 2 may be quartz and may not include a liner.
As shown in
Feed mechanism 44 is operatively arranged to feed material into spoon 6 when spoon 6 is in fill position 55 and receiving position 57, and generally comprises a large upstream feed hopper 12, a smaller downstream funnel-shaped hopper 63 that narrows and discharges from discharge port 64 into spoon 6 when spoon 6 is in fill position 55 and receiving position 57, and a screw conveyor 7 operating between upstream hopper 12 and funnel 63. Conical or dish-shaped stopper 65 is employed to control the discharge of material from discharge port 64. Pneumatic actuator 27 moves stopper 65 vertically from open position 66 shown in
Alternative designs for discharge port 64 may be employed. For example, discharge port 64 may be a rectangular slot with the long axis of the slot parallel to axis x-x of tube 2. Whether the slot is open or closed may be controlled with a hinged door either parallel or perpendicular to axis x-x.
The position of stopper 65 is a function of the position of receptacle 6, such that the return of spoon 6 from position 56 to linear position 55 and rotational position 57 causes actuator 27 to move stopper 65 to open position 66, opening port 64 and emptying material into spoon 6. The overall average rate of material fed into spoon 6 is controlled by the rate of conveyance of screw conveyor 7. The cycle time of spoon 6 extending to discharge position 56, dumping by rotation to release position 58, rotating back to receive position 57 and returning to fill position 55 is short enough so that receptacle 6 is not over-filled by material accumulated in downstream funnel hopper 63. The cycle time for spoon 6, the speed of screw conveyor 7 and the periodic rate at which stopper 65 moves between position 66 and 67 may be coordinated such that material only exits discharge 64 into spoon 6 when spoon 6 is in positions 55 and 57 and in amounts such that spoon 6 does not overflow.
Alternatively, the movement of stopper 65 and spoon 6 may be controlled by sensors and programmable logic controllers or hardwired relays. In this alternative, proximity switches are positioned relative to the three actuators 27, 42 and 43 to sense the location of spoon 6 and stopper 65. Using these proximity switches, the system first confirms that rotational actuator 43 is in the feed position, at which spoon 6 is in receiving position 57, confirms that linear actuator 42 is in the retracted position, at which spoon 6 is in fill position 55, confirms that screw feeder 7 is off, and confirms that actuator 27 is in the closed position, at which stopper 65 is in closed position 67. Actuator 27 then elevates stopper 65 to open position 66, releasing material from discharge port 64 into spoon 6. Actuator 27 then lowers stopper 65 to closed position 67. Linear actuator 42 then extends rods 85/3 and spoon 6 to discharge position 56. This position is confirmed by proximity switch. Rotational actuator 43 then rotates actuator 42 and spoon 6 between 90° and 180° to release position 58, releasing material from spoon 6 onto process tube 2 in heating chamber 4. This is confirmed by proximity switch. Rotational actuator 43 then rotates linear actuator 42 and spoon 6 back to receiving position 57. This is confirmed by proximity switch. Linear actuator 42 then retracts rods 85/3 and spoon 6 from heating chamber 4 to fill position 55. This is confirmed by proximity switch. Screw feeder 7 is then activated for a predetermined period of time, feeding a selected amount of material from hopper 12 into funnel 63. Screw 7 is then deactivated. The above sequence is then repeated.
Thus, in this embodiment, material is feed into hopper 12, where it discharges through inlet 61 of horizontally extending feeder tube 60, which houses screw conveyor 7. While in this embodiment feeder 7 is a screw type feeder, other types of feeders may be used, such as vibratory or pneumatic type feeders. With a vibratory feeder, flexible bellows are positioned so that feeder tube motion, such as vibration, will not hinder flow and an adequate seal is provided for gas containment purposes. Tube 60 extends through a port into fill tube 54 and outlet 62 of tube 60 is positioned above cylindrical funnel 63 such that material conveyed through outlet 62 falls into funnel 63. Stopper 65 is moved by actuator 27 from its closed position 67 blocking discharge port 64 to its open position 66, allowing material to flow out of discharge port 64 and into spoon 6.
As shown in
Rotational actuator 43 is a pneumatic actuator that converts compressed air or gas from ports 75 and 76 into rotational motion about axis x-x. Rotational actuator 43 is fixably supported in tube 70 by support plate 71. Rotational actuator 43 is configured to cycle linear actuator 42 back and forth between about 0° and 180° degrees as desired.
Linear actuator 42 is connected for rotation by coupling 72 to rotational actuator 43. Linear actuator 42 is a pneumatic cylindrical actuator adapted to actuate spoon 6 from receiving position 57 shown in
Accordingly, rotational actuator 43 is configured to move spoon 6 from receiving position 57, in which material may be dropped into and retained within spoon 6, to releasing position 58, which is a rotational position from 90° to 180° about axis x-x from receiving position 57. Linear actuator 42 is adapted to move spoon 6 from fill position 55 directly below discharge port 64 to discharge position 56 within heating chamber 4. In this embodiment, actuator 42 is configured to have a stroke of between about 2 and 6 feet and preferably a stroke of about 4 feet. Thus, fill position 55 and discharge position 56 may be more than two feet apart in this embodiment.
As shown in
Tube 70 also includes cooling vent 46 for cooling spoon 6 and, if desired, rod 3 to the extent that rod 3 passes by the outlet of cooling vent 46. Thus, where the temperature of spoon 6 is likely to be exceedingly high, cooling vent 46 is used to cool spoon 6 when it is in or near fill position 55. In this embodiment, cooling vent 46 comprises a gas jet that provides an impinging cooled gas stream against the surface of spoon 6 such that the outer convex surface of spoon 6 is cooled when spoon 6 is in fill position 55 and receiving position 57. In addition, the inner concave surface of spoon 6 may be cooled by rotating spoon 6 to releasing position 58 when spoon 6 is still in fill position 55 near gas cooling vent 46. Thus, spoon 6 is periodically cooled when it is retracted from heating chamber 4.
The length of rod 3 may vary as desired. As shown in
As shown in
As shown in
As shown on
In operation at high temperatures, it is often preferred to maintain a non-oxidizing atmosphere, such as nitrogen or argon gas atmosphere, in heating chamber 4 and process tube 2. In this embodiment, entrance zone 47 is enclosed in, or surrounded by, a chamber for the containment of atmosphere, dust and light. Heating chamber 4, this entrance area, discharge assembly 21, tube 70, tube 54 and port 55 are configured to form an enclosure to maintain the selected atmosphere around and within process tube 2. The interior atmosphere of process tube 2 may be controlled by passing a non-oxidizing gas, such as nitrogen for example, through it. If a co-current gas flow is desired, gas is provided through port 17 and exits heating chamber 4 through process vent 20. If counter flow is desired, the direction of flow can be reversed. A counter flow of non-oxidizing gas in discharge chute 22 may also be provided. Furthermore, a non-oxidizing atmosphere may be provided in heating chamber 4 by maintaining a positive pressure of gas through heating chamber 4 using gas passageways into heating chamber 4. In addition, a desired atmosphere may be provided in feed mechanism 44 using inlet 18 in hopper 12. Similarly, a desired atmosphere in entrance or drive section 47 may be provided directly through drive area gas port 19. Thus, multiple alternate atmospheres and alternate current flows may be employed in furnace 1.
Overhung graphite rotary tube furnace 1 may be used to process various types of feed material, including particulate material. For example, furnace 1 may be used to process silicon particulate material, with the silicon particulate material melting inside quartz or quartz lined process tube 2 and exiting through discharge assembly 21 as a liquid. Furnace 1 is generally suitable for the treatment of particulate material which melts at temperatures as high as 2600° C. The preferred temperature range of furnace 1 is from about 600° C.-2200° C. For silicon processing the preferred temperature is about 1500° C. and the material may be fed directly into the heated and cantilevered section 37 of processing tube 2 to melt.
Furnace 1 provides a number of unexpected benefits. With feed mechanism 40 and cantilevered tube 2, furnace 1 is suitable for partially melting material in a continuous feed system without causing premature melting. In addition, because the material is discharged from discharge end 38 of tube 2 into the hot zone of the furnace, the material is discharged without premature freezing. With feed mechanism 40, the backflow of heat from heating chamber 4 does not melt material being processed, thereby causing it to stick together or to the walls of process tube 2. Likewise, discharging from cantilevered portion 37 in heating chamber 4 reduces the likelihood of material sticking together or to the tube walls or downstream surfaces, thereby blocking material flow.
The present invention contemplates that many changes and modifications may be made. Therefore, while the presently-preferred form of the improved furnace has been shown and described, and a number of alternatives discussed, persons skilled in this art will readily appreciate that various additional changes and modifications may be made without departing from the spirit of the invention, as defined and differentiated by the following claims.
This application claims the benefit of U.S. Provisional Patent Application No. 61/204,723, filed Jan. 9, 2009. The entire content of such application is incorporated by reference herein.
Number | Date | Country | |
---|---|---|---|
61204723 | Jan 2009 | US |