The disclosure relates to the field of pumps and devices for transferring molten metal.
Pumps are used for transferring molten metal. In one type of pump, molten metal is inlet into the base by a rotating impeller, travels into the bottom of a vertical riser and flows upwards to an outlet from which the molten metal travels to its intended destination. A typical riser used in a pump manufactured by High Temperature Systems, Inc., rated at about 4000 pounds/minute of aluminum flow, has an inner diameter (ID) of about 3 inches, and there is downstream piping associated with it having this diameter. This results in a metal velocity at about 9 feet/second. While the inside of the riser is not a large concern, because oxide generation inside the riser is limited by the small surface area, at the outlet of the riser high turbulence causes existing oxide layers to be constantly broken and reformed, leading to a large oxide generation. Typically, this may not be a great concern if the next step is to purify the metal anyway, but some operations skip degassing/fluxing and take the molten metal straight to casting/final production. There are small metal losses through the oxide formation regardless of whether purifying or not, but typically this prior art pumping system is still better than most other transfer methods.
When the pump is running, the outlet opening of the pump causes a stream of metal to flow to the back of the prior art riser very quickly, and can cause high turbulence and splashing on the surface of the metal (see
Referring to a first aspect of the disclosure, a pump system for transferring molten metal includes a pump that includes a motor. The pump also includes a base that is adapted to be submerged in molten metal contained in a vessel, the base including at least one inlet opening, an outlet opening and an impeller chamber fluidly communicating with the at least one inlet opening and the outlet opening. A shaft sleeve is part of the pump and is adapted to fasten to the base and extends outside the molten metal. An impeller is part of the pump and is adapted for rotation inside the impeller chamber. The pump includes a shaft that is driven by the motor and extends in the shaft sleeve. The impeller is fastened to the shaft. The pump system includes a transfer block that is adapted to be submerged in the molten metal and extends outside the molten metal. The transfer block includes an interior wall extending along its height, an inlet opening that receives molten metal outlet from the outlet opening of the base, and an outlet. The transfer block includes an obstruction member disposed in an interior thereof that disrupts an initial flow path of molten metal inlet into the transfer block from the base. The transfer block includes a diffuser plate inside the interior thereof. The diffuser plate includes through holes formed therein.
Referring to specific features of the first aspect, taken alone or in any combination, a nozzle fluidly communicates molten metal from the outlet opening of the base to the inlet opening of the transfer block.
Another feature is that the obstruction member is a post having a circular cross-sectional shape. A further feature is that the transfer block is formed of cast ceramic material and the post is part of the cast ceramic material. Yet another feature is that the post is centrally located in the interior volume, an annular space being disposed radially outward of the post between the interior wall and the post, the diffuser plate forming an upper surface of the annular space.
Another feature is that the transfer block comprises a detachable outlet spout.
Further, the interior wall can include at least two or more notches or protruding guides adapted to engage the diffuser plate to prevent rotation of the diffuser plate. In one example, vertically extending guides or ribs protrude inwardly from the interior wall, at least two spaced apart guides being used, which are received in notches of the diffuser plate. Another feature is that the guides end spaced above the obstruction member, permitting the diffuser plate to be rotated into a fixed position once it is lowered past the guides. Another feature includes structure adapted to rotationally lock the diffuser plate into the fixed position.
Another variation is that the interior wall and the diffuser plate have a circular shape in a top view and the diffuser plate contacts the interior wall. In this exemplary feature, the diffuser plate is disposed above and near the obstruction member.
In particular, all components of the pump that contact molten metal can be comprised of a refractory material.
Another feature is a lid for covering the transfer block near the upper end portion, the lid including a fitting around an opening for receiving a conduit for flowing inert gas into the transfer block.
Yet another feature is that the through holes of the diffuser plate are at least 2 inch in size.
In another feature the diameter of the interior wall of the transfer block is at least 8 inches.
In one example, the diameter of the interior wall of the transfer block is at least 8 inches for use with a pump rated at about 1000 Lbs/Min of metal flow. In another example, the diameter of the interior wall of the transfer block is at least 12 inches for use with a pump rated at about 4000 Lbs/Min of metal flow. In another example, the diameter of the interior wall of the transfer block is at least 16 inches for use with a pump rated at about 4000 Lbs/Min of metal flow.
A second aspect of the disclosure features a refractory transfer block for transferring molten metal that is adapted to be submerged in molten metal and to extend outside the molten metal. The transfer block includes an interior wall extending along a height thereof and forming an interior volume. There is a lower inlet opening that is adapted to receive an initial flow path of molten metal that flows into the interior volume, and an outlet. An obstruction member is disposed in the interior thereof that is adapted to disrupt the initial flow path of molten metal. A diffuser plate is disposed in the interior volume including through holes formed therein.
Referring to more specific features of the second aspect of the disclosure alone or in any combination, in one feature the transfer block is formed of cast ceramic material and the obstruction member includes a post that is part of the cast ceramic material.
In another feature the interior wall and the diffuser member have a generally circular shape from a top view. The obstruction member includes a cylindrical post that is centrally located in the interior of the transfer block. An annular space is disposed radially outward of the post between the interior wall and the post. The diffuser plate forms an upper surface of the annular space.
In yet another feature the interior wall includes at least two notches or protruding guides adapted to engage the diffuser plate to prevent rotation of the diffuser plate. In one example, vertically extending guides or ribs protrude inwardly from the interior wall, at least two spaced apart guides being used, which are received in notches of the diffuser plate.
Another feature is that the guides end spaced above the obstruction member, permitting the diffuser plate to be rotated into a fixed position once it is lowered past the guides.
In another feature the transfer block includes structure adapted to rotationally lock the diffuser plate into the fixed position.
A further feature is that the transfer block comprises support structure adapted to be fastened above and to a vessel containing the molten metal. The transfer block and a pump that provides the initial flow path of molten metal are adapted to be mounted to the support structure. Together the pump and the transfer block are able to be repeatedly submerged into and removed from the molten metal of the vessel when moving the support structure.
In another feature a lid covers the transfer block outside the molten metal. A fitting around an opening in the lid receives a conduit for flowing inert gas into the transfer block.
Still further is a feature in which the diameter of the holes of the diffuser plate is, for example, at least ½ inch, or at least 1 inch, and in particular, ranges from 2 inch to 1 inch. All numerical ranges used in this disclosure include the endpoint if one endpoint is used, and both endpoints if two endpoints are used.
Another feature is that the interior wall of the transfer block is circular in a top view. The diameter of the interior wall (ID) of the transfer block can be one of the following: at least 8 inches, at least 10 inches, at least 12 inches, at least 16 inches and at least 24 inches.
The disclosure now refers to the drawings and Detailed description that follows.
Referring to
A nozzle 46 fluidly communicates molten metal from the base outlet opening 20 to the transfer block inlet opening 34.
In particular, the obstruction member 38 is a cylindrical post 38a. Further, for example, the transfer block 30 is formed of cast ceramic material and the post 38a, for example, is part of the cast ceramic material (i.e., the transfer block 30 and the post 38a are cast together). The post 38a is, for example, centrally located in the interior of the transfer block 30. An annular space 48 is disposed radially outward of the post 38a between the interior wall 32 and the exterior surface 50 of the post 38a. The diffuser plate 42 is located, for example, above the post 38a, and, in particular, is near or contacts the post and its lower surface 52 forms an upper surface of the annular space 48. The transfer block 30 includes a bottom interior surface 54 that forms a bottom surface of the annular space 48. The transfer block 30 includes a detachable outlet spout 56.
Referring to
More specifically, the notches 60 of the diffuser plate 42 engage the guides 58 or ribs so that the diffuser plate 42 can slide vertically down the transfer block along the guides 58 without being permitted to rotate until near the central post 38a. The guides 58 can terminate just above the central post 38a to form a channel 60 located between the bottom of the guides 58 and the top of the post 38a, which permits the diffuser plate 42 to be rotated into a fixed position. The transfer block 30 could include a stop member that limits rotation of the diffuser plate 42 at its lowered position. In particular, the interior wall 32 can define a cylindrical volume of the transfer block 30 and the diffuser plate 42 can have a circular disk shape. Alternatively, the diffuser plate 42 and the interior wall 32 could have other shapes such as square or rectangular.
In a variation, the diffuser plate 42 may be located around the post 38a (below the top of the post 38a) with the diffuser plate 42 including a central opening that receives the post 38a and can be fastened to it such as by a threaded connection or other suitable connection. For example, the guides 58 may extend below the upper surface of the post 38a and are received in the notches 60 of the diffuser plate 42. The post 38a may include a ceramic ring fastened below its upper surface. The guides 58 may end above the ceramic ring forming a channel between the bottom of the guides 58 and the ceramic ring. The diffuser plate 42 can be pushed downward past the guides 58 into the channel and rests on the ring attached to the post after being rotated into a fixed position.
All components of the pump system 10 that contact molten metal are formed of a refractory material. For example, the base 14, shaft sleeve 24, impeller 26 and shaft 28 can be formed of graphite. In one aspect, the transfer block 30 can be formed of a suitable refractory material including but not limited to a cast ceramic material, for example, silicon carbide, alumina, silica or combinations thereof.
Another feature is a lid 70 for covering the transfer block 30 near its upper end portion. A fitting 72 around an opening receives a conduit for flowing inert gas to the molten metal contained in the transfer block 30. The inert gas flows to the surface of molten metal inside the transfer block 30 and may flow into that molten metal, further reducing a possibility of formation of metal oxides.
The shaft sleeve of the pump and the motor are mounted to a metal plate. The transfer block is also mounted to the metal plate. The metal plate can include a hook or other structure enabling the pump and transfer block to be removed from, and submerged into, the molten metal together as one unit.
This design of the molten metal transfer system of this disclosure reduces turbulence, specifically at the top surface of the metal, to generate less oxides when performing molten metal transfer. The molten metal transfer system of this disclosure increases the surface area of the transfer block 30 (e.g., the ID of the transfer block) compared to an ordinary riser's inner chamber (e.g., ID) so that the metal velocity is lowered for the same volume of metal transferred. The diameter D of the interior wall 32 forming, for example, a cylindrical shaped volume in the transfer block 30 is larger than the inner diameter of a typical riser used for that particular pump rating, by at least 2 times, or at least three times, or at least 4 times, or at least 5 times. For example, a transfer pump manufactured by High Temperature Systems, Inc., rated at about 4000 Lbs/Min of aluminum flow would typically have a riser ID of about 3 inches, as would the downstream piping associated with it. A molten metal transfer system according to this disclosure, including a pump rated at 4000 Lbs/Min of aluminum flow, can have an inner diameter of the transfer block (i.e., interior wall diameter D) of about 16 inches or more, for example. This reduces the metal flow velocity to 0.32 feet/second. This greatly reduces the possibility of breaking the top oxide surface layer and protects the metal underneath it from oxidation.
Referring to
The transfer block in
As can be seen in
This disclosure utilizes the diffuser plate 42 that can be placed inside the transfer block 30 to mostly eliminate the horizontal flow. The horizontal flow just above the diffuser plate 42 (
The features of this disclosure allow the transfer pump system 10 to perform much faster starts, as well as to reduce surface turbulence. Furthermore, this allows the benefits of this system to be realized in a much more compact system, as the conventional way to solve this issue would be to make the riser even larger yet, or significantly reduce the flow rate.
A cover 70 for the upper end portion of the transfer block 30 includes a fitting around an opening for receiving a conduit through which inert gas is provided. Flowing inert gas down into the transfer block 30 prevents or reduces the amount of oxide formation should any turbulence occur, such as if the diffuser plate was damaged or if the transfer block was operated outside of normal parameters. It may also help to reduce oxide formation on the sides of the transfer block as the metal level changes, making cleaning and normal maintenance easier.
At the outlet of the transfer block 30 a detachable outlet nozzle 56 can be fastened using a bolt on design with a refractory gasket placed between the transfer block and the outlet nozzle, allowing the end user to customize the outlet for their application, such as should they wish to operate at a lower/higher than standard flow rate.