Title of Invention

"METHOD AND APPARATUS FOR CONTINUOUS HOT- DIP COATING OF METAL STRIP"

Abstract

An apparatus for continuous hot-dip coating of metal strip is disclosed. The apparatus includes a first coating pot to hold a molten bath of a first coating metal and a first metal heating means to heat the bath of molten metal in the first pot. The apparatus also includes a second coating pot to hold a molten bath of a second coating metal, which second pot is shallow in relation to the first pot and is positionable within an upper part of the first but removable therefrom, and a second metal heating means operable to heat the molten bath of metal in the second pot. The apparatus also includes a strip feed means to feed strip into and from the upper part of the first pot when the second is removed therefrom whereby to dip the strip in the molten bath of the first coating metal and alternatively operable to feed the strip into and from the molten bath in the second coating pot when the second coating pot is positioned in the upper part of the first coating pot whereby to dip the strip within the bath of the second coating metal.

Full Text

The present invention relates to a method and apparatus for the continuous hot-dip coating of metal strip in a hot-dip coating plant so as to change the kind of coating applied to the strip. In general, the application relates to protective coatings to metal strip by hot-dip coating. The invention has particular but not exclusive application to the continuous hot-dip coating of steel strip with protective metallic coatings of zinc or aluminium-zinc alloy. In the hot-dip galvanising process, steel strip is generally passed through an annealing furnace and kept under the protection of a reducing furnace atmosphere until it passes into a bath of coating metal held in a coating pot. The coating metal is usually maintained molten in the coating pot by the use of heating inductors. The strip may pass through an elongate furnace exit chute or snout which dips into the bath. Within the bath the strip passes around one or more sink rolls and is taken upwardly out of the bath. After leaving the coating bath the strip may pass through a gas knife or gas wiping station in which its coated surfaces are subjected to jets of wiping gas to control the thickness of the coating. In a normal galvanising process the coating metal may be zinc or zinc with about 0.2% of aluminum by weight. This produces a standard galvanised steel which has moderate corrosion resistance and can be produced at moderate cost. Superior coatings can be obtained with zinc and aluminium alloys having a much higher aluminium content, for example in the range 25-70%. There is presently a need to provide a hot-dip coating plant which can be operated in alternative modes either to produce highly corrosion resistant strip coated with a zinc-aluminium alloy of high aluminium content or alternatively to produce standard galvanised strip with a predominantly zinc coating. In particular, there are many existing plants around the world producing the high corrosion resistant strip coated with zinc-aluminium alloy in locations where there is still a demand for the standard galvanised strip and there is accordingly a need to be able to convert existing plant for production of both kinds of strip. It is not commercially or technically attractive to use the same coating pot to hold both kinds of coating metal. This would require the pot to be totally pumped out or emptied on changing from one form of coating to the other, which will inevitably result in damage to the coating metal heating inductors and refractories in the pot. It is also extremely time consuming and generates metals which need to be reclaimed. Moreover, it is very difficult to produce a bath of almost pure zinc in a pot which has previously contained a metal with a high proportion of aluminium. It is known to provide two fixed coating pota side by side and make parts of the strip feed lines and furnace moveable to line up alternatively with one pot or the other. However, this is extremely expensive and involves difficult engineering of the moveable parts. It is also known to move and replace a coating pot with a similar substitute pot but this is also extremely expensive, one particular arrangement of this type is disclosed in US patent 3,643,627 of Killen et al. The apparatus and method disclosed in this US patent involve the use of a turntable capable of holding two coating pots, whereby when it is desired to change the coating metal, the "on-line" coating pot is rotated out of the on-line position, while a new coating pot is simultaneously rotated into the on-line position. Another arrangement of this type is disclosed in US patent 3,130,068 of Whitley. The US patent discloses making a changeover of one coating pot with another coating pot by emptying a first coating pot of its molten coating metal, removing the coating pot from the coating station, placing a second coating pot at the coating station, pumping a second coating metal into the second coating pot and resuming the coating process. It is also known to position a second coating pot within a first coating pot. Specifically US patent 4,645,695 of Gerard discloses an arrangement in which a second coating pot containing a second metal that is shallower than a deeper first coating pot containing a first metal is submerged in the first coating metal in the first pot, whereby a metal strip can be coated with the second coating metal instead of the first coating metal without making substantial changes to the coating line setup. The US patent immerses the second coating pot in the first coating metal to use the heat of the first coating metal to maintain the temperature of the second coating metal. There are a number of disadvantages with this immersed pot-in-pot arrangement. By way of example, it is difficult to avoid dripping the first coating metal from the outer surface of the second coating pot as it is removed from the first coating pot after a coating run. In addition, the contact of the first coating metal and the outer surface of the second coating pot accelerates wear erosion of the second coating pot. In addition, immersing the second coating pot in the first coating mean can introduce impurities on the outer surface of the second coating pot into the first coating metal. The present invention provides an alternative solution to the above-described known arrangements by which a main coating pot can be used for coating strip with a first coating metal and a second, shallower coating pot can be positioned within the upper part of the main coating pot to enable coating with a second coating metal while the main coating pot retains molten coating metal above its inductors. According to the invention there is provided a method for the continuous hot-dip coating of metal strip in a hot-dip coating plant to change the kind of coating applied to the strip, characterised in that said method comprises the steps of: passing strip through a molten bath of a first coating metal held in a first coating pot and maintained in a molten state by operation of induction heater means having metal flow channels in communication with the bath thereby producing coated strip coated with the first coating metal; stopping the strip coating operation; reducing the level of the molten bath of said first coating metal in the first coating pot to empty an upper part of the first coating pot without disrupting the communication of the induction heater channels with the molten bath; positioning within the emptied upper part of the first coating pot a second coating pot which is shallow relative to the first coating pot and is supported above and without contact with the reduced level of the molten bath of the first coating metal; forming a molten bath of a second coating metal in the second coating pot; and passing strip through the molten bath of the second coating metal in the second coating pot to produce coated strip which is coated with the second coating metal. Preferably the induction heating channels connect with the interior of the first coating pot at or below the reduced level of the molten bath therein so as to remain filled with the first molten metal throughout coating of the strip with both the first and second coating metals. Preferably the molten bath of the second coating metal is formed in the second coating pot by pre-melting the second coating metal and pouring that melted metal into the second coating pot. Preferably the molten bath of the second coating metal is maintained in a molten state during dip coating of the strip therein by heating the molten bath by the operation of electrical resistance heating means of the second coating pot. The electrical resistance heating means may be in the form of one or more than one electrical resistance heating element located in a housing that is immersed in the molten bath of the second coating metal and shields the heating element or elements from contact with the molten metal. Alternatively, the electrical resistance heating means may also be in the form of electrical resistance heaters external to the second coating pot. Preferably further the molten metal in the reduced level bath of the first coating metal is maintained in a molten state during hot-dip coating of the strip in the second coating pot by operation of the induction heater means. The strip may be passed around a first one or more sink rolls in the first coating pot during coating with the first coating metal and may be passed around a further one or more sink rolls in the second coating pot during coating with the second coating metal. In this case/ the first one or more sink rolls may be removed from the first coating pot before the second coating pot is positioned in the upper part thereof. More specifically, the first one or more sink rolls may be removed from the first coating pot before the step of reducing the level of the molten bath of the first coating metal. The present invention also provides an apparatus for continuous hot-dip coating of metal strip, having: a first coating pot to hold a molten bath of a first coating metal; first metal heating means to heat the bath of molten metal in the first pot; a second coating pot to hold a molten bath of a second coating metal which second pot is shallow in relation to the first pot and is positionable within an upper part of the first but removable therefrom; a second metal heating means operable to heat the molten bath of metal in the second pot; and a strip feed means to feed strip into and from the upper part of the first pot when the second pot is removed therefrom whereby to dip the strip in the molten bath of the first coating metal and alternatively operable to feed the strip into and from the molten bath in the second coating pot when the second coating pot is positioned in the upper part of the first coating pot whereby to dip the strip within the bath of the second coating metal. Preferably the apparatus further includes a furnace to heat the strip prior to being hot-dip coated. Preferably further the furnace has an elongate exit chute or snout to enclose the strip as it is fed by the strip feed means into the molten bath of the first coating metal or into the molten bath of the second coating metal without exposure to the air. Preferably further the apparatus includes a gas wiping means to wipe the dipped strip as it leaves the molten bath of the first coating metal or the molten bath of the second coating metal to control the thickness of the coating. The apparatus may further include sink roll means to guide the strip within the coating baths. The sink roll means may include one or more sink rolls or pair of sink rolls positionable in the first coating pot when the second pot is removed to guide the strip within the molten bath in the first coating pot and one or more further sink rolls positionable in the second coating pot to guide the strip in the molten bath in the second coating pot when the second coating pot is positioned in the upper part of the first coating pot. The one or more further sink rolls may be smaller than the one or more sink rolls positionable in the first coating pot. Preferably, there is a pair of further sink rolls positionable in the second coating pot. Preferably further, that pair of sink rolls is positionable to accommodate entry and exit of the strip to and from the molten bath in the second coating pot at substantially the same strip orientations as for the first sink roll or rolls when the strip is to be dipped into the molten bath in the first coating pot. The first metal heating means may include electrical induction heaters disposed about the first coating pot. The second metal heating means may include electrical resistance heating means. The electrical resistance heating means may be in the form of electrical resistance heaters extending around the second coating pot. The second coating pot may have steel walls and the electrical resistance heaters may be mounted to the outer surfaces of those walls, Alternatively, the electrical resistance heating means may be in the form of one or more than one electrical resistance heating element located in a housing that is immersed in use in the molten metal of the second coating metal and shields the heating element or elements from contact with the molten metal. with this arrangement, preferably the electrical resistance heating means includes a plurality of heating elements. Preferably the housing is in the form of a plurality of tubes. Preferably one heating element is located in each tube. Preferably each tube extends into the pot from a side wall of the pot. preferably each tube extends through an opening in the side wall. Preferably there is a friction fit between the opening and a section of the tube located in the opening so that there is an effective seal against breakout of the molten metal from the pot. Preferably the opening is tapered inwardly towards the interior of the pot and the section of the tube located in the opening has a corresponding taper. Preferably each tube includes a flange that is welded to the outside surface of the side wall. Preferably the electrical resistance heating means includes a terminal box that is connected to a source of electrical power. Preferably the electrical resistance heating means includes an electrical connection means that connects the heating elements to the terminal box. Preferably each tube extends into the pot from a side wall of the pot but does not reach an opposite side wall of the pot and therefore can accommodate thermal expansion of the tube. Preferably the tubes are at least partially filled with particles, granules or beads of a suitable material which prevent oxidation of the heating elements and which form a barrier to molten material flow in the event that there is a structural failure of one or more than one tube and the molten material penetrates the interior of the tube(s). Preferably the material is a ceramic material. More preferably the ceramic material is Mgo. Preferably the tubes are located close to a base wall of the pot. More preferably the tubes are also located close to opposed side walls of the pot that are perpendicular to the side wall or walls that are connected to the tubes. Preferably the tubes are parallel. Preferably the tubes are in 2 groups/ with one group extending from a first said side wall towards a second said side wall/ and with the second group extending from the second said side wall towards the first said side wall. In order that the invention may be more fully explained on* particularly embodiment will bo described in some detail with reference to the accompanying drawings in / which: Figure 1 is a vertical cross-section through part of a hot-dip coating plant incorporating a main coating pot used for hot dipping steel strip with a zinc-aluminium alloy; / Figure 2 is a cross-section similar to Figure 1 / but showing the plant modified by installation of a secondary shallow coating pot for dip coating the steel strip with an essentially zinc coating; Figure 3 is a cross-section on the line 3-3 in Figure 2; Figure 4 is a detailed plan of one embodiment of the shallow secondary coating pot; Figure 5 is a side-elevation of the secondary coating pot shown in Figure 4; Figure 6 is an end-elevation of the secondary coating pot shown in Figures 4 and 5; Figure 7 is a detailed top plan view of another embodiment of the shallow secondary coating pot; Figure 8 is a cross-section of the secondary coating pot along the line 8-8 of Figure 7; Figure 9 is an operators side elevation of the secondary coating pot; Figure 10 is a cross-section along the line 10-10 of Figure 9; Figure 11 is an enlargement of a lower section of Figure 10 which illustrates the construction of one of the tubes that house electrical resistance heating elements and the positioning of the tube in an opening in a side wall of the secondary coating pot; Figure 12 is a drive side elevation of the secondary coating pot shown in Figures 7 to 11 with side wall covers of the pot removed to illustrate the electrical cabling connecting the electrical resistance heating elements to a terminal box, and Figure 13 is a side elevation of the secondary coating pot that is similar to the side elevation of Figure/ 12 except that it is from the operators side. The illustrated hot-dip coating plant for coating a steel strip 15 comprises a main coating pot denoted generally as 11 to contain a molten coating bath 12 of a zinc-aluminium alloy which may have aluminum content in the range 25 to 70%. coating pot 11 is formed as a large refractory lined, induction heated furnace having outer peripheral metal flow passages 13 and induction heaters 14 to maintain the bath 12 of molten metal in a liquid state. The induction heaters have generally U-shaped metal flow channels 20 encircled by ferromagnetic rings fitted with energising coils so that in use molten metal is caused to flow from passages 13 around the looped inductor channels 20 so as to be inductively heated and jetted back into the bath through passages 13. An induction-heated pre-melt furnace (not shown) is located beside the coating pot 11 and the bath 12 is initially established by pumping pre-melted coating metal from the pre-melting furnace to the coating pot whereafter it is maintained in the molten condition by the operation of induction heaters 14. The steel strip 15 may be annealed before hot dipping into the coating pot so as to soften it for good formability. The strip is supplied from an annealing furnace through a furnace exit chute or snout 16 which dips into the bath of molten metal in the coating pot so that the strip is held in a reducing atmosphere of hot furnace gases without being exposed to air up until the time that it enters the coating bath 12. Figure 1 illustrates the apparatus in a condition for hot dipping the strip 15 into the bath 12 of zinc-aluminum alloy in coating pot 11. For this mode of operation the coating pot 11 is fitted with a large diameter sink roll 17 and the bath 12 is maintained at such a level as to substantially fill the coating pot so that the sink roll 17 is submerged within the bath. The strip 15 passes within the bath around sink roll 17 and is drawn upwardly out of the bath through cooling sprays (not shown), and around elevated turn around rolls (also not shown) which are set at a height sufficient to ensure that full solidification of the metal coating before it engages those rolls. As it leaves the bath 12 the coated strip passes between a pair of gas knives 18 which direct jets of wiping gas onto the coated surfaces of the strip so as to control the coating thickness. The gas knives 18 are mounted on a support frame 19 and can be readily moved to a retracted or remote position when the plant is to be converted for zinc coating in the manner to be described below. Gas knives 18 may be of conventional construction. Alternatively, they may be in the form of floater pads provided with gas knives in the manner described in Australian Patent No. 30281. The hot dip coating plant as thus far described and as illustrated in Figure 1 is conventional. However, in accordance with the present invention the plant may be converted to enable hot dip coating of the strip with a metal coating of a different composition. The conversion involves the positioning of a relatively shallow secondary coating pot 21 within the upper part of the main coating pot 11 and the replacement of the relatively large diameter sink roll 17 with a pair of smaller diameter sink rolls 22 as illustrated in Figures 2 and 3. Secondary coating pot 21 is formed with an upper perimeter frame 23 to rest on the upper rim of the main coating pot 11 and a main tub portion 24 which extends into the upper part of the main coating pot 11. Tub portion 24 is sufficiently shallow that it can be located above a bath of molten metal retained in the main coating pot 11 to a level sufficient to keep the gallery 13 and induction heaters 14 submerged with molten metal. The smaller diameter sink rolls 22 are rotatable between end support arms 28 depending from the main frame of the apparatus and are completely submerged within a. bath 25 of zinc held within the secondary coating pot. The hot zinc bath may initially be established by pumping from a separate pre-melt furnace (not shown) installed beside the main coating pot 11. The zinc pre-melting furnace will usually be separate from the pro-meIt furnace for the zinc-aluminium alloy. The small diameter sink rolls 22 are spaced across the floor of the bath portion 24 of the small coating pot so that the strip 15 can enter and leave the bath 25 in the secondary coating pot 21 with the same strip orientations as those which previously applied when hot dipping into the bath in the main coating pot. Thus the strip can simply be fed with the same strip means through furnace snout 16 into the bath and may be taken away vertically by the strip feed means in the form of a turn around roll (not shown) and between the gas knives 18. in order to maintain the zinc bath 25 in molten condition, the secondary coating pot 21 is provided with electrical resistance heating means. In the embodiment shown in Figured 4 to 6 the electrical resistance heating means are in the form of electrical resistance heaters 31 attached to the outer surfaces of the steel walls of the bath portion 24 of that pot. As illustrated in Figures 5 and 6 heaters 31 may be in the form of electrical resistance heaters extending in parallel formation around the perimeter of the bath portion 24 and connected to supply and return sockets 32, 33. in a typical installation, the secondary coating pot may have a capacity of about 3.5m3 which equates to about 21 tonnes of zinc requiring a heating capacity of up to 300 kWatts to balance heat losses and maintain the zinc bath in a molten state. in the embodiment shown in Figures 7 to 13 the electrical resistance heating means includes an array of parallel heating elements 61 (Figure 8) located in tubes 63 that are immersed in the bath 25 and extend in a direction that is transverse to the direction of movement of strip through the bath 25. The tubes 63 are provided primarily to shield the heating elements 61 from contact with the molten aine of the bath 25. The electrical resistance heating means further includes a plate 81 which protects the tubes 63 and enclosed heating elements 61 from damage that may be caused for example by uncontrolled movement of strip in the secondary coating pot 21. As can be seen in Figures 9, 12 and 13/ the heating means further include a terminal box 67 that is connected to a source of electrical power (not shown) and a series of electrical cables/connectors 87 that connect the heating elements 61 to the terminal box 67. The tubes 63 are located close to a base wall 65 and sloping side walls 83 of the secondary coating pot 21. The tubes 63 are arranged in 2 groups with one group extending through openings 69 in an operators side wall 71 of the coating pot 21 and the other group extending through openings 69 in a drive side wall 73 of the coating pot 21. Each tube 63 extends from the side wall 71, 73 to which it is connected substantially across the coating pot 21 to a position that is a small distance from the opposite side wall 71, 73. This clearance C (Figure 7) accommodates axial thermal expansion of the tubes 63 in the bath 25. Each tube 63 is located in the side wall openings 69 with a tight friction fit so that there is an effective seal between the tubes 63 and the side walls 71, 73. In addition, the side wall openings 69 are tapered and the sections 75 (Figure 11) of the tubes 63 that are located in the openings 69 have a corresponding taper that contributes to the seal. Furthermore, each tube 63 includes a flange 77 (Figure 8) that contacts an exterior surface of the side walls 71, 73 and is welded in place to further contribute to the seal. The tubes 63 are filled with MgO granules (not shown) which prevent oxidation of the heating elements 61 and which will fuse together on contact with molten metal and thereby form a barrier to molten metal flow in the event that zinc metal from the bath 25 penetrates the interior of the tubes 63. The coating pot 21 includes side wall covers 81 (Figures 9, 11) on the side walls 71, 73. The covers 85 shield the exposed end sections of the tubes 63 from contact with zinc-aluminium alloy in the first coating pot 11 and from damage caused by accidental contact with other components of the plant as the coating pot 25 is moved into and from a coating location. in a typical installation, the secondary coating pot may have a capacity of about 3.5m1 which equates to about 21 tonnes of zinc requiring a heating capacity of up to 300 kWatta to balance heat losses and maintain the zinc bath in a molten state. In order to convert the apparatus from the condition shown in Figure 1 in which it is used for coating the strip with a zinc-aluminium alloy to the condition shown in Figure 2 in which it is operable to galvanise the Strip with zinc it is necessary to carry out the following steps: 1. Dip coating of strip 15 with the zinc-aluminium alloy in the main coating pot 11 is stopped. The strip is severed and both ends of the severed strip are held out of the coating pot. 2. The equipment over the upper mouth of main coating pot 11 is moved away, including the sink roll 17 and gas knives 18. 3 . Zinc-aluminium alloy is pumped from or drained from coating pot 11 to reduce the level of the bath within the main coating pot to the level shown in Figure 2 and the furnace snout 16 is removed. 4. The secondary coating pot 21 is brought into position and supported within the upper part of the main coating pot 11 with its lower end close to but above the residual bath of zinc-aluminium alloy in the main coating pot. 5. The smaller diameter sink rolls 22 are installed within the secondary coating pot. 6. The furnace snout 16 and gas wiping knives 18 are brought back into their operative positions. 7. Molten zinc is pumped from the zinc pre-melt furnace into secondary coating pot 21. 8. The strip 15 is threaded through the bath and to the feed rolls and hot dipping with zinc coating proceeds. 9. The electrical resistance heating means of the coating pot 21 is operated as required during the hot dipping to maintain zinc in the bath 25 in a molten state. 10. Induction heaters 14 are operated throughout at a reduced intensity sufficient to maintain the zinc-aluminium metal in coating pot 11 in a liquid state. The present invention enables reasonably simple and rapid conversion of a hot-dip coating plant to coating with different metal coatings or alloys. Because separate coating pots are used for the different coating metals there is no cross contamination of the two. Moreover, the invention enables conversion of existing plants for dual coating operation at moderate expense. WE CLAIM: 1. A method for the continuous hot-dip coating of metal strip in a hot-dip coating plant to change the kind of coating applied to the strip, characterised in that said method comprises the steps of: passing strip through a molten bath of a first coating metal held in a first coating pot and maintained in a molten state by operation of induction heater means having metal flow channels in communication with the bath thereby producing coated strip coated with the first coating metal; stopping the strip coating operation; reducing the level of the molten bath of said first coating metal in the first coating pot to empty an upper part of the first coating pot without disrupting the communication of the induction heater channels with the molten bath; positioning within the emptied upper part of the first coating pot a second coating pot which is shallow relative to the first coating pot and is supported above and without contact with the reduced level of the molten bath of the first coating metal; forming a molten bath of a second coating metal in the second coating pot; and passing strip through the molten bath of the second coating metal in the second coating pot to produce coated strip which is coated with the second coating metal. 2. A method as claimed in claim 1 which comprises connecting the metal flow channels of the induction heater means with the interior of the first coating pot at or below the reduced level of the molten bath therein so that said channels remain filled with the first molten metal throughout coating of the strip with both said first and second coating metals. 3. A method as claimed in claim 1 or claim 2 which comprises forming the molten bath of the second coating metal in the second coating pot by pre-melting said second coating metal and pouring said melted metal into the second coating pot. 4. A method as claimed in any one of the preceding claims which comprises maintaining the molten bath of the second coating metal in a molten state during dip coating of the strip therein by heating the molten bath by the operation of electrical resistance heating means of the second coating pot. 5. A method as claimed in any of the preceding claims which comprises maintaining the first coating metal in a molten state in the reduced level molten bath during hot- dip coating of the strip in the second coating pot by operation of induction heater means 6. A method as claimed in any one of the preceding claims which comprises passing the strip around a first one or more sink rolls in the first coating pot during coating with the first coating metal and passing the strip around an additional one or more sink rolls in the second coating pot during coating with the second coating metal. 7. A method as claimed in claim 6 which comprises removing the first one or more sink rolls from the first coating pot before the second coating pot is positioned in the upper part thereof. 8. A method as claimed in claim 7 which comprises removing the first one or more sink rolls from the first coating pot before the step of reducing the level of the molten bath of the first coating metal. 9. An apparatus for continuous hot-dip coating of metal strip (15), characterised in that said apparatus comprises: a first coating pot (11) to hold a molten bath (12) of a first coating metal; a first metal heating means (14) to heat the bath (12) of molten metal in the first pot (11); a second coating pot (21) to hold a molten bath (25) of a second coating metal, said second pot (21) being shallow in relation to the first pot (11) and being positionable within an upper part of the first but removable therefrom; a second metal heating means (31) operable to heat the molten bath (25) of metal in the second pot (21); and a strip feed means (16) to feed strip (15) into and from the upper part of said first pot (11) when said second pot (21) is removed therefrom whereby to dip the strip (15) in the molten bath (12) of the first coating metal and alternatively operable to feed the strip (15) into and from the molten bath (25) in the second coating pot (21) when the second coating pot (21) is positioned in the upper part of the first coating pot (11) whereby to dip the strip (150 within the bath (25) of the second coating metal. 10. An apparatus as claimed in claim 9 which is provided with a sink roll means (17) to guide the strip (15) within the coating baths (12, 25). 11. An apparatus as claimed in claim 10 wherein the sink roll means (17) has one or more sink rolls or pair of sink rolls (22) positionable in the first coating pot (11) when the second pot (21) is removed to guide the strip (15) within the molten bath (12) in the first coating pot (11) and one or more additional sink rolls (22) positionable in the second coating pot (21) to guide the strip (15) in the molten bath (25) in the second coating pot (21) when the second coating pot (21) is positioned in the upper part of the first coating pot (11). 12. An apparatus as claimed in claim 11 wherein the one or more additional sink rolls (22) positionable in the second coating pot (21) are smaller than the one or more sink rolls (17) positionable in the first pot (11). 13. An apparatus as claimed in any one of claims 9 to 12 wherein the first metal heating means (14) comprises electrical induction heaters disposed about the first coating pot (11). 14. An apparatus as claimed in any one of claims 9 to 13 wherein the second metal heating means (31) comprises an electrical resistance means. 15. An apparatus as claimed in claim 14 wherein the electrical resistance heating means comprises one or more than one electrical resistance heating element (61) located in a housing (63) that is immersed in use in the molten bath (25) of the second coating metal and shields the heating element or elements (61) from contact with the molten metal. 16. An apparatus as claimed in claim 14 wherein the second metal heating means (31) comprises electrical resistance heaters extending around the second coating pot (21). 17. A method for the continuous hot- dip coating of metal strip substantially as herein described. 18. An apparatus for continuous hot-dip coating of metal strip substantially as herein described.

Documents:

3806-del-1998-abstract.pdf

3806-del-1998-assignment.pdf

3806-del-1998-claims.pdf

3806-del-1998-correspondence-others.pdf

3806-del-1998-correspondence-po.pdf

3806-del-1998-description (complete).pdf

3806-del-1998-drawings.pdf

3806-del-1998-form-1.pdf

3806-del-1998-form-13.pdf

3806-del-1998-form-19.pdf

3806-del-1998-form-2.pdf

3806-del-1998-form-3.pdf

3806-del-1998-form-4.pdf

3806-del-1998-form-6.pdf

3806-del-1998-gpa.pdf