The present invention relates to apparatus for the coating of molten metal onto steel. More specifically it relates to bubble pumps used in molten metal baths to remove surface dross from the molten metal in the vicinity of the steel strip being coated. Most specifically it relates to protection of the interior of such bubble pumps from attach attack and destruction by the molten metal.
Molten aluminum and molten zinc have been used for years to coat the surface of steel. One of the coating process steps is to immerse the steel sheet in the molten aluminum or molten zinc. The surface quality of coating is very important to produce high quality coated products. However, introduction of aluminized steel for the US market in 2007 was quite a challenge for the aluminizing lines. Early trials resulted in >50% rejects due to coating defects.
One of the major sources of defects was dross floating on the aluminum bath within the snout and sticking to the strip. To achieve high quality surface finish, floating dross and oxides in the molten metal bath, especially in the confined regions inside the snout, need to be diverted from the surface being coated. Carbon steel pneumatic dross pump, also referred to as bubble pump, has been used to remove the dross from the coating zone. Implementing push and pull snout pumps to ensure a dross-free melt surface inside the snout made high quality coating possible. The bubble pump (a.k.a. dross pump) uses the artificial lift technique of raising a fluid such as water or oil (or in this case molten metal) by introducing bubbles of compressed gases, air, water vapor or other vaporous bubbles into the outlet tube. This has the effect of reducing the hydrostatic pressure in the outlet tube vs. the hydrostatic pressure at the inlet side of the tube. The bubble pump is used in the molten metal bath of the metal coating lines to remove floating dross from surface of the aluminizing bath inside the snout in order to prevent dross-related defects on the coated strip. Thus, the bubble pump is a critical hardware component in the production of high quality automotive aluminized sheet.
One of the major factors impacting production costs is aluminizing pot hardware failures. Prominent among hardware failures is the failure of the bubble pump (pull pump). The average service life of bubble pumps made of carbon steel is 8-12 hours, resulting in the use of 35-40 pumps every month (for a 2 week production). The change of carbon steel bubble pumps during production leads to production disruption and contamination of molten metal bath. In addition, the “quality” of the coated steel sheet must be downgraded (resulting in a less valuable product) during carbon steel pump changes. Further, pump changes require line stops and restarts, leading to excessive consumption of startup coils. Average losses attributable to bubble pumps are about close to a million U.S. dollars per year. An increase in life of the bubble pump will significantly reduce the quantity of downgraded sheet, and will reduce downtime and costs.
Thus, there is a need in the art for bubble pumps for use in molten aluminum baths that can last significantly longer than bare carbon steel tube pumps.
The present invention provides a bubble pump having an interior formed from a material that is resistant attack by molten aluminum. The interior surface may be formed from a ceramic. The ceramic may be selected from the group consisting of alumina, magnesia, silicate, silicon carbide, or graphite, and the mixtures. The ceramic may be a carbon-free, 85% Al2O3 phosphate bonded castable refractory.
The exterior of the bubble pump may be formed from carbon steel tubing. The bubble pump may be formed from multiple sections of tubing bound together. The bubble pump may include 3 straight pieces of tubing and 3 elbow pieces of tubing. The multiple sections of tubing may be bound together by compression flange joints. The compression flange joints may compress the interior ceramic material such that molten aluminum cannot penetrate the joint. The compression flange joints of the interior material that is resistant attack by molten aluminum may form a 45 degree angle male/female joint between sections of bubble pump.
A preferred embodiment of the present invention will be elucidated with reference to the drawings, in which:
The present inventors sought to develop a way to improve the pump performance and significantly increase service life of the pumps, preferable to at least five days. Extensive investigations of the failure modes of the carbon steel bubble pumps were conducted. Based on the results, the present inventors have developed an improved bubble pump with a cast ceramic protective lining. One embodiment of the improved pump has lasted continuously up to 167 hours (˜7 days) without failure, demonstrating a major performance advantage over the 8-12 hours of service life normally experienced with the carbon steel pumps in molten aluminum. Changes in pump design and the incorporation of a cast refractory lining are the key factors in the improvement.
Analysis of Failure Mode
The U-shaped bubble pump operates in the melting pot at a temperature of 668° C. (1235° F.). The chemistry of the melt is typically Al-9.5% Si-2.4% Fe. The inlet of the pump is positioned within the molten aluminum bath, inside the snout and the outlet is positioned on the outside of the snout. Pumping action is created by bubbling nitrogen in the vertical leg of the pump on the outlet side. Nitrogen at ambient temperature is introduced at 40 psi and at flow rates of ˜120 standard cubic feet per hour (scfh, 90-150 scfh). Expansion of the nitrogen creates bubbles that escape through the outlet expelling simultaneously liquid metal. The expulsion creates a pressure difference between the two sides of the pump, generating suction that allows the melt and floating dross to be sucked in at the inlet. The process is continuous, thereby enabling continuous removal of dross from the inside of the snout and expulsion to the outside.
There are three main areas of failure in the bubble pumps, in order of severity: 1) within the discharge head (elbow 6); 2) around the nitrogen inlet nipple in vertical section on the outlet side (vertical piece 5); and 3) in the middle of vertical section on the inlet side (vertical piece 1). In order to better understand the mode of failure, a regular carbon steel pump that failed after about 12 hours of service was split in half and analyzed. Analysis shows that the horizontal bottom part of the pump is almost intact, while the inlet and outlet sections are severely damaged. Also, the material loss occurs mostly on inside of the bubble pump, while the outside diameter remains unchanged. The degree of attack is different in different locations of the pump.
Water Modeling of the Bubble Pump
The inventors believed that fluid dynamics inside the pump affected the failure mode. However, design factors which influenced the fluid flow were not well understood. In order to investigate the influence of melt turbulence, a small Plexiglas bubble pump model (1:2 scale) was built and operated in water. The model allowed the investigation of the effect of gas pressure, inlet position, the elbow radius, orientation and shape of the outlet on pump operation and performance. The water flow characteristics in the pump during normal operation were ascertained and it was determined that the locations of corrosion and metal loss observed in the failed pumps correspond to the locations of turbulence inside the water model.
Mechanism of Aluminum Attack
The mechanism of material loss in the carbon steel pump was investigated by metallographic techniques. There are several stages of aluminum attack. In the first moments of aluminum contact with the pump, a hard and brittle intermetallic layer forms on the inside wall as a result of the reaction between the liquid aluminum and steel surface. This layer substantially restricts the diffusion of aluminum and iron through it and limits further attack on steel. The intermetallic layer thus serves as a quasi-protective coating on the metal body. However, whenever mechanical stresses appear on the surface, this brittle layer develops micro-cracks and spalls off the steel surface, creating deep pits. Because the bottom of the pit is no longer protected by the intermetallic layer, it is attacked by the melt until a new layer is formed. This process repeats itself while the stresses continue to be present on the steel surface and the loss of metal will continue to increase as a result. The stresses involved in the attack are likely to be the result of melt turbulence and/or impingement of foreign particles at susceptible locations. The process of attack can therefore be characterized as dynamic erosion by the liquid aluminum.
Thus, the failure of carbon steel bubble pumps in service is by dynamic pitting and abrasive wear (dynamic erosion). The degree of attack is different at different locations. The outer surface of pump, being not exposed to melt turbulence, suffers less damage and therefore survives in the melt with minimal protection. The melt attack and metal loss progresses mostly from the inside outward.
The present inventors have determined that coatings which can withstand molten aluminum attack in stagnant melts are likely to fail under turbulence conditions experienced in the pump. Strong coating adhesion to pump body is crucial for protection under such dynamic conditions. The inventors have further determined that in order to improve the pump performance it is necessary to isolate the inside surface of the pump from molten aluminum. The isolating layer must be adherent, thick and continuous. Any opening in the protective layer could lead to the pump failure.
Selection of Refractory Material for Protective Lining
Based on the knowledge from failure investigation and water modeling the present inventors developed a new bubble pump. The requirements for protective lining materials were: 1) non-wetting materials against liquid aluminum penetration; 2) thermal shock resistant materials to avoid preheating; 3) erosion resistant materials; 4) low cost; and 5) design flexibility. In order to meet the requirements, a literature search and laboratory testing were performed. A carbon-free, 85% Al2O3 phosphate bonded castable refractory was selected.
Design of Inventive Pump
The shape of the standard carbon steel bubble pump contains three 90 degree elbow sections. The complicated shape makes it very difficult to cast the ceramic lining inside the entire shell without joints. It was therefore necessary to cut the shell into several sections, cast each section separately and assemble the pump subsequently. It is also necessary for the joint of each assembled part to maintain integrity during use. To address these stringent requirements, the following ideas features were applied in assembling the pump: 1) unique 45 degree angle male/female joints between sections of refractory lining; 2) two flange joints to assemble the three pieces of the pump, allowing the joints of the ceramic protective lining to be placed under compression; 3) continuous ceramic lining in elbows to reduce aluminum attack through joints; and 4) flange modification in the outlet area to put the ceramic lining under compression.
The compression joints are used to maintain the protective lining joint under compression to seal off the protective lining joint against molten metal penetration. The protective lining may be formed from any material that is resistant to attack by molten aluminum, such as non-wetting materials against molten metals. Examples of the non-wetting materials include alumina, magnesia, silicate, silicon carbide, or graphite, and the mixtures of these ceramic materials.
Filing Document | Filing Date | Country | Kind |
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PCT/US2013/036500 | 4/12/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2013/155497 | 10/17/2013 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
3606291 | Schneider | Sep 1971 | A |
4522926 | Felice | Jun 1985 | A |
5203910 | Areaux et al. | Apr 1993 | A |
5650120 | Morando | Jul 1997 | A |
5735935 | Areaux | Apr 1998 | A |
5863314 | Morando | Jan 1999 | A |
6039917 | Morando | Mar 2000 | A |
6051183 | Morando | Apr 2000 | A |
6068812 | Areaux et al. | May 2000 | A |
6355206 | Hanzawa et al. | Mar 2002 | B1 |
7470392 | Cooper | Dec 2008 | B2 |
20020148328 | Holz | Oct 2002 | A1 |
20070253807 | Cooper | Nov 2007 | A1 |
20110049878 | Goode | Mar 2011 | A1 |
20150104333 | Lee | Apr 2015 | A1 |
Number | Date | Country |
---|---|---|
101592186 | Dec 2009 | CN |
0808914 | Nov 1997 | EP |
S5747860 | Mar 1982 | JP |
S59169971 | Sep 1984 | JP |
S6212653 | Jan 1987 | JP |
H0734209 | Feb 1995 | JP |
H09137265 | May 1997 | JP |
H10273763 | Oct 1998 | JP |
H10277726 | Oct 1998 | JP |
H11199334 | Jul 1999 | JP |
H11256298 | Sep 1999 | JP |
H11279729 | Oct 1999 | JP |
2000119834 | Apr 2000 | JP |
2000351672 | Dec 2000 | JP |
2001158659 | Jun 2001 | JP |
2001335906 | Dec 2001 | JP |
2011168832 | Sep 2011 | JP |
2247289 | Feb 2005 | RU |
358851 | Dec 1972 | SU |
1682409 | Oct 1991 | SU |
Entry |
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Machine translation of SU 358851 A1, Dec. 20, 1972. |
Number | Date | Country | |
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20150104333 A1 | Apr 2015 | US |
Number | Date | Country | |
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61624042 | Apr 2012 | US |