CN202519322U - Circulating cooling deslagging device in continuous hot-dip galvanizing aluminum - Google Patents

Abstract

The device for cyclic cooling and deslagging of the utility model is a cyclic cooling and slag removal device for continuous hot-dip galvanized aluminum. It is that: the inside of the circulating cooling and deslagging device is a circuitous tank with openings at both ends, the bottom of the circulating cooling and slag removing device is a zinc slag collector, and a built-in low-temperature and low-melting point melting tank with an inlet and an outlet is built in the circuitous tank. The honeycomb cooling pipe of the metal liquid, the zinc-aluminum liquid driving device is installed at the entrance of the detour tank to drive the zinc-aluminum liquid from the detour tank entrance into the detour tank, and the zinc-aluminum liquid flows naturally back to the galvanized zinc pot from the detour tank outlet. The above structure stabilizes the product quality of the hot-dip galvanized steel sheet, guarantees the quality of the hot-dip galvanized steel sheet, expands the application range of the product, reduces the loss of zinc and aluminum, and has considerable social and economic benefits.

Description

A continuous hot-dip galvanized aluminum circulation cooling and deslagging device

technical field

The utility model relates to the technical field of metal smelting, in particular to a continuous hot-dip galvanized aluminum circulation cooling and deslagging device. the

Background technique

Hot-dip galvanizing is a more effective and convenient steel anti-corrosion method. Its coating has excellent sacrificial anti-corrosion effect; The characteristics and cathodic protection characteristics of zinc, the performance of the coating is superior to that of a single element coating, and the anti-corrosion performance is several times higher than that of pure zinc coating, so it is widely used. Because galvanized aluminum sheets, such as Galvalume coated steel sheets, have excellent comprehensive properties and Beautiful appearance, there is a tendency to replace aluminum-coated sheets and some galvanized steel sheets with this coated sheet abroad, forming a zinc-aluminum alloy coating heat, and its products are mainly used in the construction industry, automobile industry, household appliances and agriculture. the

At present, a serious problem on the hot-dip galvanizing production line is the zinc slag problem. Due to the high aluminum content of the zinc-aluminum alloy coating, compared with the zinc bath of hot-dip pure zinc, the composition of the zinc bath has changed greatly, especially When silicon and other elements are added to the zinc-aluminum pool, the phase relationship will become more complicated. The zinc slag phase in the zinc-aluminum-zinc pool is FeAl ₃ containing zinc and Fe-Al-Si intermetallic compound. The density of the zinc-aluminum pool is smaller than that of hot-dip pure zinc, and the density of the 55% Al-Zn zinc-aluminum pool is about 1/2 of that of hot-dip pure zinc; therefore, it is easier to form suspended slag and Bottom dross and zinc dross are much more complex than those in hot-dip pure galvanized zinc baths. Many typical Galvalume production lines currently have zinc dross problems that plague people. For example, Bluescope Steel in Australia has three Galvalume production lines. Serious zinc slag problem, many domestic Galvalume production lines also have zinc slag problem.

The main problems of zinc-aluminum products are defects such as bright spots, zinc particles, zinc scars, uneven spangles, indentations, and reduced formability of the coating. Among them, bright spots, zinc particles, and zinc scars are mainly caused by zinc slag, especially suspended slag. The influence of zinc slag is the greatest. The adsorption of zinc slag on the sinking roller and stabilizing roller will cause uneven spangles or slag printing defects on the coating, and the zinc slag will have a negative impact on the formability of the coating. At the same time, the formation of bottom slag will cause aluminum zinc liquid waste of resources and increase production costs. In addition, the bottom slag accumulated at the bottom of the aluminum-zinc liquid is very difficult to remove, and regular production shutdowns must be carried out for salvage, which seriously affects production efficiency. If the zinc slag in the zinc pool can be removed by some method, It will greatly reduce the impact of zinc slag in the zinc pool on product quality, and has extremely important significance for improving the quality of galvanized aluminum products and expanding the application range of products. the

Contents of the invention

The purpose of this utility model is to provide a slag removal device used in the zinc-aluminum molten pool in continuous galvanizing production. A circulating cooling device is installed in the zinc-aluminum liquid inside the galvanizing pot, and the zinc slag is melted in the zinc-aluminum liquid. When the temperature of the body decreases, the precipitation will grow up and precipitate, so as to achieve the purpose of continuously removing the zinc slag in the zinc pool. the

Inside the circulation cooling and cooling device is a circuitous tank, which drives the zinc-aluminum liquid to flow through the circuitous channel. The circuitous channel is embedded with a cooling tube, and the tube is continuously filled with low-temperature molten metal. The inside of the cooling tube adopts a unique honeycomb structure, which effectively improves the heat exchange capacity. , to improve the cooling effect of the zinc-aluminum liquid outside the tube, the design width of the circuitous groove is 10-12cm, the design width of the embedded cooling pipe is 5-6cm, the height of the embedded cooling pipe and the circuitous groove is equal, and the narrow and long design of the circuitous groove is conducive to stabilizing the inside of the tank The flow of the zinc-aluminum liquid and prolong the time for the zinc-aluminum liquid to flow through the cooling and cooling device. The design width of the cooling pipe is half of the width of the roundabout groove, and the height is equal, which can enhance the cooling effect of the zinc slag in the device and have sufficient time When the cooling precipitate grows, the flow direction of the zinc-aluminum liquid in the circuitous tank is opposite to the flow direction of the low-temperature molten metal liquid in the cooling tube, so that the cooling of the zinc-aluminum liquid can achieve the best effect. the

The zinc slag in the zinc pool will cause defects such as bright spots, zinc particles, zinc scars, uneven spangles, indentations, and reduced formability of the coating during continuous galvanizing. The slag removal method, after the zinc slag is cooled and precipitated to grow, is settled and collected in the zinc slag collector at the bottom of the slag removal device, which can continuously and effectively reduce the zinc slag in the zinc pool, and reduce the continuous galvanized sheet bright spots, zinc particles, zinc scars, and zinc slag. In order to reduce the influence of zinc slag in the zinc pool on the quality of the coating and improve product quality, the online continuous deslagging of the zinc pool will reduce the time for stopping the machine to remove the slag. Reduce the consumption of zinc and aluminum raw materials, effectively improve production efficiency and reduce production costs. the

In order to achieve the above object, the utility model is realized through the following technical solutions:

A cyclic cooling and deslagging device for continuous hot-dip galvanized aluminum. The cyclic cooling and slag removal device is located in the zinc-aluminum liquid inside the galvanizing pot. It is characterized in that: the interior of the cyclic cooling and slag removal device is A detour tank with openings at both ends, the bottom of the circulating cooling and slag removal device is a zinc slag collector, a honeycomb cooling pipe with an inlet and an outlet and a low-temperature and low-melting molten metal liquid is built in the detour tank, and zinc is installed at the entrance of the detour tank. The aluminum liquid driving device drives the zinc-aluminum liquid to enter the circuitous tank from the entrance of the circuitous tank, and the zinc-aluminum liquid flows naturally back to the galvanized zinc pot from the circuitous channel exit.

The above-mentioned cyclic cooling and deslagging device for continuous hot-dip galvanized aluminum is characterized in that: the top of the cyclic cooling and slag removing device is 20-40 cm lower than the zinc-aluminum liquid level of the galvanizing pot. the

All components of the circulating cooling and slag removal device are made of steel frame structure, covered with stainless steel, refractory clay and other heat-resistant and corrosion-resistant materials; the honeycomb cooling pipe is made of copper structure covered with heat-resistant, corrosion-resistant and heat-resistant materials such as stainless steel with excellent thermal conductivity . the

The above-mentioned device for circulating cooling and cooling slag in continuous hot-dip galvanized aluminum is characterized in that: the width of the circuitous groove is 10-12 cm, and the depth is 30-60 cm; the entrance and exit adopt a circular or square structure, and the entrance And the outlet cross-sectional area is 50-80cm ² .

The above-mentioned device for circulating cooling and deslagging in continuous hot-dip galvanized aluminum is characterized in that the cooling pipe adopts a square pipe, the width is half of the width of the detour groove, and the height is equal to the depth of the detour groove. the

The above-mentioned continuous hot-dip galvanized aluminum circulation cooling and slag removal device is characterized in that: the inlet of the honeycomb cooling pipe is continuously pressed into a low-temperature and low-melting point molten metal liquid to meet the needs of cooling the zinc-aluminum liquid in the circuitous tank. According to the requirements, after the zinc-aluminum liquid in the circuitous tank is cooled, the molten metal flows out from the outlet of the cooling pipe for recycling and reuse. the

A method for circulating cooling and cooling slag removal in continuous hot-dip galvanized aluminum, which is characterized in that a circulating cooling cooling and slag removal device is installed in the zinc-aluminum liquid inside the galvanized galvanizing pot, and the inside is a circuitous tank with openings at both ends. A honeycomb cooling pipe with an inlet and an outlet is embedded in the tank; the zinc-aluminum liquid is driven to enter the circuitous tank from the entrance of the circuitous tank. Cool the zinc-aluminum liquid in the roundabout tank, lower the temperature of the zinc-aluminum liquid to cause the zinc dross to grow up from the zinc-aluminum liquid, and settle in the zinc dross collector at the bottom of the slag removal device. The zinc-aluminum liquid after the zinc-aluminum liquid is separated passes through The outlet of the detour tank flows back to the galvanized zinc pot to complete the slag removal and purification of the zinc-aluminum liquid. the

The above-mentioned method for continuously hot-dipping galvanized aluminum with circular cooling and cooling for deslagging is characterized in that: the zinc-aluminum liquid in the galvanized zinc pot flows into the detour tank by means of electromagnetic drive. the

The above-mentioned method for cyclic cooling and slag removal in continuous hot-dip galvanized aluminum is characterized in that: the temperature of the zinc-aluminum liquid in the detour tank of the cyclic cooling and slag removal device is lower than that of the zinc-aluminum liquid in the galvanized zinc pot The temperature is 20-50°C. the

The above-mentioned method for continuously hot-dipping galvanized aluminum by circulating cooling and lowering the temperature to remove slag is characterized in that: the flow rate of the zinc-aluminum liquid in the circuitous tank is 50-500kg/min. the

The above-mentioned method for continuously hot-dipping galvanized aluminum by circulating cooling and cooling to remove slag is characterized in that 20-60% of the zinc slag in the zinc-aluminum liquid is cooled, precipitated and precipitated. the

The above-mentioned method for continuous hot-dip galvanized aluminum circulation cooling and deslagging method is characterized in that: the low-temperature and low-melting-point molten metal liquid includes tin and zinc. the

The above-mentioned method for cyclic cooling and deslagging in continuous hot-dip galvanized aluminum is characterized in that the flow direction of the zinc-aluminum liquid in the detour tank is opposite to the flow direction of the low-temperature molten metal liquid in the cooling pipe. the

The concrete implementation steps of described device are:

(1) From the inlet of the honeycomb cooling pipe, the molten metal with low temperature and low melting point is continuously pressed into the honeycomb cooling pipe. Cooling requirements, and outflow from the outlet for recycling;

(2) The driving device at the entrance of the detour tank drives the zinc-aluminum liquid in the galvanizing pool into the detour tank, and the flow rate of the zinc-aluminum liquid in the detour tank is 50-500kg/min;

(3) Use the honeycomb cooling pipe to reduce the temperature of the zinc-aluminum liquid in the detour tank, and the temperature in the detour tank of the circulating cooling device is 20-50 °C lower than the temperature of the zinc-aluminum liquid in the galvanized zinc pot;

(4) When the temperature of the zinc-aluminum liquid in the circuitous tank decreases, the zinc dross precipitates from the zinc-aluminum liquid and grows up, and settles to the zinc dross collector set at the bottom;

(5) During the flow of the zinc-aluminum liquid in the circuitous tank, 20-60% of the zinc slag is cooled and precipitated, and flows back to the galvanized zinc pool through the circuitous tank outlet to complete the slag removal and purification of the zinc-aluminum liquid;

(6) During the continuous slag removal process, the zinc slag in the bottom zinc slag collector continues to increase, and when it reaches a certain amount, it can be cleaned online or by suspending the slag removal.

The utility model provides a slag removal device for continuous hot-dip galvanized aluminum. The slag removal process is completed in the cyclic cooling and slag removal device, which can be applied to the inside and outside of the continuous production line. Under the action of pressure, the molten metal with low temperature and low melting point is pressed into the honeycomb cooling pipe, and flows through the honeycomb cooling pipe at a certain speed to meet the requirement of cooling the zinc and aluminum liquid in the roundabout tank, and flows out from the outlet for recycling and reuse , under the action of driving force such as electromagnetic drive, the zinc-aluminum liquid flows through the entrance of the detour tank and flows into the detour tank. The zinc-aluminum liquid cools down under the action of the honeycomb cooling tube and precipitates zinc slag, which grows up and precipitates only in the zinc slag collector at the bottom , and the zinc-aluminum liquid after cooling down and removing slag is naturally returned to the galvanized zinc pot through the outlet of the circuitous tank, reducing the content of zinc dross in the zinc-aluminum liquid in the galvanized zinc pot, and providing a clean zinc pool for the production of high-quality hot-dip galvanized steel sheets Environment, reduce zinc slag defects in hot-dip galvanized aluminum steel sheets from the source, stabilize product quality of hot-dip galvanized steel sheets, provide guarantee for providing high-quality hot-dip galvanized steel sheets, expand product application range, reduce zinc and aluminum loss, and have considerable social and economic benefits. the

Description of drawings

The accompanying drawings described here are used to further explain the utility model and constitute a part of the application. The schematic diagrams of the utility model are used to explain the utility model and do not constitute improper limitations to the utility model. The scope of protection is not limited to the following schematic diagram;

In the attached picture:

Fig. 1 is the schematic diagram of the cross section of the utility model circulation cooling deslagging device;

Fig. 2 is a schematic diagram of the longitudinal section at A of the circulating cooling and deslagging device of the present invention;

Fig. 3 is a schematic diagram of the longitudinal section at B of the circulating cooling and deslagging device of the present invention;

Figure 4 is a schematic diagram of the hot-dip galvanizing process of the steel plate and the equipment position of the circulating cooling and deslagging device;

Fig. 5 is a cross-sectional schematic diagram of the inlet of the detour tank of the circulating cooling and slag removal device of the utility model.

[0024] Drawing number: [1] Galvanized zinc pot [2] Detour slot entrance [3] Zinc-aluminum liquid driving device [4] Cooling pipe outlet [5] Detour Slot [6] Circulating cooling and deslagging device [7] Cooling tube inlet [8] Low temperature molten metal driving device [9] Detour slot exit [10] Zinc dross [11] Cooling tube [12] Low temperature molten metal [13] Liquid zinc and aluminum [14] Air Knife [15] Strip steel [16] Sinking roller [17] Zinc level [18] Zinc slag collector.

Detailed ways

Introduce this embodiment in detail below in conjunction with the accompanying drawings: this embodiment is implemented under the premise of the technical solution of the utility model, and detailed implementation methods and processes are provided, but the protection scope of the utility model is not limited to the following Described embodiment. the

As shown in Figures 1-3, the continuous hot-dip galvanized aluminum circulation cooling and deslagging device 6 is located in the galvanizing bath 13 of the galvanizing pot 1, and the installation position of the circulating cooling and deslagging device 6 is lower than The height of the zinc liquid level 17 in the galvanized zinc pot is h, and the height difference is 20 to 40 cm; the hot-dip galvanizing process of the steel plate is completed in the galvanized zinc pot 1, and the circulating cooling and slag removal device 6 is used for cooling and slag removal, and the circulating cooling Inside the cooling and slag removal device 6 is a detour tank 5, the two ends of the detour tank 5 are the detour tank inlet 2 and the detour tank outlet 9, and the zinc-aluminum liquid 13 enters the detour tank 5 through the detour tank entrance 2 under the action of the zinc-aluminum liquid driving device 3 After the slag removal is completed, it flows back to the galvanized zinc pool 1 from the outlet 9 of the detour tank. The detour groove 5 is embedded with a cooling pipe 11. The cooling pipe 11 has a honeycomb structure. The cooling pipe 11 includes the cooling pipe inlet 7 and the cooling pipe outlet 4. The low-temperature molten metal 12 is driven from the cooling pipe The inlet 7 enters the cooling pipe 11, and then flows out from the cooling pipe outlet 4 for recycling. the

The galvanized zinc pot 1 is heated by electromagnetic induction heating at a temperature of 580-620°C. Liquid low-temperature metal liquid 12 (tin, zinc, etc.) is continuously pressed into the cooling pipe 11 at a temperature of 200-450°C. 12 When flowing through the cooling pipe 11, the heat of the zinc-aluminum liquid 13 flowing in the detour tank 5 is taken away, the temperature of the zinc-aluminum liquid 13 in the detour tank 5 is reduced by 20-50°C, and a large amount of zinc slag is released from the zinc-aluminum liquid 13 with lowered temperature The precipitation grows up and settles in the zinc slag collector 18 located at the bottom. After the zinc-aluminum liquid 13 is cooled to remove slag, it flows back to the galvanizing zinc pot 1 through the outlet 9 of the detour tank to complete the process of removing slag from the zinc-aluminum liquid. The zinc-aluminum liquid 20-60% of the zinc slag is cooled and precipitated. the

It can be seen from the above-mentioned implementation examples that the method for cyclically cooling and cooling the slag in the continuous hot-dip galvanized aluminum of the utility model utilizes the method for cyclically cooling and cooling the zinc-aluminum liquid to effectively remove the zinc slag in the zinc-aluminum liquid, and to provide high-quality hot-dip galvanized aluminum. The dip-galvanized steel plate provides a clean zinc pool environment, fundamentally avoids the occurrence of zinc slag defects in the hot-dip galvanized aluminum steel plate, stabilizes the product quality of the hot-dip galvanized steel plate, provides a guarantee for providing high-quality hot-dip galvanized steel plates, and expands product applications range, while reducing the loss of zinc and aluminum, bringing considerable social and economic benefits. the

Claims (4)

1. A continuous hot-dip galvanized aluminum circulation cooling and deslagging device, the circulating cooling and deslagging device is located in the zinc-aluminum liquid inside the galvanized zinc pot, characterized in that: the circulating cooling and deslagging device The interior is a detour tank with openings at both ends. The bottom of the circulating cooling and slag removal device is a zinc slag collector. A honeycomb cooling pipe with an inlet and an outlet and a low-temperature and low-melting molten metal liquid is built in the detour tank. The entrance of the detour tank is The zinc-aluminum liquid driving device is set to drive the zinc-aluminum liquid to enter the circuitous tank from the entrance of the circuitous tank, and the zinc-aluminum liquid flows naturally back to the galvanized zinc pot from the circuitous channel exit. 2. A continuous hot-dip galvanized aluminum circulation cooling and deslagging device according to claim 1, characterized in that: the top of the circulating cooling and deslagging device is lower than the zinc-aluminum liquid level of the galvanizing pot 20-40cm. 3. A device for continuous hot-dip galvanized aluminum circulation cooling and deslagging as claimed in claim 1, characterized in that: the width of the detour groove is 10-12cm, and the depth is 30-60cm; the entrance and exit adopt Circular or square structure, the cross-sectional area of the inlet and outlet is 50-80cm ² . 4. A device for circulating cooling and deslagging in continuous hot-dip galvanized aluminum as claimed in claim 1, characterized in that: the cooling pipe adopts a square pipe, the width is half of the width of the detour groove, and the height is equal to the depth of the detour groove .

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