Information
-
Patent Grant
-
6761936
-
Patent Number
6,761,936
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Date Filed
Thursday, May 9, 200223 years ago
-
Date Issued
Tuesday, July 13, 200420 years ago
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Inventors
-
Original Assignees
-
Examiners
Agents
-
CPC
-
US Classifications
Field of Search
US
- 427 431
- 427 433
- 427 319
- 427 321
- 427 329
- 118 419
- 118 429
- 118 66
- 118 67
- 118 68
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International Classifications
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Abstract
A method for hot dip galvanizing of hot-rolled steel strip, wherein in a first method step, the strip (50) is introduced into a pickling station (10-13) and a layer of scale and reaction products are removed from the strip surface in the pickling station. In another method step, the strip (50) is introduced into a rinsing station (21-23) and residues of the pickle and pickling products are removed from the strip surface in the rinsing station, and subsequently the strip is introduced into a drying station and is dried. And from there, in another method step, the strip is introduced into a furnace (40) and is adjusted to galvanizing temperature under a protective gas atmosphere. In a last method step, the strip is guided through a galvanizing bath and the surface of the (50) is coated with a hot dip galvanizing layer in the galvanizing bath, wherein the strip temperature in the furnace (40) is adjusted at most to 50° K. above immersion temperature of the strip (50) into the zinc bath.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to a method and an installation for hot dip galvanizing of hot-rolled steel strip, wherein, in a first method step, the strip is introduced into a pickling station and a layer of scale and reaction products are removed from the strip surface in the pickling station. In a second method step, the strip is introduced into a rinsing station and residues of the pickle and pickling products are rinsed from the strip surface in the rinsing station, and subsequently, the strip is introduced into a drying station and is dried in the drying station. From the drying station, the strip is introduced into a furnace in another method step and is adjusted to galvanizing temperature in the furnace under a protective gas atmosphere. In a last method step, the strip is guided through a galvanizing bath and the surface of the strip is coated in the galvanizing bath with a hot dip galvanizing layer.
2. Description of the Related Art
Hot dip coating, particularly hot dip galvanizing, of hot-rolled steel strip, so called hot strip, is becoming economically increasingly more important as compared to conventional cold strip hot dip galvanizing. As a result of the development of thin slab technology in hot-rolled strip, there is the technical possibility of producing hot strips in the thickness range of below 1.2 mm from casting heat. There is the additional possibility to substitute cold strip for comparatively inexpensive hot strip in dependence on the requirements of the customer.
Different methods and installations for hot dip coating, particularly hot dip galvanizing, of steel strip are known. They are predominantly types of installation in which cold-rolled strips are used.
In such installations, the actual coating process is preceded by an annealing furnace in which a structural transformation takes place at high temperatures for obtaining the desired mechanical properties. The existing temperature difference between the melt bath, preferably zinc or zinc alloys, and the maximum strip temperature may be up to 400° C. However, hot dip galvanizing cannot be carried out with this overheated strip, so that the strip must be cooled prior to coating to temperatures close to the melt bath temperature.
In contrast, hot strip or preheated cold strip do not require annealing for influencing the mechanical properties; rather, the strip temperature is merely adjusted to that of the melt bath in order to achieve the desired reaction of the steel strip surface with the alloying components of the melt bath. In contrast, high temperature annealing is frequently disadvantageous for the mechanical properties of the strip.
The present invention relates exemplary exclusively to the various methods of hot strip hot dip refining or hot strip hot dip galvanizing.
The desired temperature level, particularly for hot strip hot dip galvanizing, is in the previously operated installations for hot dip galvanizing still always higher than the required 450° C. of the zinc bath. The reason for this is the required removal of all oxidation products and their prior stages from the steel strip surface. Oxidation products are inevitably produced in the transition area from the pickling stage through the rinsing and drying stage into the furnace entrance due to the influence of ambient oxygen. The quantity and formation of the oxidation products entering the furnace and the ambient oxygen entrained by the strip determine the necessary method parameters of the treatment procedure, characterized by a required reduction potential, temperature level and holding time. The temperature level which is used is frequently so high that the strip must be additionally cooled prior to entering the zinc bath.
Another method of operation is characterized by a significant increase of the temperature level in the zinc bath to values above 460° C. A particular disadvantage of this type of method is the increased production of zinc-containing slag. On the one hand, this leads to increased material and operating costs for the zinc bath and, on the other hand, to a reduced quality of the strip.
SUMMARY OF THE INVENTION
Starting from the prior art mentioned above, the invention is based on the object of providing a method and a hot strip hot dip galvanizing installation which overcome the disadvantages and difficulties discussed above and produce hot dip galvanized steel strip having a high and defect-free surface quality with an economical amount of material and operating costs.
For meeting this object, the invention proposes to adjust the strip temperature in the furnace at most to 50° K. above immersion temperature in the zinc bath.
The H
2
concentration in the furnace is advantageously adjusted to at most 20% and preferably to less than 5%. It is useful to carry out the method steps between the last rinsing stage of the rinsing station through the drying station up to the entrance of the heating furnace hermetically screened from the ambient oxygen from the surroundings.
Consequently, an installation for carrying out the method according to the invention provides that the outlet of the last rinsing stage of the rinsing station is connected to the inlet of the drier and the outlet of the drier is connected to the inlet of the furnace by locks and are hermetically sealed from the ambient atmosphere.
Additional useful further developments of the method and of the hot dip galvanizing installation for hot strip are provided in accordance with the features of subclaims.
The method and the installation according to the invention advantageously ensure that the optimum surface condition of the strip achieved after passing the strip through the pickling station and the rinsing station is preserved in the subsequent drying stage as well as during the transition in the furnace areas and from the furnace into the galvanizing bath.
This is achieved by:
the above-mentioned adjustment of the temperature of the strip in the furnace,
direct coupling of at least the last rinsing stage of the rinsing station through the drying stage with the furnace inlet while screening ambient oxygen,
application of a water-binding medium, preferably NH
3
, or a solution thereof, onto the strip in the rinsing stage, wherein subsequently in the drying stage the water-binding medium can be removed from the strip quickly and without residue, i.e., without the introduction of oxygen or liquid cleaning medium,
alternatively by operating the drying stage with an atmosphere which has a reducing effect, for example, a N
2
H
2
gas mixture.
As a result of the measures mentioned above, the optimum strip condition is preserved after pickling up into the furnace and an optimum adjustment of the strip temperature when it is immersed into the zinc bath is achieved. The entrance of oxygen and the attendant surface reactions, particularly oxidation, are prevented. This makes it possible to operate the furnace at temperatures in the range of the melt bath temperature. An overheating of the strip and a prolongation of the holding time in the furnace do not take place. A strip cooler is not necessary. The manner of operation according to the invention and the corresponding installation generally make possible a substantially more compact construction of the furnace element and lower investment and operating costs. Simultaneously, it is possible to operate the furnace with low H
2
contents in the protective gas. The disadvantages of the conventional methods mentioned above with increased zinc bath temperature are advantageously eliminated.
This is because, in accordance with the invention, the strip is adjusted to a temperature which is at most 50° K. higher than the immersion temperature in the zinc bath.
Additional details, features and advantages of the invention result from the following explanation of an embodiment which is schematically illustrated in the drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1
shows a layout of a hot dip galvanizing installation according to the prior art,
FIG. 2
shows a layout of a hot dip galvanizing installation according to the invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
In accordance with the layout of a conventional hot dip galvanizing installation shown in
FIG. 1
, a strip
50
is introduced in a first method step into a pickling station
10
with three pickling stages
11
to
13
and a layer of scale as well as reaction products are removed from the strip surface in the pickling station. Pickling is usually carried out in the pickling station
10
or in the pickling stages
11
,
12
,
13
by means of hydrochloric acid (HCl).
In the subsequent method step, the strip
50
is introduced into the rinsing station
20
with the rinsing stages
21
to
23
and residues of the pickle and pickling products are removed in the rinsing station from the strip surface. Subsequently, the strip is introduced into and dried in the drying station
30
. From the drying station, the strip
50
is introduced in another method step into a furnace
40
which comprises a preheating stage
41
and an integrated heating stage
42
and the strip is heated in the furnace to galvanizing temperature preferably under a protective gas atmosphere. In a last method step, the strip is guided through a galvanizing bath. In the galvanizing bath, the surface of the strip
50
is coated with a hot dip galvanizing layer. In contrast to the conventional galvanizing installation according to
FIG. 1
, in accordance with the layout according to the invention of the hot dip galvanizing installation according to
FIG. 2
, the method steps between the last rinsing stage
23
of the rinsing station
20
through the drying station
30
up to the inlet
43
of the heating furnace
40
are carried out while being hermetically screened from the ambient oxygen from the surroundings.
By expanding the rinsing station
20
by a rinsing stage
23
or by screening the rinsing stage
23
by means of a separating wall
24
from the preceding rinsing stations
21
,
22
, a water-repellent or water-binding medium
25
is introduced into the rinsing stage
23
. The medium used may be, for example, NH
3
or a solution of NH
3
.
A preferred development of the method provides that rinsing of the strip
50
in the rinsing station
20
is carried out in the first stages
21
and
22
with deionized water and in the third stage
23
with the addition of NH
3
as a drying medium.
Drying of the strip
50
in the drying station
30
takes place without the supply of air. In accordance with the invention, drying is carried out by means of thermal radiation with the addition of a mixture of nitrogen, hydrogen and ammonia gas (N
2
/NH
3
) or H
2
.
The drying station
30
is hermetically closed off against the entrance of ambient oxygen on both sides by means of locks
70
,
80
adjacent the stations
20
and
40
. The outlet of the last rinsing stage
23
of the rinsing station
20
is connected to the inlet of the drying station
30
and the outlet of the drying station
30
is connected to the inlet
43
of the heating furnace
40
through locks
70
,
80
, and they are hermetically sealed from the ambient atmosphere.
The measures according to the invention maintain the optimum strip condition after pickling up to the heating furnace because the introduction of ambient oxygen is prevented. Consequently, as can be seen in the illustration of the heating furnace
40
in
FIG. 2
, the construction of the furnace can be simplified and realized with lower investment and operating costs because of the lower necessary heating power and the omission of the cooling stretch. In addition, the furnace operation is possible with comparatively low H
2
contents in the protective gas.
Claims
- 1. Method for hot dip galvanizing of hot-rolled steel strip, wherein:in a first method step, the strip (50) is introduced into a pickling station (10-13) and a layer of scale and reaction products are removed from the strip surface in the pickling station, in another method step, the strip (50) is introduced into a rinsing station (21-23) and residues of the pickle and pickling products are removed from the strip surface in the rinsing station, and subsequently the strip is introduced into a drying station and is dried, and from there in another method step, the strip is introduced into a furnace (40) and is adjusted to galvanizing temperature under a protective gas atmosphere, and in a last method step, the strip is guided through a galvanizing bath and the surface of the strip (50) is coated with a hot dip galvanizing layer in the galvanizing bath, wherein the strip temperature in the furnace (40) is adjusted at most to 50° K. above immersion temperature of the strip (50) into the zinc bath, wherein a water-repellent or water-binding medium (25) which wets the strip (50) is introduced into the last rinsing stage (23) of the rinsing station (20).
- 2. Method according to claim 1, wherein the medium (25) introduced into the third rinsing stage (23) is NH3 or a solution containing NH3.
- 3. Method according to claim 1, wherein drying of the strip (50) in the drying station (30) is carried out without the supply of air from the outside by means of heat radiation with the addition of a mixture of nitrogen, hydrogen and ammonia gas (N2/NH3)+H2 or another mixture of two of the mentioned gases.
Priority Claims (2)
Number |
Date |
Country |
Kind |
199 37 216 |
Aug 1999 |
DE |
|
199 43 238 |
Sep 1999 |
DE |
|
PCT Information
Filing Document |
Filing Date |
Country |
Kind |
PCT/EP00/07582 |
|
WO |
00 |
Publishing Document |
Publishing Date |
Country |
Kind |
WO01/11099 |
2/15/2001 |
WO |
A |
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Number |
Name |
Date |
Kind |
4143184 |
Paulus et al. |
Mar 1979 |
A |
4643131 |
Umeda et al. |
Feb 1987 |
A |
4814210 |
Ackermann et al. |
Mar 1989 |
A |
5284680 |
Bilimoria |
Feb 1994 |
A |
5677005 |
Isobe et al. |
Oct 1997 |
A |
5976272 |
Seidel et al. |
Nov 1999 |
A |
6159622 |
Hori et al. |
Dec 2000 |
A |
Foreign Referenced Citations (1)
Number |
Date |
Country |
8300885 |
Mar 1983 |
WO |